diff --git a/ravenframework/CodeInterfaceClasses/Factory.py b/ravenframework/CodeInterfaceClasses/Factory.py index 98555d99b4..7820d882a1 100644 --- a/ravenframework/CodeInterfaceClasses/Factory.py +++ b/ravenframework/CodeInterfaceClasses/Factory.py @@ -25,7 +25,6 @@ from .MAAP5.MAAP5Interface import MAAP5 from .MAMMOTH.MAMMOTHInterface import MAMMOTH from .MELCOR.melcorCombinedInterface import Melcor -from .MELCOR.melcorInterface import MelcorApp from .MooseBasedApp.BisonAndMeshInterface import BisonAndMesh from .MooseBasedApp.CubitInterface import Cubit from .MooseBasedApp.CubitMooseInterface import CubitMoose diff --git a/ravenframework/CodeInterfaceClasses/MELCOR/MELCORdata.py b/ravenframework/CodeInterfaceClasses/MELCOR/MELCORdata.py deleted file mode 100644 index 3892bd2ede..0000000000 --- a/ravenframework/CodeInterfaceClasses/MELCOR/MELCORdata.py +++ /dev/null @@ -1,152 +0,0 @@ -# Copyright 2017 University of Rome La Sapienza and Battelle Energy Alliance, LLC -# -# Licensed under the Apache License, Version 2.0 (the "License"); -# you may not use this file except in compliance with the License. -# You may obtain a copy of the License at -# -# http://www.apache.org/licenses/LICENSE-2.0 -# -# Unless required by applicable law or agreed to in writing, software -# distributed under the License is distributed on an "AS IS" BASIS, -# WITHOUT WARRANTIES OR CONDITIONS OF ANY KIND, either express or implied. -# See the License for the specific language governing permissions and -# limitations under the License. -""" - Created on April 18, 2017 - @author: Matteo Donorio (University of Rome La Sapienza), - Fabio Gianneti (University of Rome La Sapienza), - Andrea Alfonsi (INL) - - Modified on January 24, 2018 - @author: Violet Olson - Thomas Riley (Oregon State University) - Robert Shannon (Oregon State University) - Change Summary: Added Control Function parsing -""" -from __future__ import division, print_function, unicode_literals, absolute_import -import re -import copy -import numpy as np -from collections import OrderedDict - -class MELCORdata: - """ - class that parses output of MELCOR 2.1 output file and reads in trip, minor block and write a csv file - For now, Only the data associated to control volumes and control functions are parsed and output - """ - def __init__(self,filen): - """ - Constructor - @ In, filen, FileObject, the file to parse - @ Out, None - """ - self.lines = open(filen,"r").readlines() - timeBlocks = self.getTimeBlocks() - self.timeParams = self.returnVolumeHybro(timeBlocks) - self.functions = self.returnControlFunctions(timeBlocks) - - def getTimeBlocks(self): - """ - This method returns a dictionary of lists of type {"time":[lines Of Output for that time]} - @ In, None - @ Out, timeBlock, dict, {"time":[lines Of Output for that time]} - """ - lineNum = [] - timeBlock = {} - for lineNumber, line in enumerate(self.lines): - if line.strip().startswith("1*"): - lineNum.append([lineNumber,self.lines[lineNumber+1].split("=")[1].split( )[0]]) - for cnt,info in enumerate(lineNum): - endLineCnt = lineNum[cnt+1][0]-1 if cnt < len(lineNum)-1 else len(self.lines)-1 - timeBlock[info[1]] = self.lines[info[0]+1:endLineCnt] - return timeBlock - - def returnControlFunctions(self, timeBlock): - """ - CONTROL FUNCTIONS EDIT - @ In, timeBlock, dict, {"time":[lines Of Output for that time]} - @ Out, functionValuesForEachTime, dict, {"time":{"functionName":"functionValue"}} - """ - functionValuesForEachTime = {'time': []} - timeOneRegex_name = re.compile(r"^\s*CONTROL\s+FUNCTION\s+(?P[^\(]*)\s+(\(.*\))?\s*IS\s+.+\s+TYPE.*$") - timeOneRegex_value = re.compile(r"^\s*VALUE\s+=\s+(?P[^\s]*)") - startRegex = re.compile(r"\s*CONTROL\s*FUNCTION\s*NUMBER\s*CURRENT\s*VALUE") - regex = re.compile(r"^\s*(?P( ?([0-9a-zA-Z-]+))*)\s+([0-9]+)\s*(?P((([0-9.-]+)E(\+|-)[0-9][0-9])|((T|F))))\s*.*$") - for time,listOfLines in timeBlock.items(): - functionValuesForEachTime['time'].append(float(time)) - start = -1 - for lineNumber, line in enumerate(listOfLines): - if re.search(startRegex, line): - start = lineNumber + 1 - break - elif re.search(timeOneRegex_name, line): - start = -2 - break - if start > 0: - for lineNumber, line in enumerate(listOfLines[start:]): - if line.startswith(" END OF EDIT FOR CF"): - break - match = re.match(regex, line) - if match is not None: - if match.groupdict()["name"] not in functionValuesForEachTime: - functionValuesForEachTime[match.groupdict()["name"]] = [] - functionValuesForEachTime[match.groupdict()["name"]].append(float(match.groupdict()["value"])) - elif start == -2: - for lineNumber, line in enumerate(listOfLines): - fcnName = re.match(timeOneRegex_name, line) - if fcnName is not None: - fcnValue = re.match(timeOneRegex_value, listOfLines[lineNumber+1]) - if fcnValue is not None: - if fcnName.groupdict()["name"] not in functionValuesForEachTime: - functionValuesForEachTime[fcnName.groupdict()["name"]] = [] - functionValuesForEachTime[fcnName.groupdict()["name"]].append(float(fcnValue.groupdict()["value"])) - for parameter in functionValuesForEachTime: - functionValuesForEachTime[parameter] = np.asarray(functionValuesForEachTime[parameter]) - return functionValuesForEachTime - - def returnVolumeHybro(self,timeBlock): - """ - CONTROL VOLUME HYDRODYNAMICS EDIT - @ In, timeBlock, dict, {"time":[lines Of Output for that time]} - """ - volForEachTime = {'time': []} - for time,listOfLines in timeBlock.items(): - volForEachTime['time'].append(float(time)) - for cnt, line in enumerate(listOfLines): - if line.strip().startswith("VOLUME"): - headers = line.strip().split()[1:len(line.strip().split())-1] - for lineLine in listOfLines[cnt + 2:]: - if len(lineLine.strip()) < 1: - break - valueSplit = lineLine.strip().split() - volumeNumber = lineLine.strip().split()[0] - if not volumeNumber.isdigit(): - break - valueSplit = valueSplit[1:len(valueSplit)] - for paramCnt,header in enumerate(headers): - parameter = "volume_"+str(volumeNumber)+"_"+header.strip() - try: - _ = float(valueSplit[paramCnt]) - if parameter not in volForEachTime: - volForEachTime[parameter] = [] - if parameter in volForEachTime and len(volForEachTime['time']) !=len(volForEachTime[parameter]): - # there might be repetition(same variable with different units) - volForEachTime[parameter].append(float(valueSplit[paramCnt])) - except ValueError: - # in this way, the "strings" are not placed in the resulting csv - pass - for parameter in volForEachTime: - if parameter == 'volume_2_CVVELO(1)': - print("a") - volForEachTime[parameter] = np.asarray(volForEachTime[parameter]) - return volForEachTime - - def returnData(self): - """ - Method to return the data in a dictionary - @ In, None - @ Out, data, dict, the dictionary containing the data {var1:array,var2:array,etc} - """ - data = self.timeParams - data.update(self.functions) - return data diff --git a/ravenframework/CodeInterfaceClasses/MELCOR/melcorCombinedInterface.py b/ravenframework/CodeInterfaceClasses/MELCOR/melcorCombinedInterface.py index 032b82a7c1..2d101b7470 100644 --- a/ravenframework/CodeInterfaceClasses/MELCOR/melcorCombinedInterface.py +++ b/ravenframework/CodeInterfaceClasses/MELCOR/melcorCombinedInterface.py @@ -1,4 +1,4 @@ -# Copyright 2017 University of Rome La Sapienza and Battelle Energy Alliance, LLC +# Copyright 2017 Battelle Energy Alliance, LLC # # Licensed under the Apache License, Version 2.0 (the "License"); # you may not use this file except in compliance with the License. @@ -13,73 +13,103 @@ # limitations under the License. """ Created on April 18, 2017 - @author: Matteo Donorio (University of Rome La Sapienza), - Fabio Gianneti (University of Rome La Sapienza), + @author: Matteo D'Onorio (Sapienza University of Rome) Andrea Alfonsi (INL) """ + +import os +from ...contrib.melcorTools import melcorTools from ravenframework.CodeInterfaceBaseClass import CodeInterfaceBase -from .melcorInterface import MelcorApp -from .melgenInterface import MelgenApp +from ..Generic import GenericParser +import pandas as pd + class Melcor(CodeInterfaceBase): """ - this class is used a part of a code dictionary to specialize Model.Code for MELCOR 2. Version + This class is used a part of a code dictionary to specialize Model. Code for different MELCOR versions + like MELCOR 2.2x, MELCOR 1.86, MELCOR for fusion applications """ - def __init__(self): + def _readMoreXML(self,xmlNode): """ - Constructor. - @ In, None - @ Out, None + Function to read the portion of the xml input that belongs to this specialized class and initialize + some members based on inputs. This can be overloaded in specialize code interface in order to + read specific flags. + Only one option is possible. You can choose here, if multi-deck mode is activated, from which deck you want to load the results + @ In, xmlNode, xml.etree.ElementTree.Element, Xml element node + @ Out, None. """ - CodeInterfaceBase.__init__(self) - self.melcorInterface = MelcorApp() - self.melgenInterface = MelgenApp() - def findInps(self,inputFiles): + melNode = xmlNode.find('MelcorOutput') + varNode = xmlNode.find('variables') + plotNode = xmlNode.find('CodePlotFile') + + if varNode is None: + raise IOError("Melcor variables not found, define variables to print") + if plotNode is None: + raise IOError("Please define the name of the MELCOR plot file in the CodePlotFile xml node") + if melNode is None: + raise IOError("Please enter MELCOR message file name") + + self.varList = [var.strip() for var in varNode.text.split("$,")] + self.melcorPlotFile = [var.strip() for var in plotNode.text.split(",")][0] + self.melcorOutFile = [var.strip() for var in melNode.text.split(",")][0] + + return self.varList, self.melcorPlotFile, self.melcorOutFile + + def findInps(self,currentInputFiles): """ Locates the input files for Melgen, Melcor - @ In, inputFiles, list, list of Files objects - @ Out, (melgIn,melcIn), tuple, tuple containing Melgin and Melcor input files + @ In, currentInputFiles, list, list of Files objects + @ Out, (melgIn,melcIn), tuple, tuple containing Melgen and Melcor input files """ foundMelcorInp = False - for index, inputFile in enumerate(inputFiles): + for index, inputFile in enumerate(currentInputFiles): if inputFile.getExt() in self.getInputExtension(): + if foundMelcorInp: + raise IOError(f"Multiple Melcor input files are found {inputFile} and {melgIn}, please check your inputs, only one of input is accepted") foundMelcorInp = True - melgIn = inputFiles[index] - melcIn = inputFiles[index] + melgIn = currentInputFiles[index] + melcIn = currentInputFiles[index] + + if not foundMelcorInp: + raise IOError('None of the input files has one of the following extensions: ' + ' '.join(self.getInputExtension())) + if not foundMelcorInp: raise IOError("Unknown input extensions. Expected input file extensions are "+ ",".join(self.getInputExtension())+" No input file has been found!") - return melgIn,melcIn + return melgIn, melcIn + def generateCommand(self, inputFiles, executable, clargs=None, fargs=None, preExec=None): """ - Generate a command to run MELCOR (combined MELGEN AND MELCOR) - Collects all the clargs and the executable to produce the command-line call. + This method is used to retrieve the command (in tuple format) needed to launch the Code. + See base class. Collects all the clargs and the executable to produce the command-line call. Returns tuple of commands and base file name for run. Commands are a list of tuples, indicating parallel/serial and the execution command to use. - This method is used to retrieve the command (in tuple format) needed to launch the Code. - @ In, inputFiles, list, List of input files (length of the list depends on the number of inputs that have been added in the Step is running this code) + @ In, inputFiles, list, List of input files (length of the list depends on the number of inputs have been added in the Step is running this code) @ In, executable, string, executable name with absolute path (e.g. /home/path_to_executable/code.exe) @ In, clargs, dict, optional, dictionary containing the command-line flags the user can specify in the input (e.g. under the node < Code >< clargstype =0 input0arg =0 i0extension =0 .inp0/ >< /Code >) - @ In, fargs, dict, optional, a dictionary containing the axuiliary input file variables the user can specify in the input (e.g. under the node < Code >< clargstype =0 input0arg =0 aux0extension =0 .aux0/ >< /Code >) + @ In, fargs, dict, optional, a dictionary containing the auxiliary input file variables the user can specify in the input (e.g. under the node < Code >< fileargstype =0 input0arg =0 aux0extension =0 .aux0/ >< /Code >) @ In, preExec, string, optional, a string the command that needs to be pre-executed before the actual command here defined @ Out, returnCommand, tuple, tuple containing the generated command. returnCommand[0] is the command to run the code (string), returnCommand[1] is the name of the output root """ - if preExec is None: - raise IOError('No preExec listed in input! Exiting...') + found = False + + melcOut = 'OUTPUT_MELCOR' melcin,melgin = self.findInps(inputFiles) - #get the melgen part - melgCommand,melgOut = self.melcorInterface.generateCommand([melgin],preExec,clargs,fargs) - #get the melcor part - melcCommand,melcOut = self.melgenInterface.generateCommand([melcin],executable,clargs,fargs) - #combine them - returnCommand = melgCommand + melcCommand, melcOut + if clargs: + precommand = executable + clargs['text'] + else: + precommand = executable + melgCommand = str(preExec)+ ' '+melcin.getFilename() + melcCommand = precommand+ ' '+melcin.getFilename() + returnCommand = [('serial',melgCommand + ' && ' + melcCommand +' ow=o ')],melcOut + return returnCommand def createNewInput(self,currentInputFiles,origInputFiles,samplerType,**Kwargs): """ - This generates a new input file depending on which sampler has been chosen + This generates a new input file depending on which sampler is chosen @ In, currentInputFiles, list, list of current input files (input files from last this method call) @ In, oriInputFiles, list, list of the original input files @ In, samplerType, string, Sampler type (e.g. MonteCarlo, Adaptive, etc. see manual Samplers section) @@ -87,19 +117,52 @@ def createNewInput(self,currentInputFiles,origInputFiles,samplerType,**Kwargs): where RAVEN stores the variables that got sampled (e.g. Kwargs['SampledVars'] => {'var1':10,'var2':40}) @ Out, newInputFiles, list, list of newer input files, list of the new input files (modified and not) """ - return self.melcorInterface.createNewInput(currentInputFiles,origInputFiles,samplerType,**Kwargs) - def finalizeCodeOutput(self, command, output, workingDir): + if "dynamicevent" in samplerType.lower(): + raise IOError("Dynamic Event Tree-based samplers not implemented for MELCOR yet! But we are working on that.") + indexes = [] + inFiles = [] + origFiles= [] + for index,inputFile in enumerate(currentInputFiles): + if inputFile.getExt() in self.getInputExtension(): + indexes.append(index) + inFiles.append(inputFile) + for index,inputFile in enumerate(origInputFiles): + if inputFile.getExt() in self.getInputExtension(): + origFiles.append(inputFile) + parser = GenericParser.GenericParser(inFiles) + parser.modifyInternalDictionary(**Kwargs) + parser.writeNewInput(currentInputFiles,origFiles) + + return currentInputFiles + + def writeDict(self,workDir): + """ + Output the parsed results into a CSV file + @ In, workDir, str, current working directory + @ Out, dictionary, dict, dictioanry containing the data generated by MELCOR + """ + fileDir = os.path.join(workDir,self.melcorPlotFile) + time,data,varUdm = melcorTools.MCRBin(fileDir,self.varList) + dfTime = pd.DataFrame(time, columns= ["Time"]) + dfData = pd.DataFrame(data, columns = self.varList) + df = pd.concat([dfTime, dfData], axis=1, join='inner') + df.drop_duplicates(subset="Time",keep='first',inplace=True) + dictionary = df.to_dict(orient='list') + return dictionary + + def finalizeCodeOutput(self,command,output,workingDir): """ This method is called by the RAVEN code at the end of each run (if the method is present, since it is optional). - In this method the MELCOR outputfile is parsed and a CSV is created + It can be used for those codes, that do not create CSV files to convert the whatever output format into a csv @ In, command, string, the command used to run the just ended job @ In, output, string, the Output name root @ In, workingDir, string, current working dir - @ Out, output, string, optional, present in case the root of the output file gets changed in this method. + @ Out, response, dict, dictionary containing the data """ - output = self.melcorInterface.finalizeCodeOutput(command,output, workingDir) - return output + response = self.writeDict(workingDir) + return response + def checkForOutputFailure(self,output,workingDir): """ @@ -107,10 +170,20 @@ def checkForOutputFailure(self,output,workingDir): This method needs to be implemented by the codes that, if the run fails, return a return code that is 0 This can happen in those codes that record the failure of the job (e.g. not converged, etc.) as normal termination (returncode == 0) This method can be used, for example, to parse the outputfile looking for a special keyword that testifies that a particular job got failed - (e.g. in MELCOR would be the expression "Normal termination") + (e.g. in RELAP5 would be the keyword "********") @ In, output, string, the Output name root @ In, workingDir, string, current working dir @ Out, failure, bool, True if the job is failed, False otherwise """ - failure = self.melcorInterface.checkForOutputFailure(output, workingDir) + failure = True + goodWord = "Normal termination" # This is for MELCOR 2.2 (todo: list for other MELCOR versions) + try: + outputToRead = open(os.path.join(workingDir,self.melcorOutFile),"r") + except FileNotFoundError: + return failure + readLines = outputToRead.readlines() + lastRow = readLines[-1] + if goodWord in lastRow: + failure = False + outputToRead.close() return failure diff --git a/ravenframework/CodeInterfaceClasses/MELCOR/melcorInterface.py b/ravenframework/CodeInterfaceClasses/MELCOR/melcorInterface.py deleted file mode 100644 index 5bc97e0bf3..0000000000 --- a/ravenframework/CodeInterfaceClasses/MELCOR/melcorInterface.py +++ /dev/null @@ -1,125 +0,0 @@ -# Copyright 2017 University of Rome La Sapienza and Battelle Energy Alliance, LLC -# -# Licensed under the Apache License, Version 2.0 (the "License"); -# you may not use this file except in compliance with the License. -# You may obtain a copy of the License at -# -# http://www.apache.org/licenses/LICENSE-2.0 -# -# Unless required by applicable law or agreed to in writing, software -# distributed under the License is distributed on an "AS IS" BASIS, -# WITHOUT WARRANTIES OR CONDITIONS OF ANY KIND, either express or implied. -# See the License for the specific language governing permissions and -# limitations under the License. -""" - Created on April 18, 2017 - @author: Matteo Donorio (University of Rome La Sapienza) -""" -import os -import copy -import sys -from . import MELCORdata -from ravenframework.utils import utils -from ..Generic import GenericParser -from .melgenInterface import MelgenApp -from ravenframework.CodeInterfaceBaseClass import CodeInterfaceBase - -class MelcorApp(CodeInterfaceBase): - """ - This class is the CodeInterface for MELCOR - """ - def __init__(self): - """ - Constructor - @ In, None - @ Out, None - """ - CodeInterfaceBase.__init__(self) - self.melgenApp = MelgenApp() - self.inputExtensions = ['i','inp'] - - def generateCommand(self, inputFiles, executable, clargs=None, fargs=None, preExec=None): - """ - Generate a command to run MELCOR - Collects all the clargs and the executable to produce the command-line call. - Returns tuple of commands and base file name for run. - Commands are a list of tuples, indicating parallel/serial and the execution command to use. - This method is used to retrieve the command (in tuple format) needed to launch the Code. - @ In, inputFiles, list, List of input files (length of the list depends on the number of inputs that have been added in the Step is running this code) - @ In, executable, string, executable name with absolute path (e.g. /home/path_to_executable/code.exe) - @ In, clargs, dict, optional, dictionary containing the command-line flags the user can specify in the input (e.g. under the node < Code >< clargstype =0 input0arg =0 i0extension =0 .inp0/ >< /Code >) - @ In, fargs, dict, optional, a dictionary containing the axuiliary input file variables the user can specify in the input (e.g. under the node < Code >< clargstype =0 input0arg =0 aux0extension =0 .aux0/ >< /Code >) - @ In, preExec, string, optional, a string the command that needs to be pre-executed before the actual command here defined - @ Out, returnCommand, tuple, tuple containing the generated command. returnCommand[0] is the command to run the code (string), returnCommand[1] is the name of the output root - """ - subReturnCommand = self.melgenApp.generateCommand(inputFiles, executable, clargs, fargs) - outputfile = 'GEN_OUTPUT' - returnCommand = subReturnCommand[0],outputfile - return returnCommand - - def createNewInput(self,currentInputFiles,origInputFiles,samplerType,**Kwargs): - """ - This generates a new input file depending on which sampler has been chosen - @ In, currentInputFiles, list, list of current input files (input files from last this method call) - @ In, oriInputFiles, list, list of the original input files - @ In, samplerType, string, Sampler type (e.g. MonteCarlo, Adaptive, etc. see manual Samplers section) - @ In, Kwargs, dictionary, kwarded dictionary of parameters. In this dictionary there is another dictionary called "SampledVars" - where RAVEN stores the variables that got sampled (e.g. Kwargs['SampledVars'] => {'var1':10,'var2':40}) - @ Out, newInputFiles, list, list of newer input files, list of the new input files (modified and not) - """ - if "dynamicevent" in samplerType.lower(): - raise IOError("Dynamic Event Tree-based samplers not implemented for MELCOR yet!") - indexes = [] - inFiles = [] - origFiles= [] - #FIXME possible danger here from reading binary files - for index,inputFile in enumerate(currentInputFiles): - if inputFile.getExt() in self.getInputExtension(): - indexes.append(index) - inFiles.append(inputFile) - for index,inputFile in enumerate(origInputFiles): - if inputFile.getExt() in self.getInputExtension(): - origFiles.append(inputFile) - parser = GenericParser.GenericParser(inFiles) - parser.modifyInternalDictionary(**Kwargs) - parser.writeNewInput(currentInputFiles,origFiles) - return currentInputFiles - - def finalizeCodeOutput(self,command,output,workingDir): - """ - This method is called by the RAVEN code at the end of each run (if the method is present, since it is optional). - In this method the MELCOR outputfile is parsed and a CSV is created - @ In, command, string, the command used to run the just ended job - @ In, output, string, the Output name root - @ In, workingDir, string, current working dir - @ Out, response, dict, the data dictionary {var1:array,var2:array, etc} - """ - outfile = os.path.join(workingDir,output+'.out') - outputobj=MELCORdata.MELCORdata(outfile) - response = outputobj.returnData() - return response - - def checkForOutputFailure(self,output,workingDir): - """ - This method is called by the RAVEN code at the end of each run if the return code is == 0. - This method needs to be implemented by the codes that, if the run fails, return a return code that is 0 - This can happen in those codes that record the failure of the job (e.g. not converged, etc.) as normal termination (returncode == 0) - This method can be used, for example, to parse the outputfile looking for a special keyword that testifies that a particular job got failed - (e.g. in MELCOR would be the expression "Normal termination") - @ In, output, string, the Output name root - @ In, workingDir, string, current working dir - @ Out, failure, bool, True if the job is failed, False otherwise - """ - failure = True - errorWord = ["Normal termination"] - try: - outputToRead = open(os.path.join(workingDir,output+'.out'),"r") - except IOError: - # the output does not exist => MELCOR failed - return failure - readLines = outputToRead.readlines() - for goodMsg in errorWord: - if any(goodMsg in x for x in readLines): - failure = False - break - return failure diff --git a/ravenframework/CodeInterfaceClasses/MELCOR/melgenInterface.py b/ravenframework/CodeInterfaceClasses/MELCOR/melgenInterface.py deleted file mode 100644 index 6695d6d57a..0000000000 --- a/ravenframework/CodeInterfaceClasses/MELCOR/melgenInterface.py +++ /dev/null @@ -1,69 +0,0 @@ -# Copyright 2017 University of Rome La Sapienza and Battelle Energy Alliance, LLC -# -# Licensed under the Apache License, Version 2.0 (the "License"); -# you may not use this file except in compliance with the License. -# You may obtain a copy of the License at -# -# http://www.apache.org/licenses/LICENSE-2.0 -# -# Unless required by applicable law or agreed to in writing, software -# distributed under the License is distributed on an "AS IS" BASIS, -# WITHOUT WARRANTIES OR CONDITIONS OF ANY KIND, either express or implied. -# See the License for the specific language governing permissions and -# limitations under the License. -""" - Created on April 18, 2017 - @author: Matteo Donorio (University of Rome La Sapienza) - This is a utility class for the creation of the command. - It is not an interface that can work on its own -""" -from __future__ import division, print_function, unicode_literals, absolute_import - -import os -from ravenframework.utils import utils - -class MelgenApp(): - """ - This class is the CodeInterface for MELGEN (a sub-module of Melcor) - """ - def __init__(self): - """ - Constructor - @ In, None - @ Out, None - """ - self.inputExtensions = ['i','inp'] - - def generateCommand(self,inputFiles,executable,clargs=None,fargs=None,preExec=None): - """ - Generate a command to run MELGEN (a sub-module of Melcor) - Collects all the clargs and the executable to produce the command-line call. - Returns tuple of commands and base file name for run. - Commands are a list of tuples, indicating parallel/serial and the execution command to use. - This method is used to retrieve the command (in tuple format) needed to launch the Code. - @ In, inputFiles, list, List of input files (length of the list depends on the number of inputs that have been added in the Step is running this code) - @ In, executable, string, executable name with absolute path (e.g. /home/path_to_executable/code.exe) - @ In, clargs, dict, optional, dictionary containing the command-line flags the user can specify in the input (e.g. under the node < Code >< clargstype =0 input0arg =0 i0extension =0 .inp0/ >< /Code >) - @ In, fargs, dict, optional, a dictionary containing the axuiliary input file variables the user can specify in the input (e.g. under the node < Code >< clargstype =0 input0arg =0 aux0extension =0 .aux0/ >< /Code >) - @ In, preExec, string, optional, a string the command that needs to be pre-executed before the actual command here defined - @ Out, returnCommand, tuple, tuple containing the generated command. returnCommand[0] is the command to run the code (string), returnCommand[1] is the name of the output root - """ - outputfile = 'OUTPUT_MELCOR' - found = False - - for index, inputFile in enumerate(inputFiles): - if inputFile.getExt() in self.inputExtensions: - found = True - break - if not found: - raise IOError("Unknown input extension. Expected input file extensions are "+ ",".join(self.inputExtensions)) - if clargs: - precommand = executable + clargs['text'] - else : - precommand = executable - executeCommand = [('serial',precommand + ' '+inputFiles[index].getFilename())] - returnCommand = executeCommand, outputfile - return returnCommand - - - diff --git a/ravenframework/Models/PostProcessors/SubdomainBasicStatistics.py b/ravenframework/Models/PostProcessors/SubdomainBasicStatistics.py index 646294e2e1..8f1e601cb6 100644 --- a/ravenframework/Models/PostProcessors/SubdomainBasicStatistics.py +++ b/ravenframework/Models/PostProcessors/SubdomainBasicStatistics.py @@ -137,12 +137,12 @@ def initialize(self, runInfo, inputs, initDict): self.gridEntity.initialize({'computeCells': True,'constructTensor': True,}) # check that the grid is defined only in the input space. dims = self.gridEntity.returnParameter("dimensionNames") - inputs = inputs[-1].getVars("input") - if not all(item in inputs for item in dims): - unset = ', '.join(list(set(dims) - set(inputs))) - self.raiseAnError(RuntimeError, "Subdomain grid must be defined on the input space only (inputs)." - f"The following variables '{unset}' are not part of the input space of DataObject {inputs[-1].name}!") - + inputVars = inputs[-1].getVars("input") + if not all(item in inputVars for item in dims): + unset = ', '.join(list(set(dims) - set(inputVars))) + self.raiseAnError(RuntimeError, ("Subdomain grid must be defined on the input space only (inputs)." + f"The following variables '{unset}' are not part " + f"of the input space of DataObject {inputs[-1].name}!")) def _handleInput(self, paramInput): """ diff --git a/ravenframework/contrib/melcorTools/melcorTools.py b/ravenframework/contrib/melcorTools/melcorTools.py new file mode 100644 index 0000000000..0a10f455a8 --- /dev/null +++ b/ravenframework/contrib/melcorTools/melcorTools.py @@ -0,0 +1,116 @@ +""" + MELCOR FORMAT SUPPORT MODULE + Created on March 28, 2017 + Last update on October 14, 2022 + @authors: + Matteo D'Onorio (University of Rome La Sapienza) + Paolo Balestra (University of Rome La Sapienza) +""" +# =============================================================================== +def MCRBin(fileDir, VarSrch): + """ + This method is called to collect the variables to be used in the postprocess + @ In, fileDir, string, the file directory. This is the directory of the MELCOR plot file + @ In, VarSrch, list, list of variables to be collected + @ Out, Data, tuple (numpy.ndarray,numpy.ndarray,numpy.ndarray), this contains the extracted data for each declared variable + from MELCOR output file. The first variables indicates the + time arrays, the second one indicates the arryas of the melcor + output variables + """ + from struct import unpack + import numpy as np + from collections import Counter + HdrList = [] + BlkLenBef = [] + BlkLenAft = [] + DataPos=[] + cntr = 0 + Var_dict = {} + with open(fileDir, 'rb') as bf: + while True: + BlkLenBefSlave = bf.read(4) + if not BlkLenBefSlave: + break + BlkLenBef.append(unpack('I', BlkLenBefSlave)[0]) + if BlkLenBef[cntr] == 4: + HdrList.append(str(unpack('4s', bf.read(4))[0], 'utf-8')) + elif HdrList[cntr - 1] == 'TITL': + probemTitle=str(unpack('%d' % BlkLenBef[cntr] + 's', bf.read(BlkLenBef[cntr]))[0], 'utf-8') + HdrList.append([]) + elif HdrList[cntr - 1] == 'KEY ': + VarName=unpack('2I', bf.read(8)) + HdrList.append([]) + elif HdrList[cntr - 2] == 'KEY ': + a = BlkLenBef[-1]/VarName[0] + stringa=str(int(a))+"s" + VarNam=[str(i, 'utf-8') for i in unpack(stringa * VarName[0], bf.read(BlkLenBef[cntr]))] + HdrList.append([]) + elif HdrList[cntr - 3] == 'KEY ': + VarPos=unpack('%d' % VarName[0] + 'I', bf.read(BlkLenBef[cntr])) + HdrList.append([]) + elif HdrList[cntr - 4] == 'KEY ': + VarUdm=[str(i, 'utf-8') for i in unpack('16s' * VarName[0], bf.read(BlkLenBef[cntr]))] + HdrList.append([]) + elif HdrList[cntr - 5] == 'KEY ': + VarNum=unpack('%d' % VarName[1] + 'I', bf.read(BlkLenBef[cntr])) + VarNameFull=[] + VarUdmFull=[] + NamCntr=0 + VarPos = VarPos + (VarName[1]+1,) + VarSrchPos=[0] + itm_x_Var = [] + for k in range(0,len(VarNam)): + itm_x_Var.append(VarPos[k+1]-VarPos[k]) + if len(itm_x_Var) != len(VarNam): + print("MelcorTools: Number of variables different from number of items of offset array") + print(itm_x_Var) + print(len(VarNam)) + break + Items_Tot = sum(itm_x_Var) + if Items_Tot != len(VarNum): + print("MelcorTools: The Sum of the items to be associated with each variable is different from the sum of all items id VarNum") + VarNum_Cntr =0 + Var_dict = {} + for i,Var in enumerate(VarNam): + NumOfItems = itm_x_Var[i] + end = VarNum_Cntr + NumOfItems + Var_dict[Var] = list(VarNum[VarNum_Cntr:end]) + VarNum_Cntr = VarNum_Cntr+NumOfItems + for key in Var_dict.keys(): + for element in Var_dict[key]: + if element == 0: + VarNameFull.append(str(key).strip()) + else: + VarNameFull.append(key.strip()+'_%d' %element) + for i,item in enumerate(itm_x_Var): + for k in range(0,item): + VarUdmFull.append(VarUdm[i].strip()) + VarNameFull=['TIME','CPU','DT','UNKN03']+VarNameFull + VarUdmFull=['sec','','','']+VarUdmFull + for Nam in VarSrch: + VarSrchPos.append(VarNameFull.index(Nam.strip())) + VarUdmFull=[VarUdmFull[i] for i in VarSrchPos] + SwapPosVarSrch=sorted(range(len(VarSrchPos)), key=lambda k: VarSrchPos[k]) + SwapPosVarSrch=sorted(range(len(SwapPosVarSrch)), key=lambda k: SwapPosVarSrch[k]) + VarSrchPos.sort() + VarSrchPos.append(VarName[1]+4) + HdrList.append([]) + elif HdrList[cntr - 1] == '.TR/': + DataPos.append(bf.tell()) + bf.seek(BlkLenBef[cntr], 1) + HdrList.append([]) + else: + HdrList.append([]) + BlkLenAft.append(unpack('I', bf.read(4))[0]) + + cntr +=1 + + data=np.empty([len(DataPos), len(VarSrch)+1])*np.nan + with open(fileDir, 'rb') as bf: + for i,Pos in enumerate(DataPos): + bf.seek(Pos, 0) + for j in range(len(VarSrchPos)-1): + data[i,j]=unpack('f', bf.read(4))[0] + bf.seek((VarSrchPos[j+1]-VarSrchPos[j])*4-4, 1) + data=data[:,SwapPosVarSrch] + return data[:,0],data[:,1:],VarUdmFull[1:] diff --git a/tests/framework/CodeInterfaceTests/MelcorInterface/test.i b/tests/framework/CodeInterfaceTests/MelcorInterface/test.i index e8ca01a174..a4c659f185 100644 --- a/tests/framework/CodeInterfaceTests/MelcorInterface/test.i +++ b/tests/framework/CodeInterfaceTests/MelcorInterface/test.i @@ -12,7 +12,7 @@ MEL_OUTPUTFILE 'OUTPUT_MELCOR.out' !EXTDIAGFILE 'EXTDIAG.TXT' ! !************************************************* -!'test_1' +! 'test_1' * !************************************************* ! ! @@ -55,13 +55,12 @@ TF_TAB 2 !n x y 2 100.0 1. ! CF_INPUT ! -CF_ID 'ZERO' 01 EQUALS ! +CF_ID 'ZERO' 1 EQUALS ! CF_SAI 1.0 0.0 0.0 ! CFSCAL CFADCN CFVALR (INITIAL VALUE) CF_ARG 1 ! NARG CHARG ARSCAL ARADCN 1 EXEC-TIME 0.0 0.0 ! -CF_INPUT ! -CF_ID 'Tes CF' 02 EQUALS ! +CF_ID 'Test_CF' 2 EQUALS ! CF_SAI 1.0 0.0 0.0 ! CFSCAL CFADCN CFVALR (INITIAL VALUE) CF_ARG 1 ! NARG CHARG ARSCAL ARADCN 1 EXEC-TIME 2.0 1.0 @@ -69,7 +68,6 @@ CF_ARG 1 ! NARG CHARG ARSCAL ARADCN ! CVH_INPUT ! -! ! cvname icvnum CV_ID 'IN' 1 ! icvthr ipfsw icvact @@ -152,10 +150,10 @@ Program MELCOR !* Block: MEX (Exec) data **************************** EXEC_INPUT EXEC_TITLE test_1 ! Title of the calculation -EXEC_TEND 10.0E+03 !* ! End of calculation time +EXEC_TEND 10.0E+02 !* ! End of calculation time EXEC_TIME 2 !*NUMBER TIME DTMAX DTMIN DTEDT DTPLT DTRST DCRST - 1 0.00 0.1000E+00 0.10000E-06 2.50000E+03 1.00000E+01 1.00000E+03 0.10000000E+11 - 2 1.50000E+02 0.2000E+00 0.10000E-09 2.50000E+03 1.00000E+01 1.0000E+03 0.10000000E+11 + 1 0.00 0.5000E+00 0.10000E-06 2.50000E+03 1.00000E+01 1.00000E+03 0.10000000E+11 + 2 1.50000E+03 0.5000E+00 0.10000E-09 2.50000E+03 1.00000E+01 1.0000E+03 0.10000000E+11 EXEC_CPULEFT 1000. ! cpu sec left at end of calculation EXEC_CPULIM 4000000. ! Maximum number of CPU seconds allowed for this execution diff --git a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/1/MELMES_v2-0 b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/1/MELMES_v2-0 new file mode 100644 index 0000000000..3f1dc1c8dd --- /dev/null +++ b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/1/MELMES_v2-0 @@ -0,0 +1,9 @@ + MELCOR message output TWBKAGZ 2/20/23 10:03:01 + TEST_1 + Listing written TIME= 0.00000E+00 CYCLE= 0 + Relative Energy Error 1.320451326020530E-263 +Begin normal termination + Time 1000.04218279900 + CPU 0.141447000000000 + CVH-H2O-RELERR 2.362551580189640E-013 + Normal termination TIME= 1.00004E+03 CYCLE= 2017 CPU = 1.41447E-01 diff --git a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/1/MELPTF.PTF b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/1/MELPTF.PTF new file mode 100644 index 0000000000..e0ffe4dfdc Binary files /dev/null and b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/1/MELPTF.PTF differ diff --git a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/1/OUTPUT_MELCOR.out b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/1/OUTPUT_MELCOR.out deleted file mode 100644 index f38dd32bf2..0000000000 --- a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/1/OUTPUT_MELCOR.out +++ /dev/null @@ -1,2222 +0,0 @@ - COMMAND-LINE: /usr/local/neapps/melcor/melcor_2_2/melcor i=test.i - COMMAND-LINE ARGUMENTS: - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - This is an official build. - MELCOR 2.2.10167 - Executing on: Intel(R) Xeon(R) CPU E5-2670 v3 @ 2.30GHz - Configuration information: - Configuration RL_NL_CHECKALL - Subversion revision: 10167 - - Build Processor: Intel(R) Xeon(R) CPU E5-2643 v2 @ 3.50GHz - - Compiler: Intel(R) Visual Fortran Compiler Professional for applications runnin - g on IA-32, Version 11.1 Build 20100414 - - Compiler settings: - /fpp /nologo /O2 /Oy- /DNIGHTLY_TESTING /DLICENSING_INACTIVE /DWINDOWS /DARCH_I - NT /DGET_CPU_INFO /DINTEROP /I..\compiled_modules /check:all /check:uninit /ch - eck:noarg_temp_created /check:nooutput_conversion /assume:nocc_omp /assume:prot - ect-parens /noaltparam /error_limit:25 /warn:errors /real_size:64 /Qauto /Qpre - c-div /Qprec-sqrt /libs:static /threads /iface:cvf /align:rec8byte /align:dcomm - ons /align:records /traceback /fp:source /module:..\compiled_modules /warn:noal - ign /debug:all /Qdiag-disable:8291 /F20000000 /Qmkl:sequential /fpe0 - - Linker settings: - /NODEFAULTLIB:LIBCMT /LIBPATH:..\RL_NL_CHECKALL_Library /LIBPATH:C:\Program Fil - es (x86)\Microsoft SDKs\Windows\v7.1A\Lib /LIBPATH:C:\Program Files (x86)\Inte - l\Compiler\11.1\065\lib\ia32 /LIBPATH:..\lib - - !!!LICENSING HAS BEEN DISABLED!!! - - -MELCOR OUTPUT FILENAMES - TEXT OUTPUT: OUTPUT_MELCOR.out - DIAGNOSTIC FILE: MELDIA_v2-0 - EXTENDED DIAGNOSTIC FILE: extDIAG_v2-0 - RESTART FILE: MELRST_v2-0 - PLOTFILE: MELPTF.PTF - STOP FILE: MELSTP_v2-0 - MESSAGE FILE: MELMES_v2-0 - STATUS FILE: MELSTT_v2-0 - PAUSE FILE: PAUSEFN - CFEXFILE: CFEXFILE - CFEXWRITE: CFEXWRITE - - - Opening user input file test.i - - Computer environment = ANY - - WWWWWWWWWWWWW MELCOR input WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW - - - 1 Input file: test.i - 2 *m: SNAP:Symbolic Nuclear Analysis Package, Version 2.4.0, July 09, 2015 - 3 *m: PLUGIN:MELCOR Version 2.3.0 - 4 *m: CODE:MELCOR Version 2.1 - 5 *m: DATE:12/16/16 - 6 ! - 7 !MEG_DIAGFILE 'MEGDIA.TXT' - 8 !MEG_OUTPUTFILE 'MEGOUT.TXT' - 9 MEL_OUTPUTFILE 'OUTPUT_MELCOR.out' - 10 !MEG_RESTARTFILE 'MELRST.RST' - 11 !PLOTFILE 'MELPTF.PTF' - 12 !MESSAGEFILE 'MELMES.TXT' - 13 !EXTDIAGFILE 'EXTDIAG.TXT' - 14 ! - 15 !************************************************* - 16 !'test_1' - 17 !************************************************* - 18 ! - 19 ! - 20 ! - 21 !* Block: MEX (Exec) data **************************** - 22 EXEC_INPUT - 23 EXEC_TITLE test_1 ! Title of the calculation - 24 EXEC_TEND 10.0E+03 !* ! End of calculation time - 25 EXEC_TIME 2 !*NUMBER TIME DTMAX DTMIN DTEDT DTPLT DTRST DCRST - 26 1 0.00 0.1000E+00 0.10000E-06 2.50000E+03 1.00000E+01 1.00000E+03 0.10000000E+11 - 27 2 1.50000E+02 0.2000E+00 0.10000E-09 2.50000E+03 1.00000E+01 1.0000E+03 0.10000000E+1 - 28 - 29 EXEC_CPULEFT 1000. ! cpu sec left at end of calculation - 30 EXEC_CPULIM 4000000. ! Maximum number of CPU seconds allowed for this executio - 31 EXEC_NOFLUSH ! Suppress Explicit Buffer Flushing - 32 EXEC_CYMESF 100 1000 1 1 - 33 !* END MEX (Exec) ****************************** - 34 ! - 35 !*CVH_INPUT - 36 !*CVH_TRACE 3 - 37 - Time= 0.0000E+00 Dt= 1.0000E-04 Cycle= 0 (MEX) - ERROR IN MEXSET - - - TITLES DO NOT MATCH TO SPECIFIED LENGTH - /TEST_1 - /test_1 - - - RUN TITLE : TEST_1 - - RUN ID : IRDKESE 4/09/18 10:52:56 -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during MELCOR input processing EXEC package: - - MEGEDG 1111, IOUTSW 4 - - - TIME STEP AND EDIT INTERVALS (S) - - TIME DTMAX DTMIN DTEDIT DTPLOT DTRESTART - 0.0000E+00 - 1.0000E-01 1.0000E-07 2.5000E+03 1.0000E+01 1.0000E+03 - 1.5000E+02 - 2.0000E-01 1.0000E-10 2.5000E+03 1.0000E+01 1.0000E+03 - 1.0000E+04 ( = TEND ) - - - NO EXACT TIME VALUES REQUESTED - - SOFTDTMIN UNDERRUN NOT ALLOWED - - FORCEPLOT DT REDUCTION FOR EXTRA FORCED PLOT DUMP = 2.00000E-01 - MAXIMUM NUMBER OF EXTRA PLOT DUMPS PER EXECUTION = 20 - - RESTART REQUESTED FROM LAST AVAILABLE CYCLE - or FIRST TIME >= 0.0000E+00 - - CPU LIMIT FOR EXECUTION = 4.00000E+06 - - CPU LEFT AT TERMINATION = 1.00000E+03 - - FILE MESSAGE LEVEL FOR LIST - STANDARD OUTPUT 2 - DIAGNOSTIC OUTPUT 2 - TERMINAL OUTPUT -1 - -NO Errors during MELCOR input processing EXEC package - MEX PACKAGE IS ACTIVE - NCG PACKAGE IS ACTIVE - CVH PACKAGE IS ACTIVE - FL PACKAGE IS ACTIVE - CVT PACKAGE IS ACTIVE - INP PACKAGE IS ACTIVE - CRA PACKAGE IS ACTIVE - CF PACKAGE IS ACTIVE - TF PACKAGE IS ACTIVE - MES PACKAGE IS ACTIVE - H2O PACKAGE IS ACTIVE - SC PACKAGE IS ACTIVE - ESF PACKAGE IS ACTIVE -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during PASS2 input processing CF package: -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during MELCOR PASS2 input processing EXEC package: -NO Errors during MELCOR PASS2 input processing EXEC package -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during MELCOR PASS2 input processing ESF package: -NO Errors during MELCOR PASS2 input processing ESF package - - - GRAPHICS KEY DIRECTORY - - CFVALU CVH-ATM-FR CVH-CLIQLEV - CVH-CPUC CVH-CPUE CVH-CPUR - CVH-CPUT CVH-CVOLLIQ CVH-E - CVH-E.1 CVH-E.2 CVH-E.3 - CVH-ECV CVH-ECV.1 CVH-ECV.2 - CVH-ECV.3 CVH-GR-ATMS CVH-GR-POOL - CVH-H CVH-H.1 CVH-H.2 - CVH-H.3 CVH-H2O-ERR CVH-H2O-ERR0 - CVH-LIQLEV CVH-MASS CVH-MASS.1 - CVH-MASS.2 CVH-MASS.3 CVH-NCYCLE - CVH-P CVH-PPART.1 CVH-PPART.2 - CVH-PPART.3 CVH-PR-ATMS CVH-PR-POOL - CVH-PSAT(TLIQ) CVH-PSAT(TVAP) CVH-QUALITY - CVH-RHO CVH-RHO.1 CVH-RHO.2 - CVH-RHO.3 CVH-SC-ATMS CVH-TLIQ - CVH-TOT-E CVH-TOT-M CVH-TSAT(A) - CVH-TSAT(P) CVH-TVAP CVH-VELLIQCV - CVH-VELVAPCV CVH-VIRVOLIQ CVH-VIRVOVAP - CVH-VOID-P CVH-VOID-T CVH-VOIDSG - CVH-VOLFOG CVH-VOLLIQ CVH-VOLVAP - CVH-X.3 FL-CHOKE FL-CONDITION - FL-EFLOW.A FL-EFLOW.P FL-I-EFLOW.A - FL-I-EFLOW.P FL-I-H2O-MFLOW FL-I-MFLOW.1 - FL-I-MFLOW.2 FL-I-MFLOW.3 FL-MFLOW - FL-MFLOW.1 FL-MFLOW.2 FL-MFLOW.3 - FL-PMP-QFLO FL-VELLIQ FL-VELVAP - FL-VOID GLOBALENERGYERR LOCALWARP - Messages Messages-Details WARP - - - ** ** ** ** ** ** ** ** - ** RESTART SETUP COMPLETE ** - ** ** ** ** ** ** ** ** - - -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 0.0000E+00 s = 0.0000E+00 min = 0.0000E+00 hrs = 0.0000E+00 days - DT(LAST)= 1.000000E-04 s CYCLE= 0 CPU TIME= 3.0000E-06 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKESE 4/09/18 10:52:56 - - TEST_1 - CYCLES/CPU = 0.00000E+00 (1/s) TIME/CPU= 0.00000E+00 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = 0.00000E+00 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = 0.00000E+00 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 3.41469E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - - NON-CONDENSIBLE GAS TIME INDEPENDENT DATA EDIT - - - - - 3 MATERIALS ARE DEFINED FOR THIS CALCULATION - - MATERIAL MATERIAL MOLECULAR INTERNAL - NUMBER NAME WEIGHT ENERGY ZERO - (KG/MOL) (J/KG) - - 1 POOL 1.8016E-02 0.0000E+00-ELV - 2 FOG 1.8016E-02 0.0000E+00-ELV - 3 H2O-VAP 1.8016E-02 0.0000E+00 - - - - MATERIAL CONSTANTS FOR CV(T) - - NUMB CV0 CV1 CV2 CV3 CVSQRT - J/KG-K J/KG-K**2 J/KG-K**3 J/KG-K**4 J/KG-K**(3/2) - CVM1 CVM2 TLOW TUP - J/KG J-K/KG K K - - 3 1.507E+03 0.000E+00 0.000E+00 0.000E+00 0.000E+00 - 0.000E+00 0.000E+00 1.000E+00 1.000E+04 - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.1000E+01 1.1000E+01 1.4956E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8423E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 5.82126E+04 5.82126E+04 0.00000E+00 0.00000E+00 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 3.4147E+10 3.4147E+10 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 0.0000E+00 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT 0.0000E+00 0.0000E+00 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 0 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 0 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 1.13900E-03 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 0.00000E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 1.00000E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 1.39000E-04 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 0 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 0 - PRESENT SUBCYCLE TIMESTEP = 0.00000E+00 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 1.0000E+00 1.0000E+00 0.0000E+00 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 0.0000E+00 0.0000E+00 0.0000E+00 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 12 FP2_3 CENTR OUT 1 POOL 0.00000E+00 0.00000E+00 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 5.0000E-01 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 0.0000E+00 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ****************************************** - * * - * FLOW PATH TIME INDEPENDENT DATA EDIT * - * * - ****************************************** - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME ORIENTATION FLOW TYPE OTHER SPARC FLASH - MODEL FM TO FM TO - 11 FP1_2 IN CENTR VERTICAL NORMAL V(T) N N N N - 12 FP2_3 CENTR OUT VERTICAL NORMAL N N N N - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME JUNCTION ELEVATION LENGTH AREA FRACT OPEN - FM (M) TO (M) (M) (M**2) (-) - 11 FP1_2 IN CENTR 1.0500E+01 1.0500E+01 1.0000E+01 1.0000E+00 1.0000E+00 - 12 FP2_3 CENTR OUT 1.0500E+01 1.0500E+01 1.0000E+01 1.0000E+00 1.0000E+00 - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME 'FM' JUNCTION OPENING 'TO' JUNCTION OPENING MOM.EXCH.L - BOTTOM (M) TOP (M) BOTTOM (M) TOP (M) (M) - 11 FP1_2 IN CENTR 1.0218E+01 1.0782E+01 1.0218E+01 1.0782E+01 5.6419E-01 - 12 FP2_3 CENTR OUT 1.0218E+01 1.0782E+01 1.0218E+01 1.0782E+01 5.6419E-01 - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME LOSS COEFFICIENT DISCHARGE COEFFICIENT - FWD (-) REV (-) FWD (-) REV (-) - 11 FP1_2 IN CENTR 1.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 CENTR OUT 1.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - - - Number FLOW PATH FROM VOLUME TO VOLUME SEG AREA SEG LEN HYD DIA ROUGHNESS F.LAMINAR - (M**2) (M) (M) (M) (-) - 11 FP1_2 IN CENTR 1.0000E+00 1.0000E+01 1.0000E+00 5.0000E-05 1.6000E+01 - 12 FP2_3 CENTR OUT 1.0000E+00 1.0000E+01 1.0000E+00 5.0000E-05 1.6000E+01 - - - *** CONTROL VOLUME CONNECTIVITY DATA *** - VOLUME CONNECTING FLOW PATH VOLUME - IN FP1_2 TO CENTR - CENTR FP1_2 FROM IN - FP2_3 TO OUT - OUT FP2_3 FROM CENTR - - IHX PACKAGE IS NOT ACTIVE - - - MCH PACKAGE IS NOT ACTIVE - - - CCF PACKAGE IS NOT ACTIVE - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 0 - NUMBER OF CONTROL VOLUMES PROCESSED = 0 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 0 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 0 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - -CONTROL FUNCTION ORDER OF EVALUATION - 1 ZERO (CF 1) - 2 Test CF (CF 2) - - - CONTROL FUNCTION ZERO (CF 1) IS REAL TYPE EQUALS - VALUE = 0.0000E+00 - SCALE FACTOR = 1.0000E+00 ADDITIVE CONSTANT = 0.0000E+00 - UPPER BOUND = 3.4028E+38 LOWER BOUND = -3.4028E+38 - NUMBER OF ARGUMENTS = 1 - ARGUMENT NUMBER = 1 HAS CHARACTER IDENTIFIER =EXEC-TIME - IS REAL VALUED - MULTIPLICATIVE CONSTANT = 0.0000E+00 ADDITIVE CONSTANT = 0.0000E+00 - - CONTROL FUNCTION Test CF (CF 2) IS REAL TYPE EQUALS - VALUE = 0.0000E+00 - SCALE FACTOR = 1.0000E+00 ADDITIVE CONSTANT = 0.0000E+00 - UPPER BOUND = 3.4028E+38 LOWER BOUND = -3.4028E+38 - NUMBER OF ARGUMENTS = 1 - ARGUMENT NUMBER = 1 HAS CHARACTER IDENTIFIER =EXEC-TIME - IS REAL VALUED - MULTIPLICATIVE CONSTANT = 2.0000E+00 ADDITIVE CONSTANT = 1.0000E+00 - - END OF EDIT FOR CF - - - ***** TABULAR FUNCTION EDIT ***** - - - TOTAL NUMBER OF TABULAR FUNCTIONS = 3 - TOTAL NUMBER OF DATA PAIRS = 6 - - - - TABULAR FUNCTION P_in - MULTIPLICATIVE CONSTANT = 1.00000E+00 ADDITIVE CONSTANT = 0.00000E+00 - LOWER BD CONDITION SWITCH = 0 UPPER BD CONDITION SWITCH = 0 - I X Y - 1 0.00000E+00 1.00000E+07 - 2 1.00000E+02 1.00000E+07 - - TABULAR FUNCTION T_in - MULTIPLICATIVE CONSTANT = 1.00000E+00 ADDITIVE CONSTANT = 0.00000E+00 - LOWER BD CONDITION SWITCH = 0 UPPER BD CONDITION SWITCH = 0 - I X Y - 1 0.00000E+00 4.00000E+02 - 2 1.00000E+02 4.00000E+02 - - TABULAR FUNCTION M_in - MULTIPLICATIVE CONSTANT = 1.00000E+00 ADDITIVE CONSTANT = 0.00000E+00 - LOWER BD CONDITION SWITCH = 0 UPPER BD CONDITION SWITCH = 0 - I X Y - 1 0.00000E+00 1.00000E+00 - 2 1.00000E+02 1.00000E+00 - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 - RUN 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 1.00000E-04 DTMAX= 1.00000E-01 DTMIN= 1.00000E-07 - DT CONTROL=(INC, 0) DT CUTS= 0 - DT(LAST CYCLE)= 0.00000E+00 - CYCLE= 0 T= 0.000000E+00 DT(INC)= 9.999900E-05 CPU= 3.000000E-06 - CYCLE= 1000 T= 9.866279E+01 DT(MAX)= 1.000000E-01 CPU= 1.389020E-01 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 1.5006E+02 s = 2.5010E+00 min = 4.1684E-02 hrs = 1.7368E-03 days - DT(LAST)= 1.000000E-01 s CYCLE= 1514 CPU TIME= 2.0699E-01 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKESE 4/09/18 10:52:56 - - TEST_1 - CYCLES/CPU = 7.31429E+03 (1/s) TIME/CPU= 7.24969E+02 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.81198E-05 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -6.69158E-16 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.70785E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -7.06835E+09 - ENERGY ERROR = -1.81198E-05 REL ENERGY ERROR = -6.69158E-16 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0003E+07 430.4339 584.2568 8.4692E+03 9.3138E+05 2.8231E+02 9.6681E+05 1.4470E-01 7.3629E-01 3.0202E-03 3.3910E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.911E+00 0.000E+00 2.209E+01 0.000E+00 0.000E+00 7.888E+09 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0264E+01 1.0264E+01 7.8880E+09 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 7.2437E+03 9.1562E+02 6.5847E+05 1.0003E+07 4.7697E+09 - 3 H2O-VAP 1.2255E+03 5.5481E+01 2.5445E+06 1.0003E+07 3.1183E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.84075E+04 5.82126E+04 -1.98051E+04 4.36557E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.7079E+10 3.4147E+10 -1.2197E+10 5.1288E+09 0.0000E+00 2.2888E-05 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 8.3234E+03 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.1687E+04 0.0000E+00 -6.4412E+03 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 2.2680E+10 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.2197E+10 -1.7551E+10 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 3030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 1515 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 7.82260E-02 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 7.62450E-02 - CPU TIME FOR CVH AND FL PKGS EDITS = 1.84200E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 1.39000E-04 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 1515 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 1515 - PRESENT SUBCYCLE TIMESTEP = 1.58480E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 9.0607E-02 1.0361E+00 5.9553E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 8.32342E+03 - 12 FP2_3 CENTR OUT 1 POOL 6.73674E+00 2.16874E+04 - 3 H2O VAP 5.28164E+01 6.44118E+03 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.1880E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 3030 - NUMBER OF CONTROL VOLUMES PROCESSED = 6060 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 1515 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 3030 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 3.01126E+02 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 9.248E+04 3.676E+04 9.032E+04 4.800E+01 1.666E+04 1.058E+04 3.030E+03 - RUN 9.248E+04 3.676E+04 9.032E+04 4.800E+01 1.666E+04 1.058E+04 3.030E+03 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 1.58480E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(INC, 0) DT CUTS= 0 - DT(CVH)= 9.10000E-01 - DT(LAST CYCLE)= 1.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 1515 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - Restart written TIME = 1.500628E+02 CYCLE= 1514 - CYCLE= 2000 T= 2.472213E+02 DT(MAX)= 2.000000E-01 CPU= 2.868680E-01 - CYCLE= 3000 T= 4.472213E+02 DT(MAX)= 2.000000E-01 CPU= 4.315990E-01 - CYCLE= 4000 T= 6.472213E+02 DT(MAX)= 2.000000E-01 CPU= 5.872260E-01 - CYCLE= 5000 T= 8.472213E+02 DT(MAX)= 2.000000E-01 CPU= 7.367070E-01 - CYCLE= 6000 T= 1.047221E+03 DT(MAX)= 2.000000E-01 CPU= 8.763510E-01 - Restart written TIME = 1.150021E+03 CYCLE= 6514 - CYCLE= 7000 T= 1.247221E+03 DT(MAX)= 2.000000E-01 CPU= 1.013480E+00 - CYCLE= 8000 T= 1.447221E+03 DT(MAX)= 2.000000E-01 CPU= 1.144211E+00 - CYCLE= 9000 T= 1.647221E+03 DT(MAX)= 2.000000E-01 CPU= 1.276076E+00 - CYCLE= 10000 T= 1.847221E+03 DT(MAX)= 2.000000E-01 CPU= 1.417202E+00 - CYCLE= 11000 T= 2.047221E+03 DT(MAX)= 2.000000E-01 CPU= 1.541850E+00 - Restart written TIME = 2.150021E+03 CYCLE= 11514 - CYCLE= 12000 T= 2.247221E+03 DT(MAX)= 2.000000E-01 CPU= 1.672173E+00 - CYCLE= 13000 T= 2.447221E+03 DT(MAX)= 2.000000E-01 CPU= 1.814599E+00 - CYCLE= 14000 T= 2.647221E+03 DT(MAX)= 2.000000E-01 CPU= 1.952939E+00 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 2.6500E+03 s = 4.4167E+01 min = 7.3612E-01 hrs = 3.0672E-02 days - DT(LAST)= 2.000000E-01 s CYCLE= 14014 CPU TIME= 1.9556E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKESE 4/09/18 10:52:58 - - TEST_1 - CYCLES/CPU = 7.16605E+03 (1/s) TIME/CPU= 1.35509E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -7.62939E-05 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -2.59487E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.94018E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.74506E+09 - ENERGY ERROR = -7.62939E-05 REL ENERGY ERROR = -2.59487E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 563.9050 584.2558 6.7543E+03 1.5118E+06 2.2514E+02 1.5563E+06 1.8496E-01 7.5058E-01 3.7775E-04 3.4208E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.483E+00 0.000E+00 2.252E+01 0.000E+00 0.000E+00 1.021E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0249E+01 1.0249E+01 1.0211E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.5050E+03 7.3570E+02 1.2775E+06 1.0002E+07 7.0325E+09 - 3 H2O-VAP 1.2493E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1788E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.66926E+04 5.82126E+04 -2.15200E+04 -8.00355E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9402E+10 3.4147E+10 -1.6154E+10 1.1408E+10 0.0000E+00 1.4496E-04 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 1.4699E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.5707E+04 0.0000E+00 -1.4280E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 4.0051E+11 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.6154E+10 -3.8910E+11 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 28030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 14015 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 6.78588E-01 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 6.74831E-01 - CPU TIME FOR CVH AND FL PKGS EDITS = 2.54900E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 1.20800E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 14015 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 14015 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 1.1333E-02 1.0540E+00 5.5677E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 1.46987E+05 - 12 FP2_3 CENTR OUT 1 POOL 4.65765E-01 2.57069E+04 - 3 H2O VAP 5.52109E+01 1.42800E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4414E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 25000 - NUMBER OF CONTROL VOLUMES PROCESSED = 50000 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 12500 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 25000 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 5.30104E+03 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 4.833E+05 1.880E+05 4.702E+05 7.500E+02 1.375E+05 7.704E+03 2.500E+04 - RUN 5.757E+05 2.248E+05 5.605E+05 7.980E+02 1.542E+05 1.828E+04 2.803E+04 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 14015 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - CYCLE= 15000 T= 2.847221E+03 DT(MAX)= 2.000000E-01 CPU= 2.087425E+00 - CYCLE= 16000 T= 3.047221E+03 DT(MAX)= 2.000000E-01 CPU= 2.254320E+00 - Restart written TIME = 3.150021E+03 CYCLE= 16514 - CYCLE= 17000 T= 3.247221E+03 DT(MAX)= 2.000000E-01 CPU= 2.394919E+00 - CYCLE= 18000 T= 3.447221E+03 DT(MAX)= 2.000000E-01 CPU= 2.536022E+00 - CYCLE= 19000 T= 3.647221E+03 DT(MAX)= 2.000000E-01 CPU= 2.694278E+00 - CYCLE= 20000 T= 3.847221E+03 DT(MAX)= 2.000000E-01 CPU= 2.817051E+00 - CYCLE= 21000 T= 4.047221E+03 DT(MAX)= 2.000000E-01 CPU= 2.946875E+00 - Restart written TIME = 4.150021E+03 CYCLE= 21514 - CYCLE= 22000 T= 4.247221E+03 DT(MAX)= 2.000000E-01 CPU= 3.082000E+00 - CYCLE= 23000 T= 4.447221E+03 DT(MAX)= 2.000000E-01 CPU= 3.236195E+00 - CYCLE= 24000 T= 4.647221E+03 DT(MAX)= 2.000000E-01 CPU= 3.372704E+00 - CYCLE= 25000 T= 4.847221E+03 DT(MAX)= 2.000000E-01 CPU= 3.503513E+00 - CYCLE= 26000 T= 5.047221E+03 DT(MAX)= 2.000000E-01 CPU= 3.643297E+00 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 5.1500E+03 s = 8.5834E+01 min = 1.4306E+00 hrs = 5.9607E-02 days - DT(LAST)= 2.000000E-01 s CYCLE= 26514 CPU TIME= 3.7059E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKESE 4/09/18 10:53:00 - - TEST_1 - CYCLES/CPU = 7.15457E+03 (1/s) TIME/CPU= 1.38969E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.74522E-04 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -5.91865E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.94868E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.66004E+09 - ENERGY ERROR = -1.74522E-04 REL ENERGY ERROR = -5.91865E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 578.4274 584.2558 6.4863E+03 1.5874E+06 2.1621E+02 1.6337E+06 1.9293E-01 7.5188E-01 9.3745E-05 3.4229E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.444E+00 0.000E+00 2.256E+01 0.000E+00 0.000E+00 1.030E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0248E+01 1.0248E+01 1.0296E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.2349E+03 7.0327E+02 1.3586E+06 1.0002E+07 7.1120E+09 - 3 H2O-VAP 1.2514E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1843E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.64246E+04 5.82126E+04 -2.17880E+04 -3.63798E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9487E+10 3.4147E+10 -1.6933E+10 1.2273E+10 0.0000E+00 2.9755E-04 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 2.8565E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.6292E+04 0.0000E+00 -2.8115E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 7.7835E+11 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.6933E+10 -7.6608E+11 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 53030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 26515 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 1.26951E+00 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 1.26409E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 3.49300E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 1.92500E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 26515 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 26515 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 2.8123E-03 1.0552E+00 5.5515E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 2.85652E+05 - 12 FP2_3 CENTR OUT 1 POOL 1.05920E-01 2.62922E+04 - 3 H2O VAP 5.54095E+01 2.81148E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4645E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 25000 - NUMBER OF CONTROL VOLUMES PROCESSED = 50000 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 12500 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 25000 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 1.03010E+04 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 4.459E+05 1.709E+05 4.334E+05 7.500E+02 1.375E+05 0.000E+00 2.500E+04 - RUN 1.022E+06 3.957E+05 9.938E+05 1.548E+03 2.917E+05 1.828E+04 5.303E+04 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 26515 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - Restart written TIME = 5.150021E+03 CYCLE= 26514 - CYCLE= 27000 T= 5.247221E+03 DT(MAX)= 2.000000E-01 CPU= 3.769048E+00 - CYCLE= 28000 T= 5.447221E+03 DT(MAX)= 2.000000E-01 CPU= 3.899985E+00 - CYCLE= 29000 T= 5.647221E+03 DT(MAX)= 2.000000E-01 CPU= 4.028836E+00 - CYCLE= 30000 T= 5.847221E+03 DT(MAX)= 2.000000E-01 CPU= 4.150715E+00 - CYCLE= 31000 T= 6.047221E+03 DT(MAX)= 2.000000E-01 CPU= 4.278346E+00 - Restart written TIME = 6.150021E+03 CYCLE= 31514 - CYCLE= 32000 T= 6.247221E+03 DT(MAX)= 2.000000E-01 CPU= 4.404067E+00 - CYCLE= 33000 T= 6.447221E+03 DT(MAX)= 2.000000E-01 CPU= 4.560245E+00 - CYCLE= 34000 T= 6.647221E+03 DT(MAX)= 2.000000E-01 CPU= 4.700426E+00 - CYCLE= 35000 T= 6.847221E+03 DT(MAX)= 2.000000E-01 CPU= 4.835798E+00 - CYCLE= 36000 T= 7.047221E+03 DT(MAX)= 2.000000E-01 CPU= 4.967461E+00 - Restart written TIME = 7.150021E+03 CYCLE= 36514 - CYCLE= 37000 T= 7.247221E+03 DT(MAX)= 2.000000E-01 CPU= 5.089076E+00 - CYCLE= 38000 T= 7.447221E+03 DT(MAX)= 2.000000E-01 CPU= 5.208195E+00 - CYCLE= 39000 T= 7.647221E+03 DT(MAX)= 2.000000E-01 CPU= 5.360898E+00 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 7.6500E+03 s = 1.2750E+02 min = 2.1250E+00 hrs = 8.8542E-02 days - DT(LAST)= 2.000000E-01 s CYCLE= 39014 CPU TIME= 5.3636E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKESE 4/09/18 10:53:01 - - TEST_1 - CYCLES/CPU = 7.27380E+03 (1/s) TIME/CPU= 1.42628E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.57356E-04 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -5.33439E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.94985E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.64840E+09 - ENERGY ERROR = -1.57356E-04 REL ENERGY ERROR = -5.33439E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 581.9940 584.2557 6.4145E+03 1.6070E+06 2.1382E+02 1.6538E+06 1.9517E-01 7.5215E-01 3.0470E-05 3.4232E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.435E+00 0.000E+00 2.256E+01 0.000E+00 0.000E+00 1.031E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0248E+01 1.0248E+01 1.0308E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.1626E+03 6.9432E+02 1.3796E+06 1.0002E+07 7.1225E+09 - 3 H2O-VAP 1.2519E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1855E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.63528E+04 5.82126E+04 -2.18598E+04 7.27596E-12 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9498E+10 3.4147E+10 -1.7147E+10 1.2499E+10 0.0000E+00 3.3951E-04 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 4.2432E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.6447E+04 0.0000E+00 -4.1973E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 1.1562E+12 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.7147E+10 -1.1437E+12 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 78030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 39015 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 1.81033E+00 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 1.80313E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 4.21400E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 2.98700E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 39015 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 39015 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 9.1411E-04 1.0554E+00 5.5482E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 4.24318E+05 - 12 FP2_3 CENTR OUT 1 POOL 3.36847E-02 2.64466E+04 - 3 H2O VAP 5.54483E+01 4.19731E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4693E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 25000 - NUMBER OF CONTROL VOLUMES PROCESSED = 50000 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 12500 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 25000 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 1.53010E+04 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 4.316E+05 1.566E+05 4.191E+05 7.500E+02 1.375E+05 0.000E+00 2.500E+04 - RUN 1.453E+06 5.523E+05 1.413E+06 2.298E+03 4.292E+05 1.828E+04 7.803E+04 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 39015 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - CYCLE= 40000 T= 7.847221E+03 DT(MAX)= 2.000000E-01 CPU= 5.528950E+00 - CYCLE= 41000 T= 8.047221E+03 DT(MAX)= 2.000000E-01 CPU= 5.686795E+00 - Restart written TIME = 8.150021E+03 CYCLE= 41514 - CYCLE= 42000 T= 8.247221E+03 DT(MAX)= 2.000000E-01 CPU= 5.854023E+00 - CYCLE= 43000 T= 8.447221E+03 DT(MAX)= 2.000000E-01 CPU= 6.018049E+00 - CYCLE= 44000 T= 8.647221E+03 DT(MAX)= 2.000000E-01 CPU= 6.139831E+00 - CYCLE= 45000 T= 8.847221E+03 DT(MAX)= 2.000000E-01 CPU= 6.268591E+00 - CYCLE= 46000 T= 9.047221E+03 DT(MAX)= 2.000000E-01 CPU= 6.402658E+00 - Restart written TIME = 9.150021E+03 CYCLE= 46514 - CYCLE= 47000 T= 9.247221E+03 DT(MAX)= 2.000000E-01 CPU= 6.531960E+00 - CYCLE= 48000 T= 9.447221E+03 DT(MAX)= 2.000000E-01 CPU= 6.681590E+00 - CYCLE= 49000 T= 9.647221E+03 DT(MAX)= 2.000000E-01 CPU= 6.845768E+00 - CYCLE= 50000 T= 9.847221E+03 DT(MAX)= 2.000000E-01 CPU= 6.972043E+00 - - JOB TERMINATION PROCEDURE STARTED - -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 1.0000E+04 s = 1.6667E+02 min = 2.7778E+00 hrs = 1.1574E-01 days - DT(LAST)= 2.000000E-01 s CYCLE= 50764 CPU TIME= 7.0650E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKESE 4/09/18 10:53:03 - - TEST_1 - CYCLES/CPU = 7.18528E+03 (1/s) TIME/CPU= 1.41543E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.69754E-04 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -5.75407E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.95016E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.64529E+09 - ENERGY ERROR = -1.69754E-04 REL ENERGY ERROR = -5.75407E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 583.1678 584.2557 6.3904E+03 1.6135E+06 2.1301E+02 1.6605E+06 1.9592E-01 7.5223E-01 1.2565E-05 3.4233E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.433E+00 0.000E+00 2.257E+01 0.000E+00 0.000E+00 1.031E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0248E+01 1.0248E+01 1.0311E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.1384E+03 6.9127E+02 1.3867E+06 1.0002E+07 7.1253E+09 - 3 H2O-VAP 1.2520E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1858E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.63287E+04 5.82126E+04 -2.18839E+04 -5.82077E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9502E+10 3.4147E+10 -1.7219E+10 1.2574E+10 0.0000E+00 -4.9591E-05 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 5.5466E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.6498E+04 0.0000E+00 -5.5005E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 1.5114E+12 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.7219E+10 -1.4988E+12 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 101528 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 50764 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 2.37935E+00 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 2.37041E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 5.14100E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 3.80100E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 50764 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 50764 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 3.7694E-04 1.0555E+00 5.5473E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 5.54664E+05 - 12 FP2_3 CENTR OUT 1 POOL 1.37949E-02 2.64983E+04 - 3 H2O VAP 5.54589E+01 5.50049E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4706E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 23498 - NUMBER OF CONTROL VOLUMES PROCESSED = 46996 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 11749 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 23498 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 2.00010E+04 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 3.614E+05 1.137E+05 3.567E+05 7.050E+02 1.292E+05 0.000E+00 2.350E+04 - RUN 1.815E+06 6.660E+05 1.770E+06 3.003E+03 5.584E+05 1.828E+04 1.015E+05 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 50765 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - Restart written TIME = 1.000002E+04 CYCLE= 50764 - - - FOR THIS RUN THERE WERE - - PLOT TIME RECORDS = 1001 - - EDIT TIME RECORDS = 6 - - START MESSAGE FILE ************* - - MELCOR message output IRDKESE 4/09/18 10:52:56 - TEST_1 - Listing written TIME= 0.00000E+00 CYCLE= 0 - Listing written TIME= 1.50063E+02 CYCLE= 1514 - Restart written TIME = 1.500628E+02 CYCLE= 1514 - Restart written TIME = 1.150021E+03 CYCLE= 6514 - Restart written TIME = 2.150021E+03 CYCLE= 11514 - Listing written TIME= 2.65002E+03 CYCLE= 14014 - Restart written TIME = 3.150021E+03 CYCLE= 16514 - Restart written TIME = 4.150021E+03 CYCLE= 21514 - Listing written TIME= 5.15002E+03 CYCLE= 26514 - Restart written TIME = 5.150021E+03 CYCLE= 26514 - Restart written TIME = 6.150021E+03 CYCLE= 31514 - Restart written TIME = 7.150021E+03 CYCLE= 36514 - Listing written TIME= 7.65002E+03 CYCLE= 39014 - Restart written TIME = 8.150021E+03 CYCLE= 41514 - Restart written TIME = 9.150021E+03 CYCLE= 46514 - Listing written TIME= 1.00000E+04 CYCLE= 50764 - Restart written TIME = 1.000002E+04 CYCLE= 50764 - Begin normal termination - Time 10000.0212728003 - CPU 7.06499500000000 - Relative Energy Error -5.754070000000000E-015 - CVH-H2O-RELERR 3.998693332606853E-012 - Normal termination TIME= 1.00000E+04 CYCLE= 50764 CPU = 7.06500E+00 diff --git a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/2/MELMES_v2-0 b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/2/MELMES_v2-0 new file mode 100644 index 0000000000..292b72c5cc --- /dev/null +++ b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/2/MELMES_v2-0 @@ -0,0 +1,9 @@ + MELCOR message output TWBKAGZ 2/20/23 10:03:01 + TEST_1 + Listing written TIME= 0.00000E+00 CYCLE= 0 + Relative Energy Error 1.320451326020530E-263 +Begin normal termination + Time 1000.04218279900 + CPU 0.151202000000000 + CVH-H2O-RELERR 5.869692967383991E-014 + Normal termination TIME= 1.00004E+03 CYCLE= 2017 CPU = 1.51202E-01 diff --git a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/2/MELPTF.PTF b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/2/MELPTF.PTF new file mode 100644 index 0000000000..618f8c41a8 Binary files /dev/null and b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/2/MELPTF.PTF differ diff --git a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/2/OUTPUT_MELCOR.out b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/2/OUTPUT_MELCOR.out deleted file mode 100644 index c06cf4a847..0000000000 --- a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/2/OUTPUT_MELCOR.out +++ /dev/null @@ -1,2222 +0,0 @@ - COMMAND-LINE: /usr/local/neapps/melcor/melcor_2_2/melcor i=test.i - COMMAND-LINE ARGUMENTS: - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - This is an official build. - MELCOR 2.2.10167 - Executing on: Intel(R) Xeon(R) CPU E5-2670 v3 @ 2.30GHz - Configuration information: - Configuration RL_NL_CHECKALL - Subversion revision: 10167 - - Build Processor: Intel(R) Xeon(R) CPU E5-2643 v2 @ 3.50GHz - - Compiler: Intel(R) Visual Fortran Compiler Professional for applications runnin - g on IA-32, Version 11.1 Build 20100414 - - Compiler settings: - /fpp /nologo /O2 /Oy- /DNIGHTLY_TESTING /DLICENSING_INACTIVE /DWINDOWS /DARCH_I - NT /DGET_CPU_INFO /DINTEROP /I..\compiled_modules /check:all /check:uninit /ch - eck:noarg_temp_created /check:nooutput_conversion /assume:nocc_omp /assume:prot - ect-parens /noaltparam /error_limit:25 /warn:errors /real_size:64 /Qauto /Qpre - c-div /Qprec-sqrt /libs:static /threads /iface:cvf /align:rec8byte /align:dcomm - ons /align:records /traceback /fp:source /module:..\compiled_modules /warn:noal - ign /debug:all /Qdiag-disable:8291 /F20000000 /Qmkl:sequential /fpe0 - - Linker settings: - /NODEFAULTLIB:LIBCMT /LIBPATH:..\RL_NL_CHECKALL_Library /LIBPATH:C:\Program Fil - es (x86)\Microsoft SDKs\Windows\v7.1A\Lib /LIBPATH:C:\Program Files (x86)\Inte - l\Compiler\11.1\065\lib\ia32 /LIBPATH:..\lib - - !!!LICENSING HAS BEEN DISABLED!!! - - -MELCOR OUTPUT FILENAMES - TEXT OUTPUT: OUTPUT_MELCOR.out - DIAGNOSTIC FILE: MELDIA_v2-0 - EXTENDED DIAGNOSTIC FILE: extDIAG_v2-0 - RESTART FILE: MELRST_v2-0 - PLOTFILE: MELPTF.PTF - STOP FILE: MELSTP_v2-0 - MESSAGE FILE: MELMES_v2-0 - STATUS FILE: MELSTT_v2-0 - PAUSE FILE: PAUSEFN - CFEXFILE: CFEXFILE - CFEXWRITE: CFEXWRITE - - - Opening user input file test.i - - Computer environment = ANY - - WWWWWWWWWWWWW MELCOR input WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW - - - 1 Input file: test.i - 2 *m: SNAP:Symbolic Nuclear Analysis Package, Version 2.4.0, July 09, 2015 - 3 *m: PLUGIN:MELCOR Version 2.3.0 - 4 *m: CODE:MELCOR Version 2.1 - 5 *m: DATE:12/16/16 - 6 ! - 7 !MEG_DIAGFILE 'MEGDIA.TXT' - 8 !MEG_OUTPUTFILE 'MEGOUT.TXT' - 9 MEL_OUTPUTFILE 'OUTPUT_MELCOR.out' - 10 !MEG_RESTARTFILE 'MELRST.RST' - 11 !PLOTFILE 'MELPTF.PTF' - 12 !MESSAGEFILE 'MELMES.TXT' - 13 !EXTDIAGFILE 'EXTDIAG.TXT' - 14 ! - 15 !************************************************* - 16 !'test_1' - 17 !************************************************* - 18 ! - 19 ! - 20 ! - 21 !* Block: MEX (Exec) data **************************** - 22 EXEC_INPUT - 23 EXEC_TITLE test_1 ! Title of the calculation - 24 EXEC_TEND 10.0E+03 !* ! End of calculation time - 25 EXEC_TIME 2 !*NUMBER TIME DTMAX DTMIN DTEDT DTPLT DTRST DCRST - 26 1 0.00 0.1000E+00 0.10000E-06 2.50000E+03 1.00000E+01 1.00000E+03 0.10000000E+11 - 27 2 1.50000E+02 0.2000E+00 0.10000E-09 2.50000E+03 1.00000E+01 1.0000E+03 0.10000000E+1 - 28 - 29 EXEC_CPULEFT 1000. ! cpu sec left at end of calculation - 30 EXEC_CPULIM 4000000. ! Maximum number of CPU seconds allowed for this executio - 31 EXEC_NOFLUSH ! Suppress Explicit Buffer Flushing - 32 EXEC_CYMESF 100 1000 1 1 - 33 !* END MEX (Exec) ****************************** - 34 ! - 35 !*CVH_INPUT - 36 !*CVH_TRACE 3 - 37 - Time= 0.0000E+00 Dt= 1.0000E-04 Cycle= 0 (MEX) - ERROR IN MEXSET - - - TITLES DO NOT MATCH TO SPECIFIED LENGTH - /TEST_1 - /test_1 - - - RUN TITLE : TEST_1 - - RUN ID : IRDKERV 4/09/18 10:52:47 -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during MELCOR input processing EXEC package: - - MEGEDG 1111, IOUTSW 4 - - - TIME STEP AND EDIT INTERVALS (S) - - TIME DTMAX DTMIN DTEDIT DTPLOT DTRESTART - 0.0000E+00 - 1.0000E-01 1.0000E-07 2.5000E+03 1.0000E+01 1.0000E+03 - 1.5000E+02 - 2.0000E-01 1.0000E-10 2.5000E+03 1.0000E+01 1.0000E+03 - 1.0000E+04 ( = TEND ) - - - NO EXACT TIME VALUES REQUESTED - - SOFTDTMIN UNDERRUN NOT ALLOWED - - FORCEPLOT DT REDUCTION FOR EXTRA FORCED PLOT DUMP = 2.00000E-01 - MAXIMUM NUMBER OF EXTRA PLOT DUMPS PER EXECUTION = 20 - - RESTART REQUESTED FROM LAST AVAILABLE CYCLE - or FIRST TIME >= 0.0000E+00 - - CPU LIMIT FOR EXECUTION = 4.00000E+06 - - CPU LEFT AT TERMINATION = 1.00000E+03 - - FILE MESSAGE LEVEL FOR LIST - STANDARD OUTPUT 2 - DIAGNOSTIC OUTPUT 2 - TERMINAL OUTPUT -1 - -NO Errors during MELCOR input processing EXEC package - MEX PACKAGE IS ACTIVE - NCG PACKAGE IS ACTIVE - CVH PACKAGE IS ACTIVE - FL PACKAGE IS ACTIVE - CVT PACKAGE IS ACTIVE - INP PACKAGE IS ACTIVE - CRA PACKAGE IS ACTIVE - CF PACKAGE IS ACTIVE - TF PACKAGE IS ACTIVE - MES PACKAGE IS ACTIVE - H2O PACKAGE IS ACTIVE - SC PACKAGE IS ACTIVE - ESF PACKAGE IS ACTIVE -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during PASS2 input processing CF package: -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during MELCOR PASS2 input processing EXEC package: -NO Errors during MELCOR PASS2 input processing EXEC package -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during MELCOR PASS2 input processing ESF package: -NO Errors during MELCOR PASS2 input processing ESF package - - - GRAPHICS KEY DIRECTORY - - CFVALU CVH-ATM-FR CVH-CLIQLEV - CVH-CPUC CVH-CPUE CVH-CPUR - CVH-CPUT CVH-CVOLLIQ CVH-E - CVH-E.1 CVH-E.2 CVH-E.3 - CVH-ECV CVH-ECV.1 CVH-ECV.2 - CVH-ECV.3 CVH-GR-ATMS CVH-GR-POOL - CVH-H CVH-H.1 CVH-H.2 - CVH-H.3 CVH-H2O-ERR CVH-H2O-ERR0 - CVH-LIQLEV CVH-MASS CVH-MASS.1 - CVH-MASS.2 CVH-MASS.3 CVH-NCYCLE - CVH-P CVH-PPART.1 CVH-PPART.2 - CVH-PPART.3 CVH-PR-ATMS CVH-PR-POOL - CVH-PSAT(TLIQ) CVH-PSAT(TVAP) CVH-QUALITY - CVH-RHO CVH-RHO.1 CVH-RHO.2 - CVH-RHO.3 CVH-SC-ATMS CVH-TLIQ - CVH-TOT-E CVH-TOT-M CVH-TSAT(A) - CVH-TSAT(P) CVH-TVAP CVH-VELLIQCV - CVH-VELVAPCV CVH-VIRVOLIQ CVH-VIRVOVAP - CVH-VOID-P CVH-VOID-T CVH-VOIDSG - CVH-VOLFOG CVH-VOLLIQ CVH-VOLVAP - CVH-X.3 FL-CHOKE FL-CONDITION - FL-EFLOW.A FL-EFLOW.P FL-I-EFLOW.A - FL-I-EFLOW.P FL-I-H2O-MFLOW FL-I-MFLOW.1 - FL-I-MFLOW.2 FL-I-MFLOW.3 FL-MFLOW - FL-MFLOW.1 FL-MFLOW.2 FL-MFLOW.3 - FL-PMP-QFLO FL-VELLIQ FL-VELVAP - FL-VOID GLOBALENERGYERR LOCALWARP - Messages Messages-Details WARP - - - ** ** ** ** ** ** ** ** - ** RESTART SETUP COMPLETE ** - ** ** ** ** ** ** ** ** - - -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 0.0000E+00 s = 0.0000E+00 min = 0.0000E+00 hrs = 0.0000E+00 days - DT(LAST)= 1.000000E-04 s CYCLE= 0 CPU TIME= 4.0000E-06 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKERV 4/09/18 10:52:47 - - TEST_1 - CYCLES/CPU = 0.00000E+00 (1/s) TIME/CPU= 0.00000E+00 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = 0.00000E+00 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = 0.00000E+00 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 3.41469E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - - NON-CONDENSIBLE GAS TIME INDEPENDENT DATA EDIT - - - - - 3 MATERIALS ARE DEFINED FOR THIS CALCULATION - - MATERIAL MATERIAL MOLECULAR INTERNAL - NUMBER NAME WEIGHT ENERGY ZERO - (KG/MOL) (J/KG) - - 1 POOL 1.8016E-02 0.0000E+00-ELV - 2 FOG 1.8016E-02 0.0000E+00-ELV - 3 H2O-VAP 1.8016E-02 0.0000E+00 - - - - MATERIAL CONSTANTS FOR CV(T) - - NUMB CV0 CV1 CV2 CV3 CVSQRT - J/KG-K J/KG-K**2 J/KG-K**3 J/KG-K**4 J/KG-K**(3/2) - CVM1 CVM2 TLOW TUP - J/KG J-K/KG K K - - 3 1.507E+03 0.000E+00 0.000E+00 0.000E+00 0.000E+00 - 0.000E+00 0.000E+00 1.000E+00 1.000E+04 - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.1000E+01 1.1000E+01 1.4956E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8423E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 5.82126E+04 5.82126E+04 0.00000E+00 0.00000E+00 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 3.4147E+10 3.4147E+10 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 0.0000E+00 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT 0.0000E+00 0.0000E+00 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 0 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 0 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 1.11900E-03 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 0.00000E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 9.80000E-04 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 1.39000E-04 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 0 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 0 - PRESENT SUBCYCLE TIMESTEP = 0.00000E+00 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 1.0000E+00 1.0000E+00 0.0000E+00 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 0.0000E+00 0.0000E+00 0.0000E+00 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 12 FP2_3 CENTR OUT 1 POOL 0.00000E+00 0.00000E+00 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 5.0000E-01 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 0.0000E+00 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ****************************************** - * * - * FLOW PATH TIME INDEPENDENT DATA EDIT * - * * - ****************************************** - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME ORIENTATION FLOW TYPE OTHER SPARC FLASH - MODEL FM TO FM TO - 11 FP1_2 IN CENTR VERTICAL NORMAL V(T) N N N N - 12 FP2_3 CENTR OUT VERTICAL NORMAL N N N N - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME JUNCTION ELEVATION LENGTH AREA FRACT OPEN - FM (M) TO (M) (M) (M**2) (-) - 11 FP1_2 IN CENTR 1.0500E+01 1.0500E+01 1.0000E+01 1.0000E+00 1.0000E+00 - 12 FP2_3 CENTR OUT 1.0500E+01 1.0500E+01 1.0000E+01 1.0000E+00 1.0000E+00 - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME 'FM' JUNCTION OPENING 'TO' JUNCTION OPENING MOM.EXCH.L - BOTTOM (M) TOP (M) BOTTOM (M) TOP (M) (M) - 11 FP1_2 IN CENTR 1.0218E+01 1.0782E+01 1.0218E+01 1.0782E+01 5.6419E-01 - 12 FP2_3 CENTR OUT 1.0218E+01 1.0782E+01 1.0218E+01 1.0782E+01 5.6419E-01 - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME LOSS COEFFICIENT DISCHARGE COEFFICIENT - FWD (-) REV (-) FWD (-) REV (-) - 11 FP1_2 IN CENTR 1.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 CENTR OUT 1.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - - - Number FLOW PATH FROM VOLUME TO VOLUME SEG AREA SEG LEN HYD DIA ROUGHNESS F.LAMINAR - (M**2) (M) (M) (M) (-) - 11 FP1_2 IN CENTR 1.0000E+00 1.0000E+01 1.0000E+00 5.0000E-05 1.6000E+01 - 12 FP2_3 CENTR OUT 1.0000E+00 1.0000E+01 1.0000E+00 5.0000E-05 1.6000E+01 - - - *** CONTROL VOLUME CONNECTIVITY DATA *** - VOLUME CONNECTING FLOW PATH VOLUME - IN FP1_2 TO CENTR - CENTR FP1_2 FROM IN - FP2_3 TO OUT - OUT FP2_3 FROM CENTR - - IHX PACKAGE IS NOT ACTIVE - - - MCH PACKAGE IS NOT ACTIVE - - - CCF PACKAGE IS NOT ACTIVE - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 0 - NUMBER OF CONTROL VOLUMES PROCESSED = 0 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 0 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 0 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - -CONTROL FUNCTION ORDER OF EVALUATION - 1 ZERO (CF 1) - 2 Test CF (CF 2) - - - CONTROL FUNCTION ZERO (CF 1) IS REAL TYPE EQUALS - VALUE = 0.0000E+00 - SCALE FACTOR = 1.0000E+00 ADDITIVE CONSTANT = 0.0000E+00 - UPPER BOUND = 3.4028E+38 LOWER BOUND = -3.4028E+38 - NUMBER OF ARGUMENTS = 1 - ARGUMENT NUMBER = 1 HAS CHARACTER IDENTIFIER =EXEC-TIME - IS REAL VALUED - MULTIPLICATIVE CONSTANT = 0.0000E+00 ADDITIVE CONSTANT = 0.0000E+00 - - CONTROL FUNCTION Test CF (CF 2) IS REAL TYPE EQUALS - VALUE = 0.0000E+00 - SCALE FACTOR = 1.0000E+00 ADDITIVE CONSTANT = 0.0000E+00 - UPPER BOUND = 3.4028E+38 LOWER BOUND = -3.4028E+38 - NUMBER OF ARGUMENTS = 1 - ARGUMENT NUMBER = 1 HAS CHARACTER IDENTIFIER =EXEC-TIME - IS REAL VALUED - MULTIPLICATIVE CONSTANT = 2.0000E+00 ADDITIVE CONSTANT = 1.0000E+00 - - END OF EDIT FOR CF - - - ***** TABULAR FUNCTION EDIT ***** - - - TOTAL NUMBER OF TABULAR FUNCTIONS = 3 - TOTAL NUMBER OF DATA PAIRS = 6 - - - - TABULAR FUNCTION P_in - MULTIPLICATIVE CONSTANT = 1.00000E+00 ADDITIVE CONSTANT = 0.00000E+00 - LOWER BD CONDITION SWITCH = 0 UPPER BD CONDITION SWITCH = 0 - I X Y - 1 0.00000E+00 1.00000E+07 - 2 1.00000E+02 1.00000E+07 - - TABULAR FUNCTION T_in - MULTIPLICATIVE CONSTANT = 1.00000E+00 ADDITIVE CONSTANT = 0.00000E+00 - LOWER BD CONDITION SWITCH = 0 UPPER BD CONDITION SWITCH = 0 - I X Y - 1 0.00000E+00 4.00000E+02 - 2 1.00000E+02 4.00000E+02 - - TABULAR FUNCTION M_in - MULTIPLICATIVE CONSTANT = 1.00000E+00 ADDITIVE CONSTANT = 0.00000E+00 - LOWER BD CONDITION SWITCH = 0 UPPER BD CONDITION SWITCH = 0 - I X Y - 1 0.00000E+00 1.00000E+00 - 2 1.00000E+02 1.00000E+00 - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 - RUN 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 1.00000E-04 DTMAX= 1.00000E-01 DTMIN= 1.00000E-07 - DT CONTROL=(INC, 0) DT CUTS= 0 - DT(LAST CYCLE)= 0.00000E+00 - CYCLE= 0 T= 0.000000E+00 DT(INC)= 9.999900E-05 CPU= 4.000000E-06 - CYCLE= 1000 T= 9.866279E+01 DT(MAX)= 1.000000E-01 CPU= 1.550510E-01 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 1.5006E+02 s = 2.5010E+00 min = 4.1684E-02 hrs = 1.7368E-03 days - DT(LAST)= 1.000000E-01 s CYCLE= 1514 CPU TIME= 2.4333E-01 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKERV 4/09/18 10:52:47 - - TEST_1 - CYCLES/CPU = 6.22203E+03 (1/s) TIME/CPU= 6.16707E+02 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.81198E-05 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -6.69158E-16 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.70785E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -7.06835E+09 - ENERGY ERROR = -1.81198E-05 REL ENERGY ERROR = -6.69158E-16 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0003E+07 430.4339 584.2568 8.4692E+03 9.3138E+05 2.8231E+02 9.6681E+05 1.4470E-01 7.3629E-01 3.0202E-03 3.3910E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.911E+00 0.000E+00 2.209E+01 0.000E+00 0.000E+00 7.888E+09 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0264E+01 1.0264E+01 7.8880E+09 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 7.2437E+03 9.1562E+02 6.5847E+05 1.0003E+07 4.7697E+09 - 3 H2O-VAP 1.2255E+03 5.5481E+01 2.5445E+06 1.0003E+07 3.1183E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.84075E+04 5.82126E+04 -1.98051E+04 4.36557E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.7079E+10 3.4147E+10 -1.2197E+10 5.1288E+09 0.0000E+00 2.2888E-05 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 8.3234E+03 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.1687E+04 0.0000E+00 -6.4412E+03 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 2.2680E+10 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.2197E+10 -1.7551E+10 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 3030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 1515 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 9.76600E-02 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 9.55440E-02 - CPU TIME FOR CVH AND FL PKGS EDITS = 1.97700E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 1.39000E-04 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 1515 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 1515 - PRESENT SUBCYCLE TIMESTEP = 1.58480E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 9.0607E-02 1.0361E+00 5.9553E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 8.32342E+03 - 12 FP2_3 CENTR OUT 1 POOL 6.73674E+00 2.16874E+04 - 3 H2O VAP 5.28164E+01 6.44118E+03 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.1880E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 3030 - NUMBER OF CONTROL VOLUMES PROCESSED = 6060 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 1515 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 3030 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 3.01126E+02 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 9.248E+04 3.676E+04 9.032E+04 4.800E+01 1.666E+04 1.058E+04 3.030E+03 - RUN 9.248E+04 3.676E+04 9.032E+04 4.800E+01 1.666E+04 1.058E+04 3.030E+03 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 1.58480E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(INC, 0) DT CUTS= 0 - DT(CVH)= 9.10000E-01 - DT(LAST CYCLE)= 1.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 1515 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - Restart written TIME = 1.500628E+02 CYCLE= 1514 - CYCLE= 2000 T= 2.472213E+02 DT(MAX)= 2.000000E-01 CPU= 3.370330E-01 - CYCLE= 3000 T= 4.472213E+02 DT(MAX)= 2.000000E-01 CPU= 4.802660E-01 - CYCLE= 4000 T= 6.472213E+02 DT(MAX)= 2.000000E-01 CPU= 6.485480E-01 - CYCLE= 5000 T= 8.472213E+02 DT(MAX)= 2.000000E-01 CPU= 7.823110E-01 - CYCLE= 6000 T= 1.047221E+03 DT(MAX)= 2.000000E-01 CPU= 9.080990E-01 - Restart written TIME = 1.150021E+03 CYCLE= 6514 - CYCLE= 7000 T= 1.247221E+03 DT(MAX)= 2.000000E-01 CPU= 1.035354E+00 - CYCLE= 8000 T= 1.447221E+03 DT(MAX)= 2.000000E-01 CPU= 1.168847E+00 - CYCLE= 9000 T= 1.647221E+03 DT(MAX)= 2.000000E-01 CPU= 1.307215E+00 - CYCLE= 10000 T= 1.847221E+03 DT(MAX)= 2.000000E-01 CPU= 1.430437E+00 - CYCLE= 11000 T= 2.047221E+03 DT(MAX)= 2.000000E-01 CPU= 1.566299E+00 - Restart written TIME = 2.150021E+03 CYCLE= 11514 - CYCLE= 12000 T= 2.247221E+03 DT(MAX)= 2.000000E-01 CPU= 1.752026E+00 - CYCLE= 13000 T= 2.447221E+03 DT(MAX)= 2.000000E-01 CPU= 1.921713E+00 - CYCLE= 14000 T= 2.647221E+03 DT(MAX)= 2.000000E-01 CPU= 2.093558E+00 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 2.6500E+03 s = 4.4167E+01 min = 7.3612E-01 hrs = 3.0672E-02 days - DT(LAST)= 2.000000E-01 s CYCLE= 14014 CPU TIME= 2.0962E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKERV 4/09/18 10:52:49 - - TEST_1 - CYCLES/CPU = 6.68542E+03 (1/s) TIME/CPU= 1.26420E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -7.62939E-05 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -2.59487E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.94018E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.74506E+09 - ENERGY ERROR = -7.62939E-05 REL ENERGY ERROR = -2.59487E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 563.9050 584.2558 6.7543E+03 1.5118E+06 2.2514E+02 1.5563E+06 1.8496E-01 7.5058E-01 3.7775E-04 3.4208E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.483E+00 0.000E+00 2.252E+01 0.000E+00 0.000E+00 1.021E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0249E+01 1.0249E+01 1.0211E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.5050E+03 7.3570E+02 1.2775E+06 1.0002E+07 7.0325E+09 - 3 H2O-VAP 1.2493E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1788E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.66926E+04 5.82126E+04 -2.15200E+04 -8.00355E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9402E+10 3.4147E+10 -1.6154E+10 1.1408E+10 0.0000E+00 1.4496E-04 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 1.4699E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.5707E+04 0.0000E+00 -1.4280E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 4.0051E+11 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.6154E+10 -3.8910E+11 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 28030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 14015 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 7.42338E-01 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 7.38248E-01 - CPU TIME FOR CVH AND FL PKGS EDITS = 2.67600E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 1.41400E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 14015 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 14015 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 1.1333E-02 1.0540E+00 5.5677E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 1.46987E+05 - 12 FP2_3 CENTR OUT 1 POOL 4.65765E-01 2.57069E+04 - 3 H2O VAP 5.52109E+01 1.42800E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4414E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 25000 - NUMBER OF CONTROL VOLUMES PROCESSED = 50000 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 12500 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 25000 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 5.30104E+03 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 4.833E+05 1.880E+05 4.702E+05 7.500E+02 1.375E+05 7.704E+03 2.500E+04 - RUN 5.757E+05 2.248E+05 5.605E+05 7.980E+02 1.542E+05 1.828E+04 2.803E+04 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 14015 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - CYCLE= 15000 T= 2.847221E+03 DT(MAX)= 2.000000E-01 CPU= 2.269081E+00 - CYCLE= 16000 T= 3.047221E+03 DT(MAX)= 2.000000E-01 CPU= 2.415758E+00 - Restart written TIME = 3.150021E+03 CYCLE= 16514 - CYCLE= 17000 T= 3.247221E+03 DT(MAX)= 2.000000E-01 CPU= 2.553036E+00 - CYCLE= 18000 T= 3.447221E+03 DT(MAX)= 2.000000E-01 CPU= 2.690569E+00 - CYCLE= 19000 T= 3.647221E+03 DT(MAX)= 2.000000E-01 CPU= 2.827949E+00 - CYCLE= 20000 T= 3.847221E+03 DT(MAX)= 2.000000E-01 CPU= 2.964910E+00 - CYCLE= 21000 T= 4.047221E+03 DT(MAX)= 2.000000E-01 CPU= 3.094397E+00 - Restart written TIME = 4.150021E+03 CYCLE= 21514 - CYCLE= 22000 T= 4.247221E+03 DT(MAX)= 2.000000E-01 CPU= 3.218663E+00 - CYCLE= 23000 T= 4.447221E+03 DT(MAX)= 2.000000E-01 CPU= 3.349192E+00 - CYCLE= 24000 T= 4.647221E+03 DT(MAX)= 2.000000E-01 CPU= 3.483188E+00 - CYCLE= 25000 T= 4.847221E+03 DT(MAX)= 2.000000E-01 CPU= 3.608435E+00 - CYCLE= 26000 T= 5.047221E+03 DT(MAX)= 2.000000E-01 CPU= 3.737090E+00 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 5.1500E+03 s = 8.5834E+01 min = 1.4306E+00 hrs = 5.9607E-02 days - DT(LAST)= 2.000000E-01 s CYCLE= 26514 CPU TIME= 3.8027E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKERV 4/09/18 10:52:51 - - TEST_1 - CYCLES/CPU = 6.97238E+03 (1/s) TIME/CPU= 1.35430E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.74522E-04 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -5.91865E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.94868E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.66004E+09 - ENERGY ERROR = -1.74522E-04 REL ENERGY ERROR = -5.91865E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 578.4274 584.2558 6.4863E+03 1.5874E+06 2.1621E+02 1.6337E+06 1.9293E-01 7.5188E-01 9.3745E-05 3.4229E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.444E+00 0.000E+00 2.256E+01 0.000E+00 0.000E+00 1.030E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0248E+01 1.0248E+01 1.0296E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.2349E+03 7.0327E+02 1.3586E+06 1.0002E+07 7.1120E+09 - 3 H2O-VAP 1.2514E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1843E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.64246E+04 5.82126E+04 -2.17880E+04 -3.63798E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9487E+10 3.4147E+10 -1.6933E+10 1.2273E+10 0.0000E+00 2.9755E-04 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 2.8565E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.6292E+04 0.0000E+00 -2.8115E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 7.7835E+11 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.6933E+10 -7.6608E+11 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 53030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 26515 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 1.31118E+00 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 1.30538E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 3.61500E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 2.18400E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 26515 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 26515 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 2.8123E-03 1.0552E+00 5.5515E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 2.85652E+05 - 12 FP2_3 CENTR OUT 1 POOL 1.05920E-01 2.62922E+04 - 3 H2O VAP 5.54095E+01 2.81148E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4645E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 25000 - NUMBER OF CONTROL VOLUMES PROCESSED = 50000 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 12500 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 25000 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 1.03010E+04 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 4.459E+05 1.709E+05 4.334E+05 7.500E+02 1.375E+05 0.000E+00 2.500E+04 - RUN 1.022E+06 3.957E+05 9.938E+05 1.548E+03 2.917E+05 1.828E+04 5.303E+04 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 26515 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - Restart written TIME = 5.150021E+03 CYCLE= 26514 - CYCLE= 27000 T= 5.247221E+03 DT(MAX)= 2.000000E-01 CPU= 3.864303E+00 - CYCLE= 28000 T= 5.447221E+03 DT(MAX)= 2.000000E-01 CPU= 3.996596E+00 - CYCLE= 29000 T= 5.647221E+03 DT(MAX)= 2.000000E-01 CPU= 4.118989E+00 - CYCLE= 30000 T= 5.847221E+03 DT(MAX)= 2.000000E-01 CPU= 4.251791E+00 - CYCLE= 31000 T= 6.047221E+03 DT(MAX)= 2.000000E-01 CPU= 4.384263E+00 - Restart written TIME = 6.150021E+03 CYCLE= 31514 - CYCLE= 32000 T= 6.247221E+03 DT(MAX)= 2.000000E-01 CPU= 4.529100E+00 - CYCLE= 33000 T= 6.447221E+03 DT(MAX)= 2.000000E-01 CPU= 4.691472E+00 - CYCLE= 34000 T= 6.647221E+03 DT(MAX)= 2.000000E-01 CPU= 4.830530E+00 - CYCLE= 35000 T= 6.847221E+03 DT(MAX)= 2.000000E-01 CPU= 4.974622E+00 - CYCLE= 36000 T= 7.047221E+03 DT(MAX)= 2.000000E-01 CPU= 5.136609E+00 - Restart written TIME = 7.150021E+03 CYCLE= 36514 - CYCLE= 37000 T= 7.247221E+03 DT(MAX)= 2.000000E-01 CPU= 5.281820E+00 - CYCLE= 38000 T= 7.447221E+03 DT(MAX)= 2.000000E-01 CPU= 5.436251E+00 - CYCLE= 39000 T= 7.647221E+03 DT(MAX)= 2.000000E-01 CPU= 5.605045E+00 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 7.6500E+03 s = 1.2750E+02 min = 2.1250E+00 hrs = 8.8542E-02 days - DT(LAST)= 2.000000E-01 s CYCLE= 39014 CPU TIME= 5.6076E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKERV 4/09/18 10:52:53 - - TEST_1 - CYCLES/CPU = 6.95731E+03 (1/s) TIME/CPU= 1.36422E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.57356E-04 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -5.33439E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.94985E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.64840E+09 - ENERGY ERROR = -1.57356E-04 REL ENERGY ERROR = -5.33439E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 581.9940 584.2557 6.4145E+03 1.6070E+06 2.1382E+02 1.6538E+06 1.9517E-01 7.5215E-01 3.0470E-05 3.4232E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.435E+00 0.000E+00 2.256E+01 0.000E+00 0.000E+00 1.031E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0248E+01 1.0248E+01 1.0308E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.1626E+03 6.9432E+02 1.3796E+06 1.0002E+07 7.1225E+09 - 3 H2O-VAP 1.2519E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1855E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.63528E+04 5.82126E+04 -2.18598E+04 7.27596E-12 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9498E+10 3.4147E+10 -1.7147E+10 1.2499E+10 0.0000E+00 3.3951E-04 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 4.2432E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.6447E+04 0.0000E+00 -4.1973E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 1.1562E+12 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.7147E+10 -1.1437E+12 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 78030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 39015 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 1.92432E+00 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 1.91645E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 4.47500E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 3.39300E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 39015 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 39015 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 9.1411E-04 1.0554E+00 5.5482E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 4.24318E+05 - 12 FP2_3 CENTR OUT 1 POOL 3.36847E-02 2.64466E+04 - 3 H2O VAP 5.54483E+01 4.19731E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4693E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 25000 - NUMBER OF CONTROL VOLUMES PROCESSED = 50000 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 12500 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 25000 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 1.53010E+04 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 4.316E+05 1.566E+05 4.191E+05 7.500E+02 1.375E+05 0.000E+00 2.500E+04 - RUN 1.453E+06 5.523E+05 1.413E+06 2.298E+03 4.292E+05 1.828E+04 7.803E+04 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 39015 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - CYCLE= 40000 T= 7.847221E+03 DT(MAX)= 2.000000E-01 CPU= 5.775987E+00 - CYCLE= 41000 T= 8.047221E+03 DT(MAX)= 2.000000E-01 CPU= 5.947463E+00 - Restart written TIME = 8.150021E+03 CYCLE= 41514 - CYCLE= 42000 T= 8.247221E+03 DT(MAX)= 2.000000E-01 CPU= 6.119915E+00 - CYCLE= 43000 T= 8.447221E+03 DT(MAX)= 2.000000E-01 CPU= 6.297380E+00 - CYCLE= 44000 T= 8.647221E+03 DT(MAX)= 2.000000E-01 CPU= 6.464232E+00 - CYCLE= 45000 T= 8.847221E+03 DT(MAX)= 2.000000E-01 CPU= 6.601406E+00 - CYCLE= 46000 T= 9.047221E+03 DT(MAX)= 2.000000E-01 CPU= 6.739220E+00 - Restart written TIME = 9.150021E+03 CYCLE= 46514 - CYCLE= 47000 T= 9.247221E+03 DT(MAX)= 2.000000E-01 CPU= 6.866941E+00 - CYCLE= 48000 T= 9.447221E+03 DT(MAX)= 2.000000E-01 CPU= 6.985499E+00 - CYCLE= 49000 T= 9.647221E+03 DT(MAX)= 2.000000E-01 CPU= 7.103093E+00 - CYCLE= 50000 T= 9.847221E+03 DT(MAX)= 2.000000E-01 CPU= 7.219952E+00 - - JOB TERMINATION PROCEDURE STARTED - -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 1.0000E+04 s = 1.6667E+02 min = 2.7778E+00 hrs = 1.1574E-01 days - DT(LAST)= 2.000000E-01 s CYCLE= 50764 CPU TIME= 7.3239E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDKERV 4/09/18 10:52:55 - - TEST_1 - CYCLES/CPU = 6.93129E+03 (1/s) TIME/CPU= 1.36540E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.69754E-04 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -5.75407E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.95016E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.64529E+09 - ENERGY ERROR = -1.69754E-04 REL ENERGY ERROR = -5.75407E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 583.1678 584.2557 6.3904E+03 1.6135E+06 2.1301E+02 1.6605E+06 1.9592E-01 7.5223E-01 1.2565E-05 3.4233E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.433E+00 0.000E+00 2.257E+01 0.000E+00 0.000E+00 1.031E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0248E+01 1.0248E+01 1.0311E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.1384E+03 6.9127E+02 1.3867E+06 1.0002E+07 7.1253E+09 - 3 H2O-VAP 1.2520E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1858E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.63287E+04 5.82126E+04 -2.18839E+04 -5.82077E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9502E+10 3.4147E+10 -1.7219E+10 1.2574E+10 0.0000E+00 -4.9591E-05 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 5.5466E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.6498E+04 0.0000E+00 -5.5005E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 1.5114E+12 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.7219E+10 -1.4988E+12 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 101528 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 50764 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 2.49253E+00 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 2.48299E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 5.33500E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 4.20500E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 50764 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 50764 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 3.7694E-04 1.0555E+00 5.5473E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 5.54664E+05 - 12 FP2_3 CENTR OUT 1 POOL 1.37949E-02 2.64983E+04 - 3 H2O VAP 5.54589E+01 5.50049E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4706E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 23498 - NUMBER OF CONTROL VOLUMES PROCESSED = 46996 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 11749 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 23498 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 2.00010E+04 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 3.614E+05 1.137E+05 3.567E+05 7.050E+02 1.292E+05 0.000E+00 2.350E+04 - RUN 1.815E+06 6.660E+05 1.770E+06 3.003E+03 5.584E+05 1.828E+04 1.015E+05 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 50765 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - Restart written TIME = 1.000002E+04 CYCLE= 50764 - - - FOR THIS RUN THERE WERE - - PLOT TIME RECORDS = 1001 - - EDIT TIME RECORDS = 6 - - START MESSAGE FILE ************* - - MELCOR message output IRDKERV 4/09/18 10:52:47 - TEST_1 - Listing written TIME= 0.00000E+00 CYCLE= 0 - Listing written TIME= 1.50063E+02 CYCLE= 1514 - Restart written TIME = 1.500628E+02 CYCLE= 1514 - Restart written TIME = 1.150021E+03 CYCLE= 6514 - Restart written TIME = 2.150021E+03 CYCLE= 11514 - Listing written TIME= 2.65002E+03 CYCLE= 14014 - Restart written TIME = 3.150021E+03 CYCLE= 16514 - Restart written TIME = 4.150021E+03 CYCLE= 21514 - Listing written TIME= 5.15002E+03 CYCLE= 26514 - Restart written TIME = 5.150021E+03 CYCLE= 26514 - Restart written TIME = 6.150021E+03 CYCLE= 31514 - Restart written TIME = 7.150021E+03 CYCLE= 36514 - Listing written TIME= 7.65002E+03 CYCLE= 39014 - Restart written TIME = 8.150021E+03 CYCLE= 41514 - Restart written TIME = 9.150021E+03 CYCLE= 46514 - Listing written TIME= 1.00000E+04 CYCLE= 50764 - Restart written TIME = 1.000002E+04 CYCLE= 50764 - Begin normal termination - Time 10000.0212728003 - CPU 7.32389000000000 - Relative Energy Error -5.754070000000000E-015 - CVH-H2O-RELERR 3.998693332606853E-012 - Normal termination TIME= 1.00000E+04 CYCLE= 50764 CPU = 7.32389E+00 diff --git a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/3/MELMES_v2-0 b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/3/MELMES_v2-0 new file mode 100644 index 0000000000..3137ba25e8 --- /dev/null +++ b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/3/MELMES_v2-0 @@ -0,0 +1,9 @@ + MELCOR message output TWBKAGZ 2/20/23 10:03:01 + TEST_1 + Listing written TIME= 0.00000E+00 CYCLE= 0 + Relative Energy Error 1.320451326020530E-263 +Begin normal termination + Time 1000.04218279900 + CPU 0.138125000000000 + CVH-H2O-RELERR 1.027196327305059E-013 + Normal termination TIME= 1.00004E+03 CYCLE= 2017 CPU = 1.38125E-01 diff --git a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/3/MELPTF.PTF b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/3/MELPTF.PTF new file mode 100644 index 0000000000..a4b0e69d7f Binary files /dev/null and b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/3/MELPTF.PTF differ diff --git a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/3/OUTPUT_MELCOR.out b/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/3/OUTPUT_MELCOR.out deleted file mode 100644 index 75703edc5b..0000000000 --- a/tests/framework/CodeInterfaceTests/MelcorInterface/testMelcor/3/OUTPUT_MELCOR.out +++ /dev/null @@ -1,2222 +0,0 @@ - COMMAND-LINE: /usr/local/neapps/melcor/melcor_2_2/melcor i=test.i - COMMAND-LINE ARGUMENTS: - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - This is an official build. - MELCOR 2.2.10167 - Executing on: Intel(R) Xeon(R) CPU E5-2670 v3 @ 2.30GHz - Configuration information: - Configuration RL_NL_CHECKALL - Subversion revision: 10167 - - Build Processor: Intel(R) Xeon(R) CPU E5-2643 v2 @ 3.50GHz - - Compiler: Intel(R) Visual Fortran Compiler Professional for applications runnin - g on IA-32, Version 11.1 Build 20100414 - - Compiler settings: - /fpp /nologo /O2 /Oy- /DNIGHTLY_TESTING /DLICENSING_INACTIVE /DWINDOWS /DARCH_I - NT /DGET_CPU_INFO /DINTEROP /I..\compiled_modules /check:all /check:uninit /ch - eck:noarg_temp_created /check:nooutput_conversion /assume:nocc_omp /assume:prot - ect-parens /noaltparam /error_limit:25 /warn:errors /real_size:64 /Qauto /Qpre - c-div /Qprec-sqrt /libs:static /threads /iface:cvf /align:rec8byte /align:dcomm - ons /align:records /traceback /fp:source /module:..\compiled_modules /warn:noal - ign /debug:all /Qdiag-disable:8291 /F20000000 /Qmkl:sequential /fpe0 - - Linker settings: - /NODEFAULTLIB:LIBCMT /LIBPATH:..\RL_NL_CHECKALL_Library /LIBPATH:C:\Program Fil - es (x86)\Microsoft SDKs\Windows\v7.1A\Lib /LIBPATH:C:\Program Files (x86)\Inte - l\Compiler\11.1\065\lib\ia32 /LIBPATH:..\lib - - !!!LICENSING HAS BEEN DISABLED!!! - - -MELCOR OUTPUT FILENAMES - TEXT OUTPUT: OUTPUT_MELCOR.out - DIAGNOSTIC FILE: MELDIA_v2-0 - EXTENDED DIAGNOSTIC FILE: extDIAG_v2-0 - RESTART FILE: MELRST_v2-0 - PLOTFILE: MELPTF.PTF - STOP FILE: MELSTP_v2-0 - MESSAGE FILE: MELMES_v2-0 - STATUS FILE: MELSTT_v2-0 - PAUSE FILE: PAUSEFN - CFEXFILE: CFEXFILE - CFEXWRITE: CFEXWRITE - - - Opening user input file test.i - - Computer environment = ANY - - WWWWWWWWWWWWW MELCOR input WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW - - - 1 Input file: test.i - 2 *m: SNAP:Symbolic Nuclear Analysis Package, Version 2.4.0, July 09, 2015 - 3 *m: PLUGIN:MELCOR Version 2.3.0 - 4 *m: CODE:MELCOR Version 2.1 - 5 *m: DATE:12/16/16 - 6 ! - 7 !MEG_DIAGFILE 'MEGDIA.TXT' - 8 !MEG_OUTPUTFILE 'MEGOUT.TXT' - 9 MEL_OUTPUTFILE 'OUTPUT_MELCOR.out' - 10 !MEG_RESTARTFILE 'MELRST.RST' - 11 !PLOTFILE 'MELPTF.PTF' - 12 !MESSAGEFILE 'MELMES.TXT' - 13 !EXTDIAGFILE 'EXTDIAG.TXT' - 14 ! - 15 !************************************************* - 16 !'test_1' - 17 !************************************************* - 18 ! - 19 ! - 20 ! - 21 !* Block: MEX (Exec) data **************************** - 22 EXEC_INPUT - 23 EXEC_TITLE test_1 ! Title of the calculation - 24 EXEC_TEND 10.0E+03 !* ! End of calculation time - 25 EXEC_TIME 2 !*NUMBER TIME DTMAX DTMIN DTEDT DTPLT DTRST DCRST - 26 1 0.00 0.1000E+00 0.10000E-06 2.50000E+03 1.00000E+01 1.00000E+03 0.10000000E+11 - 27 2 1.50000E+02 0.2000E+00 0.10000E-09 2.50000E+03 1.00000E+01 1.0000E+03 0.10000000E+1 - 28 - 29 EXEC_CPULEFT 1000. ! cpu sec left at end of calculation - 30 EXEC_CPULIM 4000000. ! Maximum number of CPU seconds allowed for this executio - 31 EXEC_NOFLUSH ! Suppress Explicit Buffer Flushing - 32 EXEC_CYMESF 100 1000 1 1 - 33 !* END MEX (Exec) ****************************** - 34 ! - 35 !*CVH_INPUT - 36 !*CVH_TRACE 3 - 37 - Time= 0.0000E+00 Dt= 1.0000E-04 Cycle= 0 (MEX) - ERROR IN MEXSET - - - TITLES DO NOT MATCH TO SPECIFIED LENGTH - /TEST_1 - /test_1 - - - RUN TITLE : TEST_1 - - RUN ID : IRDLAIV 4/09/18 11:03:49 -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during MELCOR input processing EXEC package: - - MEGEDG 1111, IOUTSW 4 - - - TIME STEP AND EDIT INTERVALS (S) - - TIME DTMAX DTMIN DTEDIT DTPLOT DTRESTART - 0.0000E+00 - 1.0000E-01 1.0000E-07 2.5000E+03 1.0000E+01 1.0000E+03 - 1.5000E+02 - 2.0000E-01 1.0000E-10 2.5000E+03 1.0000E+01 1.0000E+03 - 1.0000E+04 ( = TEND ) - - - NO EXACT TIME VALUES REQUESTED - - SOFTDTMIN UNDERRUN NOT ALLOWED - - FORCEPLOT DT REDUCTION FOR EXTRA FORCED PLOT DUMP = 2.00000E-01 - MAXIMUM NUMBER OF EXTRA PLOT DUMPS PER EXECUTION = 20 - - RESTART REQUESTED FROM LAST AVAILABLE CYCLE - or FIRST TIME >= 0.0000E+00 - - CPU LIMIT FOR EXECUTION = 4.00000E+06 - - CPU LEFT AT TERMINATION = 1.00000E+03 - - FILE MESSAGE LEVEL FOR LIST - STANDARD OUTPUT 2 - DIAGNOSTIC OUTPUT 2 - TERMINAL OUTPUT -1 - -NO Errors during MELCOR input processing EXEC package - MEX PACKAGE IS ACTIVE - NCG PACKAGE IS ACTIVE - CVH PACKAGE IS ACTIVE - FL PACKAGE IS ACTIVE - CVT PACKAGE IS ACTIVE - INP PACKAGE IS ACTIVE - CRA PACKAGE IS ACTIVE - CF PACKAGE IS ACTIVE - TF PACKAGE IS ACTIVE - MES PACKAGE IS ACTIVE - H2O PACKAGE IS ACTIVE - SC PACKAGE IS ACTIVE - ESF PACKAGE IS ACTIVE -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during PASS2 input processing CF package: -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during MELCOR PASS2 input processing EXEC package: -NO Errors during MELCOR PASS2 input processing EXEC package -WWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWWW -Diagnostics during MELCOR PASS2 input processing ESF package: -NO Errors during MELCOR PASS2 input processing ESF package - - - GRAPHICS KEY DIRECTORY - - CFVALU CVH-ATM-FR CVH-CLIQLEV - CVH-CPUC CVH-CPUE CVH-CPUR - CVH-CPUT CVH-CVOLLIQ CVH-E - CVH-E.1 CVH-E.2 CVH-E.3 - CVH-ECV CVH-ECV.1 CVH-ECV.2 - CVH-ECV.3 CVH-GR-ATMS CVH-GR-POOL - CVH-H CVH-H.1 CVH-H.2 - CVH-H.3 CVH-H2O-ERR CVH-H2O-ERR0 - CVH-LIQLEV CVH-MASS CVH-MASS.1 - CVH-MASS.2 CVH-MASS.3 CVH-NCYCLE - CVH-P CVH-PPART.1 CVH-PPART.2 - CVH-PPART.3 CVH-PR-ATMS CVH-PR-POOL - CVH-PSAT(TLIQ) CVH-PSAT(TVAP) CVH-QUALITY - CVH-RHO CVH-RHO.1 CVH-RHO.2 - CVH-RHO.3 CVH-SC-ATMS CVH-TLIQ - CVH-TOT-E CVH-TOT-M CVH-TSAT(A) - CVH-TSAT(P) CVH-TVAP CVH-VELLIQCV - CVH-VELVAPCV CVH-VIRVOLIQ CVH-VIRVOVAP - CVH-VOID-P CVH-VOID-T CVH-VOIDSG - CVH-VOLFOG CVH-VOLLIQ CVH-VOLVAP - CVH-X.3 FL-CHOKE FL-CONDITION - FL-EFLOW.A FL-EFLOW.P FL-I-EFLOW.A - FL-I-EFLOW.P FL-I-H2O-MFLOW FL-I-MFLOW.1 - FL-I-MFLOW.2 FL-I-MFLOW.3 FL-MFLOW - FL-MFLOW.1 FL-MFLOW.2 FL-MFLOW.3 - FL-PMP-QFLO FL-VELLIQ FL-VELVAP - FL-VOID GLOBALENERGYERR LOCALWARP - Messages Messages-Details WARP - - - ** ** ** ** ** ** ** ** - ** RESTART SETUP COMPLETE ** - ** ** ** ** ** ** ** ** - - -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 0.0000E+00 s = 0.0000E+00 min = 0.0000E+00 hrs = 0.0000E+00 days - DT(LAST)= 1.000000E-04 s CYCLE= 0 CPU TIME= 4.0000E-06 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDLAIV 4/09/18 11:03:49 - - TEST_1 - CYCLES/CPU = 0.00000E+00 (1/s) TIME/CPU= 0.00000E+00 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = 0.00000E+00 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = 0.00000E+00 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 3.41469E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - - NON-CONDENSIBLE GAS TIME INDEPENDENT DATA EDIT - - - - - 3 MATERIALS ARE DEFINED FOR THIS CALCULATION - - MATERIAL MATERIAL MOLECULAR INTERNAL - NUMBER NAME WEIGHT ENERGY ZERO - (KG/MOL) (J/KG) - - 1 POOL 1.8016E-02 0.0000E+00-ELV - 2 FOG 1.8016E-02 0.0000E+00-ELV - 3 H2O-VAP 1.8016E-02 0.0000E+00 - - - - MATERIAL CONSTANTS FOR CV(T) - - NUMB CV0 CV1 CV2 CV3 CVSQRT - J/KG-K J/KG-K**2 J/KG-K**3 J/KG-K**4 J/KG-K**(3/2) - CVM1 CVM2 TLOW TUP - J/KG J-K/KG K K - - 3 1.507E+03 0.000E+00 0.000E+00 0.000E+00 0.000E+00 - 0.000E+00 0.000E+00 1.000E+00 1.000E+04 - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.1000E+01 1.1000E+01 1.4956E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8423E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 5.82126E+04 5.82126E+04 0.00000E+00 0.00000E+00 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 3.4147E+10 3.4147E+10 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 0.0000E+00 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT 0.0000E+00 0.0000E+00 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 0 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 0 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 1.16100E-03 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 0.00000E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 1.00900E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 1.52000E-04 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 0 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 0 - PRESENT SUBCYCLE TIMESTEP = 0.00000E+00 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 1.0000E+00 1.0000E+00 0.0000E+00 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 0.0000E+00 0.0000E+00 0.0000E+00 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 12 FP2_3 CENTR OUT 1 POOL 0.00000E+00 0.00000E+00 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 5.0000E-01 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 0.0000E+00 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ****************************************** - * * - * FLOW PATH TIME INDEPENDENT DATA EDIT * - * * - ****************************************** - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME ORIENTATION FLOW TYPE OTHER SPARC FLASH - MODEL FM TO FM TO - 11 FP1_2 IN CENTR VERTICAL NORMAL V(T) N N N N - 12 FP2_3 CENTR OUT VERTICAL NORMAL N N N N - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME JUNCTION ELEVATION LENGTH AREA FRACT OPEN - FM (M) TO (M) (M) (M**2) (-) - 11 FP1_2 IN CENTR 1.0500E+01 1.0500E+01 1.0000E+01 1.0000E+00 1.0000E+00 - 12 FP2_3 CENTR OUT 1.0500E+01 1.0500E+01 1.0000E+01 1.0000E+00 1.0000E+00 - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME 'FM' JUNCTION OPENING 'TO' JUNCTION OPENING MOM.EXCH.L - BOTTOM (M) TOP (M) BOTTOM (M) TOP (M) (M) - 11 FP1_2 IN CENTR 1.0218E+01 1.0782E+01 1.0218E+01 1.0782E+01 5.6419E-01 - 12 FP2_3 CENTR OUT 1.0218E+01 1.0782E+01 1.0218E+01 1.0782E+01 5.6419E-01 - - - NUMBER FLOW PATH FROM VOLUME TO VOLUME LOSS COEFFICIENT DISCHARGE COEFFICIENT - FWD (-) REV (-) FWD (-) REV (-) - 11 FP1_2 IN CENTR 1.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 CENTR OUT 1.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - - - Number FLOW PATH FROM VOLUME TO VOLUME SEG AREA SEG LEN HYD DIA ROUGHNESS F.LAMINAR - (M**2) (M) (M) (M) (-) - 11 FP1_2 IN CENTR 1.0000E+00 1.0000E+01 1.0000E+00 5.0000E-05 1.6000E+01 - 12 FP2_3 CENTR OUT 1.0000E+00 1.0000E+01 1.0000E+00 5.0000E-05 1.6000E+01 - - - *** CONTROL VOLUME CONNECTIVITY DATA *** - VOLUME CONNECTING FLOW PATH VOLUME - IN FP1_2 TO CENTR - CENTR FP1_2 FROM IN - FP2_3 TO OUT - OUT FP2_3 FROM CENTR - - IHX PACKAGE IS NOT ACTIVE - - - MCH PACKAGE IS NOT ACTIVE - - - CCF PACKAGE IS NOT ACTIVE - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 0 - NUMBER OF CONTROL VOLUMES PROCESSED = 0 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 0 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 0 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - -CONTROL FUNCTION ORDER OF EVALUATION - 1 ZERO (CF 1) - 2 Test CF (CF 2) - - - CONTROL FUNCTION ZERO (CF 1) IS REAL TYPE EQUALS - VALUE = 0.0000E+00 - SCALE FACTOR = 1.0000E+00 ADDITIVE CONSTANT = 0.0000E+00 - UPPER BOUND = 3.4028E+38 LOWER BOUND = -3.4028E+38 - NUMBER OF ARGUMENTS = 1 - ARGUMENT NUMBER = 1 HAS CHARACTER IDENTIFIER =EXEC-TIME - IS REAL VALUED - MULTIPLICATIVE CONSTANT = 0.0000E+00 ADDITIVE CONSTANT = 0.0000E+00 - - CONTROL FUNCTION Test CF (CF 2) IS REAL TYPE EQUALS - VALUE = 0.0000E+00 - SCALE FACTOR = 1.0000E+00 ADDITIVE CONSTANT = 0.0000E+00 - UPPER BOUND = 3.4028E+38 LOWER BOUND = -3.4028E+38 - NUMBER OF ARGUMENTS = 1 - ARGUMENT NUMBER = 1 HAS CHARACTER IDENTIFIER =EXEC-TIME - IS REAL VALUED - MULTIPLICATIVE CONSTANT = 2.0000E+00 ADDITIVE CONSTANT = 1.0000E+00 - - END OF EDIT FOR CF - - - ***** TABULAR FUNCTION EDIT ***** - - - TOTAL NUMBER OF TABULAR FUNCTIONS = 3 - TOTAL NUMBER OF DATA PAIRS = 6 - - - - TABULAR FUNCTION P_in - MULTIPLICATIVE CONSTANT = 1.00000E+00 ADDITIVE CONSTANT = 0.00000E+00 - LOWER BD CONDITION SWITCH = 0 UPPER BD CONDITION SWITCH = 0 - I X Y - 1 0.00000E+00 1.00000E+07 - 2 1.00000E+02 1.00000E+07 - - TABULAR FUNCTION T_in - MULTIPLICATIVE CONSTANT = 1.00000E+00 ADDITIVE CONSTANT = 0.00000E+00 - LOWER BD CONDITION SWITCH = 0 UPPER BD CONDITION SWITCH = 0 - I X Y - 1 0.00000E+00 4.00000E+02 - 2 1.00000E+02 4.00000E+02 - - TABULAR FUNCTION M_in - MULTIPLICATIVE CONSTANT = 1.00000E+00 ADDITIVE CONSTANT = 0.00000E+00 - LOWER BD CONDITION SWITCH = 0 UPPER BD CONDITION SWITCH = 0 - I X Y - 1 0.00000E+00 1.00000E+00 - 2 1.00000E+02 1.00000E+00 - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 - RUN 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 1.00000E-04 DTMAX= 1.00000E-01 DTMIN= 1.00000E-07 - DT CONTROL=(INC, 0) DT CUTS= 0 - DT(LAST CYCLE)= 0.00000E+00 - CYCLE= 0 T= 0.000000E+00 DT(INC)= 9.999900E-05 CPU= 4.000000E-06 - CYCLE= 1000 T= 9.866279E+01 DT(MAX)= 1.000000E-01 CPU= 1.873730E-01 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 1.5006E+02 s = 2.5010E+00 min = 4.1684E-02 hrs = 1.7368E-03 days - DT(LAST)= 1.000000E-01 s CYCLE= 1514 CPU TIME= 2.8159E-01 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDLAIV 4/09/18 11:03:50 - - TEST_1 - CYCLES/CPU = 5.37669E+03 (1/s) TIME/CPU= 5.32920E+02 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.81198E-05 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -6.69158E-16 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.70785E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -7.06835E+09 - ENERGY ERROR = -1.81198E-05 REL ENERGY ERROR = -6.69158E-16 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0003E+07 430.4339 584.2568 8.4692E+03 9.3138E+05 2.8231E+02 9.6681E+05 1.4470E-01 7.3629E-01 3.0202E-03 3.3910E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.911E+00 0.000E+00 2.209E+01 0.000E+00 0.000E+00 7.888E+09 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0264E+01 1.0264E+01 7.8880E+09 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 7.2437E+03 9.1562E+02 6.5847E+05 1.0003E+07 4.7697E+09 - 3 H2O-VAP 1.2255E+03 5.5481E+01 2.5445E+06 1.0003E+07 3.1183E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.84075E+04 5.82126E+04 -1.98051E+04 4.36557E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.7079E+10 3.4147E+10 -1.2197E+10 5.1288E+09 0.0000E+00 2.2888E-05 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 8.3234E+03 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.1687E+04 0.0000E+00 -6.4412E+03 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 2.2680E+10 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.2197E+10 -1.7551E+10 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 3030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 1515 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 1.18698E-01 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 1.16425E-01 - CPU TIME FOR CVH AND FL PKGS EDITS = 2.12100E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 1.52000E-04 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 1515 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 1515 - PRESENT SUBCYCLE TIMESTEP = 1.58480E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 9.0607E-02 1.0361E+00 5.9553E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 8.32342E+03 - 12 FP2_3 CENTR OUT 1 POOL 6.73674E+00 2.16874E+04 - 3 H2O VAP 5.28164E+01 6.44118E+03 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.1880E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 3030 - NUMBER OF CONTROL VOLUMES PROCESSED = 6060 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 1515 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 3030 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 3.01126E+02 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 9.248E+04 3.676E+04 9.032E+04 4.800E+01 1.666E+04 1.058E+04 3.030E+03 - RUN 9.248E+04 3.676E+04 9.032E+04 4.800E+01 1.666E+04 1.058E+04 3.030E+03 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 1.58480E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(INC, 0) DT CUTS= 0 - DT(CVH)= 9.10000E-01 - DT(LAST CYCLE)= 1.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 1515 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - Restart written TIME = 1.500628E+02 CYCLE= 1514 - CYCLE= 2000 T= 2.472213E+02 DT(MAX)= 2.000000E-01 CPU= 3.710270E-01 - CYCLE= 3000 T= 4.472213E+02 DT(MAX)= 2.000000E-01 CPU= 5.437740E-01 - CYCLE= 4000 T= 6.472213E+02 DT(MAX)= 2.000000E-01 CPU= 7.083010E-01 - CYCLE= 5000 T= 8.472213E+02 DT(MAX)= 2.000000E-01 CPU= 8.711280E-01 - CYCLE= 6000 T= 1.047221E+03 DT(MAX)= 2.000000E-01 CPU= 1.041586E+00 - Restart written TIME = 1.150021E+03 CYCLE= 6514 - CYCLE= 7000 T= 1.247221E+03 DT(MAX)= 2.000000E-01 CPU= 1.216498E+00 - CYCLE= 8000 T= 1.447221E+03 DT(MAX)= 2.000000E-01 CPU= 1.384974E+00 - CYCLE= 9000 T= 1.647221E+03 DT(MAX)= 2.000000E-01 CPU= 1.558321E+00 - CYCLE= 10000 T= 1.847221E+03 DT(MAX)= 2.000000E-01 CPU= 1.727061E+00 - CYCLE= 11000 T= 2.047221E+03 DT(MAX)= 2.000000E-01 CPU= 1.895596E+00 - Restart written TIME = 2.150021E+03 CYCLE= 11514 - CYCLE= 12000 T= 2.247221E+03 DT(MAX)= 2.000000E-01 CPU= 2.066579E+00 - CYCLE= 13000 T= 2.447221E+03 DT(MAX)= 2.000000E-01 CPU= 2.228664E+00 - CYCLE= 14000 T= 2.647221E+03 DT(MAX)= 2.000000E-01 CPU= 2.396752E+00 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 2.6500E+03 s = 4.4167E+01 min = 7.3612E-01 hrs = 3.0672E-02 days - DT(LAST)= 2.000000E-01 s CYCLE= 14014 CPU TIME= 2.3994E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDLAIV 4/09/18 11:03:54 - - TEST_1 - CYCLES/CPU = 5.84070E+03 (1/s) TIME/CPU= 1.10447E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -7.62939E-05 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -2.59487E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.94018E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.74506E+09 - ENERGY ERROR = -7.62939E-05 REL ENERGY ERROR = -2.59487E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 563.9050 584.2558 6.7543E+03 1.5118E+06 2.2514E+02 1.5563E+06 1.8496E-01 7.5058E-01 3.7775E-04 3.4208E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.483E+00 0.000E+00 2.252E+01 0.000E+00 0.000E+00 1.021E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0249E+01 1.0249E+01 1.0211E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.5050E+03 7.3570E+02 1.2775E+06 1.0002E+07 7.0325E+09 - 3 H2O-VAP 1.2493E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1788E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.66926E+04 5.82126E+04 -2.15200E+04 -8.00355E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9402E+10 3.4147E+10 -1.6154E+10 1.1408E+10 0.0000E+00 1.4496E-04 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 1.4699E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.5707E+04 0.0000E+00 -1.4280E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 4.0051E+11 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.6154E+10 -3.8910E+11 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 28030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 14015 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 9.03546E-01 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 8.99052E-01 - CPU TIME FOR CVH AND FL PKGS EDITS = 3.02100E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 1.47300E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 14015 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 14015 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 1.1333E-02 1.0540E+00 5.5677E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 1.46987E+05 - 12 FP2_3 CENTR OUT 1 POOL 4.65765E-01 2.57069E+04 - 3 H2O VAP 5.52109E+01 1.42800E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4414E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 25000 - NUMBER OF CONTROL VOLUMES PROCESSED = 50000 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 12500 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 25000 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 5.30104E+03 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 4.833E+05 1.880E+05 4.702E+05 7.500E+02 1.375E+05 7.704E+03 2.500E+04 - RUN 5.757E+05 2.248E+05 5.605E+05 7.980E+02 1.542E+05 1.828E+04 2.803E+04 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 14015 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - CYCLE= 15000 T= 2.847221E+03 DT(MAX)= 2.000000E-01 CPU= 2.567000E+00 - CYCLE= 16000 T= 3.047221E+03 DT(MAX)= 2.000000E-01 CPU= 2.735149E+00 - Restart written TIME = 3.150021E+03 CYCLE= 16514 - CYCLE= 17000 T= 3.247221E+03 DT(MAX)= 2.000000E-01 CPU= 2.905625E+00 - CYCLE= 18000 T= 3.447221E+03 DT(MAX)= 2.000000E-01 CPU= 3.072429E+00 - CYCLE= 19000 T= 3.647221E+03 DT(MAX)= 2.000000E-01 CPU= 3.236928E+00 - CYCLE= 20000 T= 3.847221E+03 DT(MAX)= 2.000000E-01 CPU= 3.397934E+00 - CYCLE= 21000 T= 4.047221E+03 DT(MAX)= 2.000000E-01 CPU= 3.564435E+00 - Restart written TIME = 4.150021E+03 CYCLE= 21514 - CYCLE= 22000 T= 4.247221E+03 DT(MAX)= 2.000000E-01 CPU= 3.732928E+00 - CYCLE= 23000 T= 4.447221E+03 DT(MAX)= 2.000000E-01 CPU= 3.895787E+00 - CYCLE= 24000 T= 4.647221E+03 DT(MAX)= 2.000000E-01 CPU= 4.057802E+00 - CYCLE= 25000 T= 4.847221E+03 DT(MAX)= 2.000000E-01 CPU= 4.222048E+00 - CYCLE= 26000 T= 5.047221E+03 DT(MAX)= 2.000000E-01 CPU= 4.389606E+00 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 5.1500E+03 s = 8.5834E+01 min = 1.4306E+00 hrs = 5.9607E-02 days - DT(LAST)= 2.000000E-01 s CYCLE= 26514 CPU TIME= 4.4753E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDLAIV 4/09/18 11:03:57 - - TEST_1 - CYCLES/CPU = 5.92452E+03 (1/s) TIME/CPU= 1.15077E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.74522E-04 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -5.91865E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.94868E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.66004E+09 - ENERGY ERROR = -1.74522E-04 REL ENERGY ERROR = -5.91865E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 578.4274 584.2558 6.4863E+03 1.5874E+06 2.1621E+02 1.6337E+06 1.9293E-01 7.5188E-01 9.3745E-05 3.4229E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.444E+00 0.000E+00 2.256E+01 0.000E+00 0.000E+00 1.030E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0248E+01 1.0248E+01 1.0296E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.2349E+03 7.0327E+02 1.3586E+06 1.0002E+07 7.1120E+09 - 3 H2O-VAP 1.2514E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1843E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.64246E+04 5.82126E+04 -2.17880E+04 -3.63798E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9487E+10 3.4147E+10 -1.6933E+10 1.2273E+10 0.0000E+00 2.9755E-04 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 2.8565E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.6292E+04 0.0000E+00 -2.8115E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 7.7835E+11 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.6933E+10 -7.6608E+11 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 53030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 26515 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 1.65654E+00 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 1.65024E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 3.93100E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 2.36900E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 26515 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 26515 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 2.8123E-03 1.0552E+00 5.5515E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 2.85652E+05 - 12 FP2_3 CENTR OUT 1 POOL 1.05920E-01 2.62922E+04 - 3 H2O VAP 5.54095E+01 2.81148E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4645E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 25000 - NUMBER OF CONTROL VOLUMES PROCESSED = 50000 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 12500 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 25000 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 1.03010E+04 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 4.459E+05 1.709E+05 4.334E+05 7.500E+02 1.375E+05 0.000E+00 2.500E+04 - RUN 1.022E+06 3.957E+05 9.938E+05 1.548E+03 2.917E+05 1.828E+04 5.303E+04 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 26515 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - Restart written TIME = 5.150021E+03 CYCLE= 26514 - CYCLE= 27000 T= 5.247221E+03 DT(MAX)= 2.000000E-01 CPU= 4.561864E+00 - CYCLE= 28000 T= 5.447221E+03 DT(MAX)= 2.000000E-01 CPU= 4.722911E+00 - CYCLE= 29000 T= 5.647221E+03 DT(MAX)= 2.000000E-01 CPU= 4.885400E+00 - CYCLE= 30000 T= 5.847221E+03 DT(MAX)= 2.000000E-01 CPU= 5.047864E+00 - CYCLE= 31000 T= 6.047221E+03 DT(MAX)= 2.000000E-01 CPU= 5.209303E+00 - Restart written TIME = 6.150021E+03 CYCLE= 31514 - CYCLE= 32000 T= 6.247221E+03 DT(MAX)= 2.000000E-01 CPU= 5.373154E+00 - CYCLE= 33000 T= 6.447221E+03 DT(MAX)= 2.000000E-01 CPU= 5.534476E+00 - CYCLE= 34000 T= 6.647221E+03 DT(MAX)= 2.000000E-01 CPU= 5.694915E+00 - CYCLE= 35000 T= 6.847221E+03 DT(MAX)= 2.000000E-01 CPU= 5.853483E+00 - CYCLE= 36000 T= 7.047221E+03 DT(MAX)= 2.000000E-01 CPU= 6.013976E+00 - Restart written TIME = 7.150021E+03 CYCLE= 36514 - CYCLE= 37000 T= 7.247221E+03 DT(MAX)= 2.000000E-01 CPU= 6.177592E+00 - CYCLE= 38000 T= 7.447221E+03 DT(MAX)= 2.000000E-01 CPU= 6.338694E+00 - CYCLE= 39000 T= 7.647221E+03 DT(MAX)= 2.000000E-01 CPU= 6.500862E+00 -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 7.6500E+03 s = 1.2750E+02 min = 2.1250E+00 hrs = 8.8542E-02 days - DT(LAST)= 2.000000E-01 s CYCLE= 39014 CPU TIME= 6.5033E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDLAIV 4/09/18 11:04:01 - - TEST_1 - CYCLES/CPU = 5.99911E+03 (1/s) TIME/CPU= 1.17633E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.57356E-04 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -5.33439E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.94985E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.64840E+09 - ENERGY ERROR = -1.57356E-04 REL ENERGY ERROR = -5.33439E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 581.9940 584.2557 6.4145E+03 1.6070E+06 2.1382E+02 1.6538E+06 1.9517E-01 7.5215E-01 3.0470E-05 3.4232E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.435E+00 0.000E+00 2.256E+01 0.000E+00 0.000E+00 1.031E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0248E+01 1.0248E+01 1.0308E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.1626E+03 6.9432E+02 1.3796E+06 1.0002E+07 7.1225E+09 - 3 H2O-VAP 1.2519E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1855E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.63528E+04 5.82126E+04 -2.18598E+04 7.27596E-12 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9498E+10 3.4147E+10 -1.7147E+10 1.2499E+10 0.0000E+00 3.3951E-04 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 4.2432E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.6447E+04 0.0000E+00 -4.1973E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 1.1562E+12 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.7147E+10 -1.1437E+12 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 78030 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 39015 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 2.38469E+00 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 2.37614E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 4.86800E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 3.68700E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 39015 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 39015 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 9.1411E-04 1.0554E+00 5.5482E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 4.24318E+05 - 12 FP2_3 CENTR OUT 1 POOL 3.36847E-02 2.64466E+04 - 3 H2O VAP 5.54483E+01 4.19731E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4693E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 25000 - NUMBER OF CONTROL VOLUMES PROCESSED = 50000 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 12500 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 25000 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 1.53010E+04 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 4.316E+05 1.566E+05 4.191E+05 7.500E+02 1.375E+05 0.000E+00 2.500E+04 - RUN 1.453E+06 5.523E+05 1.413E+06 2.298E+03 4.292E+05 1.828E+04 7.803E+04 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 39015 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - CYCLE= 40000 T= 7.847221E+03 DT(MAX)= 2.000000E-01 CPU= 6.663712E+00 - CYCLE= 41000 T= 8.047221E+03 DT(MAX)= 2.000000E-01 CPU= 6.823873E+00 - Restart written TIME = 8.150021E+03 CYCLE= 41514 - CYCLE= 42000 T= 8.247221E+03 DT(MAX)= 2.000000E-01 CPU= 6.983719E+00 - CYCLE= 43000 T= 8.447221E+03 DT(MAX)= 2.000000E-01 CPU= 7.143730E+00 - CYCLE= 44000 T= 8.647221E+03 DT(MAX)= 2.000000E-01 CPU= 7.303574E+00 - CYCLE= 45000 T= 8.847221E+03 DT(MAX)= 2.000000E-01 CPU= 7.462682E+00 - CYCLE= 46000 T= 9.047221E+03 DT(MAX)= 2.000000E-01 CPU= 7.620302E+00 - Restart written TIME = 9.150021E+03 CYCLE= 46514 - CYCLE= 47000 T= 9.247221E+03 DT(MAX)= 2.000000E-01 CPU= 7.781440E+00 - CYCLE= 48000 T= 9.447221E+03 DT(MAX)= 2.000000E-01 CPU= 7.939622E+00 - CYCLE= 49000 T= 9.647221E+03 DT(MAX)= 2.000000E-01 CPU= 8.096513E+00 - CYCLE= 50000 T= 9.847221E+03 DT(MAX)= 2.000000E-01 CPU= 8.254537E+00 - - JOB TERMINATION PROCEDURE STARTED - -1* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * - TIME= 1.0000E+04 s = 1.6667E+02 min = 2.7778E+00 hrs = 1.1574E-01 days - DT(LAST)= 2.000000E-01 s CYCLE= 50764 CPU TIME= 8.3734E+00 - ******* TIME EDIT ***** - - MELCOR BASE CODE VERSION - 2.2 08-31-2017 - - This is an official build. - MELCOR 2.2.10167 - - !!!LICENSING HAS BEEN DISABLED!!! - - IRDLAIV 4/09/18 11:04:04 - - TEST_1 - CYCLES/CPU = 6.06252E+03 (1/s) TIME/CPU= 1.19426E+03 - - - *** GLOBAL ENERGY BALANCE EDIT *** - - GLOBAL ENERGY ERROR = -1.69754E-04 - GLOBAL ENERGY ERROR / ENERGY IN PROBLEM = -5.75407E-15 - - - ENERGY EDIT FOR PACKAGE ESF - ENERGY NOW = 0.00000E+00 ORIGINAL ENERGY = 0.00000E+00 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = 0.00000E+00 - ENERGY ERROR = 0.00000E+00 REL ENERGY ERROR = 0.00000E+00 - - ENERGY EDIT FOR PACKAGE CVH - ENERGY NOW = 2.95016E+10 ORIGINAL ENERGY = 3.41469E+10 - ENERGY TRANSMITTED = 0.00000E+00 ENERGY CREATED = -4.64529E+09 - ENERGY ERROR = -1.69754E-04 REL ENERGY ERROR = -5.75407E-15 - -USER-MODIFIED SENSITIVITY COEFFICIENTS - - - END OF EDIT FOR NCG - - - *************************************** - * * - * CONTROL VOLUME HYDRODYNAMICS EDIT * - * * - *************************************** - - - - VOLUME PRESSURE TLIQ TVAP MASS ENERGY DENSITY ENTHALPY QUALITY VOID CVVELO(1) CVVELO(2) - PA K K KG J/KG KG/M**3 J/KG FRACTION M/S M/S - 1 1.0000E+07 584.2315 584.2315 1.6640E+03 2.5445E+06 5.5466E+01 2.7248E+06 1.0000E+00 1.0000E+00 0.0000E+00 0.0000E+00 - 2 1.0002E+07 583.1678 584.2557 6.3904E+03 1.6135E+06 2.1301E+02 1.6605E+06 1.9592E-01 7.5223E-01 1.2565E-05 3.4233E-02 - 3 9.9999E+06 399.9999 399.9999 2.8274E+04 5.2897E+05 9.4248E+02 5.3958E+05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 - - - VOLUME VOLLIQ VOLFOG VOLVAP VIRVOLLIQ VIRVOLVAP ENERGY VOLUME VOLUME - M**3 M**3 M**3 M**3 M**3 J NAME TYPE - 1 0.000E+00 0.000E+00 3.000E+01 0.000E+00 0.000E+00 4.234E+09 IN - 2 7.433E+00 0.000E+00 2.257E+01 0.000E+00 0.000E+00 1.031E+10 CENTR - 3 3.000E+01 0.000E+00 0.000E+00 0.000E+00 0.000E+00 1.496E+10 OUT - - - VOLUME S-Z-POOL C-Z-POOL ENERGY AREA VOLUME - M M J M**2 NAME - 1 1.0000E+01 1.0000E+01 4.2341E+09 0.0000E+00 IN - 2 1.0248E+01 1.0248E+01 1.0311E+10 3.0000E+01 CENTR - 3 1.1000E+01 1.1000E+01 1.4956E+10 0.0000E+00 OUT - - - VOLUME T(P) - K - 1 5.8423E+02 IN - 2 5.8425E+02 CENTR - 3 5.8423E+02 OUT - - - VOLUME MATERIAL MASS DENSITY E PPART ECV - NUM NAME KG KG/M**3 J/KG PA J - IN 3 H2O-VAP 1.6640E+03 5.5466E+01 2.5445E+06 1.0000E+07 4.2341E+09 - CENTR 1 POOL 5.1384E+03 6.9127E+02 1.3867E+06 1.0002E+07 7.1253E+09 - 3 H2O-VAP 1.2520E+03 5.5480E+01 2.5445E+06 1.0002E+07 3.1858E+09 - OUT 1 POOL 2.8274E+04 9.4248E+02 5.2897E+05 9.9999E+06 1.4956E+10 - - - MATERIAL TOTAL ORIGINAL MASS MASS - NUM NAME MASS MASS SOURCE ERROR - (KG) (KG) (KG) (KG) - 1-3 WATER 3.63287E+04 5.82126E+04 -2.18839E+04 -5.82077E-11 - - - TOTAL ORIGINAL POOL ENERGY ATMOS ENERGY POOL ENERGY - ENERGY ENERGY SOURCE SOURCE SURFACE ERROR - (J) (J) (J) (J) (J) (J) - 2.9502E+10 3.4147E+10 -1.7219E+10 1.2574E+10 0.0000E+00 -4.9591E-05 - - - MASS SOURCE EDIT - - MASS SOURCE OF CONTROL VOLUME IN - DELM( 1: 3)= 0.0000E+00 0.0000E+00 5.5466E+05 - MASS SOURCE OF CONTROL VOLUME CENTR - DELM( 1: 3)= 0.0000E+00 0.0000E+00 0.0000E+00 - MASS SOURCE OF CONTROL VOLUME OUT - DELM( 1: 3)= -2.6498E+04 0.0000E+00 -5.5005E+05 - - - ENERGY SOURCE EDIT - - VOLUME POOL ENERGY ATMOS ENERGY POOL S ENERGY - (J) (J) (J) - IN 0.0000E+00 1.5114E+12 0.0000E+00 - CENTR 0.0000E+00 0.0000E+00 0.0000E+00 - OUT -1.7219E+10 -1.4988E+12 0.0000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME IN - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME CENTR - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - VOLUME - ALTITUDE TABLE FOR CONTROL VOLUME OUT - - ALTITUDE VOLUME MATL VOLUME VIRT VOLUME - (M) (M**3) (M**3) (M**3) - 2 1.10000E+01 3.00000E+01 3.00000E+01 0.00000E+00 - 1 1.00000E+01 0.00000E+00 0.00000E+00 0.00000E+00 - - - *** VELOCITY CALCULATION STATISTICS EDIT *** - NUMBER OF MATRIX INVERSIONS = 101528 - NUMBER OF FLOW REVERSALS = 0 - NUMBER OF EXPLICIT INTEGRATIONS = 0 - NUMBER OF SIGNIFICANT DIGITS INVERSIONS = 50764 - NUMBER OF WATER PACKINGS IDENTIFIED = 0 - NUMBER OF CHOKED-FLOW-BASED RESOLVES = 0 - - - TOTAL CPU TIME FOR CVH AND FL PACKAGES = 3.04177E+00 - CPU TIME FOR CVH AND FL PKGS CALCULATIONS = 3.03146E+00 - CPU TIME FOR CVH AND FL PKGS EDITS = 5.76400E-03 - CPU TIME FOR CVH AND FL PACKAGES RESTARTS = 4.55100E-03 - - - *** SUBCYCLE STATISTICS EDIT *** - NUMBER OF SUBCYCLES = 50764 - NUMBER OF REPEATED SUBCYCLES = 0 - NUMBER OF MOMENTUM BALANCE CALLS = 50764 - PRESENT SUBCYCLE TIMESTEP = 2.00000E-01 - - end OF EDIT FOR CVH - - - ****************************** - * * - * FLOW PATH PACKAGE EDIT * - * * - ****************************** - - - - - Number FLOW PATH FROM VOLUME TO VOLUME VELLIQ VELVAP MFLOW AREA TYP ACT CHOKED TIMES - M/S M/S KG/S M**2 CHOKED - 11 FP1_2 IN CENTR 0.0000E+00 1.0000E+00 5.5466E+01 1.0000E+00 0 0 NO 0. - 12 FP2_3 CENTR OUT 3.7694E-04 1.0555E+00 5.5473E+01 1.0000E+00 0 0 NO 0. - - - Number FLOW PATH FROM VOLUME TO VOLUME MATERIAL MFLOW INT-MFLOW - NUM NAME KG/S KG - 11 FP1_2 IN CENTR 1 POOL 0.00000E+00 0.00000E+00 - 3 H2O VAP 5.54662E+01 5.54664E+05 - 12 FP2_3 CENTR OUT 1 POOL 1.37949E-02 2.64983E+04 - 3 H2O VAP 5.54589E+01 5.50049E+05 - - - Number FLOW PATH P HEAD FRACTION OPEN AREA ALPHA - (PA) OPEN (M**2) - 11 FP1_2 0.0000E+00 1.0000E+00 1.0000E+00 1.0000E+00 - 12 FP2_3 0.0000E+00 1.0000E+00 1.0000E+00 9.4706E-01 - - - Number PUMP NAME SPEED FLOW HEAD HYD TRQ RHO MIX FR TRQ MOT TRQ INRT - (RPM) (m3/s) (Pa) (N*m) (kg/m3) (N*m) (N*m) (kg*m2) - - - Number PUMP NAME DEL POW DISS DISPOL DISATM EFF - (W) (W) (W) (W) (%) - - - ******************************** - * IHX PACKAGE EDIT * - ******************************** - - - Integral Heat Exchangers - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * MCH PACKAGE EDIT * - ******************************** - - - Machinery - (Currently treated as part of FL) - - ===================== - Time-Dependent data - ===================== - - - ******************************** - * CCF PACKAGE EDIT * - ******************************** - - - Counter Current Flow limit through coupled paths - - - end OF EDIT FOR FL - - - - ***** CONTROL VOLUME THERMODYNAMICS STATISTICS EDIT ***** - VALUES SINCE LAST EDIT - - - CALLS TO MAIN PROGRAM (CVTHRM) = 23498 - NUMBER OF CONTROL VOLUMES PROCESSED = 46996 - CALLS TO WATER EQUILIBRIUM PACKAGE (CVTWE) = 0 - CALLS TO GAS EQUILIBRIUM PACKAGE (CVTGE) = 0 - CALLS TO WATER + GAS EQUILIBRIUM PACKAGE (CVTWGE) = 11749 - STATISTICS ON WATER + GAS EQUILIBRIUM PACKAGE - NUMBER OF TEMPERATURE ITERATIONS = 0 - AVERAGE TEMPERATURE ITERATIONS PER CALL = 0.00000E+00 - NUMBER OF DENSITY ITERATIONS = 0 - AVERAGE DENSITY ITERATIONS PER CALL = 0.00000E+00 - AVERAGE DENSITY ITERATIONS PER TEMPERATURE ITERATION = 0.00000E+00 - CALLS TO WATER + GAS NON-EQUILIBRIUM PACKAGE (CVTNEQ) = 23498 - STATISTICS ON WATER + GAS NON-EQUILIBRIUM PACKAGE - NUMBER OF ITERATIONS = 0 - AVERAGE ITERATIONS PER CALL = 0.00000E+00 - - - - - ************************************ - * CONTROL FUNCTION EDIT * - ************************************ - - - - NUMBER OF CONTROL FUNCTIONS = 2 - NUMBER OF REAL VALUED CONTROL FUNCTIONS = 2 - NUMBER OF LOGICAL VALUED CONTROL FUNCTIONS = 0 - NUMBER OF ARGUMENTS = 2 - - - CONTROL FUNCTION NUMBER CURRENT VALUE - ZERO 1 0.00000E+00 - Test CF 2 2.00010E+04 - - END OF EDIT FOR CF - - END OF EDIT FOR TF - - - H2O PACKAGE CALL STATISTICS - - - CALLS TO H2OEST H2O1PH H2O2PH H2OSAT H2OSAU H2O2PD H2O2PL - EDIT 3.614E+05 1.137E+05 3.567E+05 7.050E+02 1.292E+05 0.000E+00 2.350E+04 - RUN 1.815E+06 6.660E+05 1.770E+06 3.003E+03 5.584E+05 1.828E+04 1.015E+05 - - Not Quite Equilibrium model is disabled - - END OF EDIT FOR ESF - - - - DT CALCULATION SUMMARY - - DT= 2.00000E-01 DTMAX= 2.00000E-01 DTMIN= 1.00000E-10 - DT CONTROL=(MAX, -1) DT CUTS= 0 - DT(CVH)= 1.82000E+00 - DT(LAST CYCLE)= 2.00000E-01 - THIS EXECUTION LOCAL AVERAGE - NUMBER OF COMPLETED CYCLE = 50765 - NUMBER OF FALLBACKS = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXDTH 1/2 DT) = 0 0.0000E+00 - NUMBER OF FALLBACKS (MEXLOP) = 0 0.0000E+00 - NUMBER OF CVH SUBCYCLES PER CYCLE = 1.000 1.0000E+00 - Restart written TIME = 1.000002E+04 CYCLE= 50764 - - - FOR THIS RUN THERE WERE - - PLOT TIME RECORDS = 1001 - - EDIT TIME RECORDS = 6 - - START MESSAGE FILE ************* - - MELCOR message output IRDLAIV 4/09/18 11:03:49 - TEST_1 - Listing written TIME= 0.00000E+00 CYCLE= 0 - Listing written TIME= 1.50063E+02 CYCLE= 1514 - Restart written TIME = 1.500628E+02 CYCLE= 1514 - Restart written TIME = 1.150021E+03 CYCLE= 6514 - Restart written TIME = 2.150021E+03 CYCLE= 11514 - Listing written TIME= 2.65002E+03 CYCLE= 14014 - Restart written TIME = 3.150021E+03 CYCLE= 16514 - Restart written TIME = 4.150021E+03 CYCLE= 21514 - Listing written TIME= 5.15002E+03 CYCLE= 26514 - Restart written TIME = 5.150021E+03 CYCLE= 26514 - Restart written TIME = 6.150021E+03 CYCLE= 31514 - Restart written TIME = 7.150021E+03 CYCLE= 36514 - Listing written TIME= 7.65002E+03 CYCLE= 39014 - Restart written TIME = 8.150021E+03 CYCLE= 41514 - Restart written TIME = 9.150021E+03 CYCLE= 46514 - Listing written TIME= 1.00000E+04 CYCLE= 50764 - Restart written TIME = 1.000002E+04 CYCLE= 50764 - Begin normal termination - Time 10000.0212728003 - CPU 8.37341200000000 - Relative Energy Error -5.754070000000000E-015 - CVH-H2O-RELERR 3.998693332606853E-012 - Normal termination TIME= 1.00000E+04 CYCLE= 50764 CPU = 8.37341E+00 diff --git a/tests/framework/CodeInterfaceTests/gold/MelcorInterface/dumpMelcorPointSet.csv b/tests/framework/CodeInterfaceTests/gold/MelcorInterface/dumpMelcorPointSet.csv index 50a174deea..29315db912 100644 --- a/tests/framework/CodeInterfaceTests/gold/MelcorInterface/dumpMelcorPointSet.csv +++ b/tests/framework/CodeInterfaceTests/gold/MelcorInterface/dumpMelcorPointSet.csv @@ -1,4 +1,4 @@ -%PRE%,time,volume_2_CVVELO(1),volume_2_DENSITY,volume_2_VOLVAP,volume_2_TLIQ,volume_1_VOLVAP,ZERO,Test CF -10000000.5154,10000.0,1.2565e-05,213.01,22.57,583.1678,30.0,0.0,20001.0 -9999998.8652,10000.0,1.2565e-05,213.01,22.57,583.1678,30.0,0.0,20001.0 -10000000.2344,10000.0,1.2565e-05,213.01,22.57,583.1678,30.0,0.0,20001.0 +%PRE%,CVH-P_1,CFVALU_2 +10000000.5154,10000001.0,1981.08435059 +9999998.8652,9999999.0,1981.08435059 +10000000.2344,10000001.0,1981.08435059 diff --git a/tests/framework/CodeInterfaceTests/gold/MelcorInterface/testMelcor/1/test.i b/tests/framework/CodeInterfaceTests/gold/MelcorInterface/testMelcor/1/test.i index f48376d8a1..566acd6563 100644 --- a/tests/framework/CodeInterfaceTests/gold/MelcorInterface/testMelcor/1/test.i +++ b/tests/framework/CodeInterfaceTests/gold/MelcorInterface/testMelcor/1/test.i @@ -12,7 +12,7 @@ MEL_OUTPUTFILE 'OUTPUT_MELCOR.out' !EXTDIAGFILE 'EXTDIAG.TXT' ! !************************************************* -!'test_1' +! 'test_1' * !************************************************* ! ! @@ -55,13 +55,12 @@ TF_TAB 2 !n x y 2 100.0 1. ! CF_INPUT ! -CF_ID 'ZERO' 01 EQUALS ! +CF_ID 'ZERO' 1 EQUALS ! CF_SAI 1.0 0.0 0.0 ! CFSCAL CFADCN CFVALR (INITIAL VALUE) CF_ARG 1 ! NARG CHARG ARSCAL ARADCN 1 EXEC-TIME 0.0 0.0 ! -CF_INPUT ! -CF_ID 'Tes CF' 02 EQUALS ! +CF_ID 'Test_CF' 2 EQUALS ! CF_SAI 1.0 0.0 0.0 ! CFSCAL CFADCN CFVALR (INITIAL VALUE) CF_ARG 1 ! NARG CHARG ARSCAL ARADCN 1 EXEC-TIME 2.0 1.0 @@ -69,7 +68,6 @@ CF_ARG 1 ! NARG CHARG ARSCAL ARADCN ! CVH_INPUT ! -! ! cvname icvnum CV_ID 'IN' 1 ! icvthr ipfsw icvact @@ -152,10 +150,10 @@ Program MELCOR !* Block: MEX (Exec) data **************************** EXEC_INPUT EXEC_TITLE test_1 ! Title of the calculation -EXEC_TEND 10.0E+03 !* ! End of calculation time +EXEC_TEND 10.0E+02 !* ! End of calculation time EXEC_TIME 2 !*NUMBER TIME DTMAX DTMIN DTEDT DTPLT DTRST DCRST - 1 0.00 0.1000E+00 0.10000E-06 2.50000E+03 1.00000E+01 1.00000E+03 0.10000000E+11 - 2 1.50000E+02 0.2000E+00 0.10000E-09 2.50000E+03 1.00000E+01 1.0000E+03 0.10000000E+11 + 1 0.00 0.5000E+00 0.10000E-06 2.50000E+03 1.00000E+01 1.00000E+03 0.10000000E+11 + 2 1.50000E+03 0.5000E+00 0.10000E-09 2.50000E+03 1.00000E+01 1.0000E+03 0.10000000E+11 EXEC_CPULEFT 1000. ! cpu sec left at end of calculation EXEC_CPULIM 4000000. ! Maximum number of CPU seconds allowed for this execution diff --git a/tests/framework/CodeInterfaceTests/test_melcor_interface.xml b/tests/framework/CodeInterfaceTests/test_melcor_interface.xml index 1e9468a241..6962a1e210 100644 --- a/tests/framework/CodeInterfaceTests/test_melcor_interface.xml +++ b/tests/framework/CodeInterfaceTests/test_melcor_interface.xml @@ -3,20 +3,18 @@ framework/CodeInterfaceTests.melcorInterfaceForwardSamplingNoExe - alfoa - 2017-04-27 + mattdon + 2023-02-20 Models.Code.Melcor An example of using the Melcor 2.1/2.2 code interface. This test is aimed to test the mechanics of the interface (no executable). - Adding this test description. - Added csv xml node in the Code block for showing how to use it. + Adding this test description. + Modified csv file for new interface test - - MelcorInterface testMelcor,dumpResults @@ -29,16 +27,13 @@ - MELCOR_2.2/bin/melcor - MELCOR_2.2/bin/melgen - - True + /home/administrator/projects/melcor/MELCOR-2.2.18019/binaries/Linux/01_Melcor.18019.lic + /home/administrator/projects/melcor/MELCOR-2.2.18019/binaries/Linux/00_Melgen.18019.lic + + CVH-P_1$, CVH-TLIQ_2$, CFVALU_2 + + MELPTF.PTF + MELMES_v2-0 @@ -65,19 +60,11 @@ %PRE% - time,volume_2_CVVELO(1),volume_2_DENSITY,volume_2_VOLVAP,volume_2_TLIQ,volume_1_VOLVAP, ZERO, Test CF + CVH-P_1, CFVALU_2 - - %PRE% - time,volume_2_CVVELO(1),volume_2_DENSITY,volume_2_VOLVAP,volume_2_TLIQ,volume_1_VOLVAP, ZERO, Test CF - - - csv - MelcorHistorySet - csv MelcorPointSet @@ -91,13 +78,10 @@ MELGEN MC_samp DataMELCOR - MelcorHistorySet MelcorPointSet - MelcorHistorySet MelcorPointSet - dumpMelcorHistorySet dumpMelcorPointSet diff --git a/tests/framework/CodeInterfaceTests/tests b/tests/framework/CodeInterfaceTests/tests index bcebbbca66..5f16aeecf5 100644 --- a/tests/framework/CodeInterfaceTests/tests +++ b/tests/framework/CodeInterfaceTests/tests @@ -78,6 +78,7 @@ output = 'GenericInterface/samples.xml GenericInterface/sample/1/testSubDirectory/dummy_file_for_subdirectory.dummy GenericInterface/sample/testSubDirectory/dummy_file_for_subdirectory.dummy' csv = 'GenericInterface/samples.csv' [../] + [./genericInterfaceParallel] type = 'RavenFramework' input = 'generic_parallel.xml' @@ -116,7 +117,6 @@ [./melcorInterfaceForwardSamplingNoExe] type = 'RavenFramework' input = 'test_melcor_interface.xml' - output = 'MelcorInterface/dumpMelcorHistorySet_2.csv MelcorInterface/dumpMelcorHistorySet.csv' csv = 'MelcorInterface/dumpMelcorPointSet.csv' text = 'MelcorInterface/testMelcor/1/test.i' test_interface_only = True