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chemkin.py
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chemkin.py
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#!/usr/bin/env python
# encoding: utf-8
"""
This module contains several helper functions useful when running Chemkin jobs
from the command line.
"""
import os.path
import subprocess
import csv
import numpy
import logging
import sys
################################################################################
# The directory in which Chemkin is installed
chemkin_path = os.path.abspath(os.path.join(os.path.dirname(__file__),'chemkin_path'))
if os.path.exists(chemkin_path):
with open(chemkin_path, 'r') as f:
CHEMKIN_DIR = os.path.abspath(f.readline())
# The preamble to each Chemkin execution shell script
CHEMKIN_SCRIPT_PREAMBLE = """#!/bin/sh -v
# Define Chemkin running environment
. {0}
""".format(os.path.join(CHEMKIN_DIR, 'bin', 'chemkinpro_setup.ksh'))
################################################################################
# Set logging parameters
logger = logging.getLogger()
logger.setLevel(logging.INFO)
# Create console handler and set level to debug; send everything to stdout
# rather than stderr
ch = logging.StreamHandler(sys.stdout)
ch.setLevel(logging.INFO)
logging.addLevelName(logging.CRITICAL, 'Critical: ')
logging.addLevelName(logging.ERROR, 'Error: ')
logging.addLevelName(logging.WARNING, 'Warning: ')
logging.addLevelName(logging.INFO, '')
formatter = logging.Formatter('%(levelname)s%(message)s')
ch.setFormatter(formatter)
logger.addHandler(ch)
################################################################################
class ChemkinJob(object):
"""
A single (gas-phase) Chemkin job.
"""
def __init__(self, name, chemFile, tempDir):
self.name = name
self.chemFile = os.path.abspath(chemFile)
self.tempDir = os.path.abspath(tempDir)
if not os.path.exists(self.tempDir):
os.makedirs(self.tempDir)
@property
def ascFile(self):
return os.path.join(self.tempDir, '{0}_gas.asc'.format(self.name))
@property
def inputFile(self):
return os.path.join(self.tempDir, '{0}.inp'.format(self.name))
@property
def outputFile(self):
return os.path.join(self.tempDir, '{0}.out'.format(self.name))
@property
def monFile(self):
return os.path.join('{0}.out.mon'.format(self.name))
@property
def ckcsvFile(self):
return os.path.join(self.tempDir, 'CKSoln.ckcsv')
@property
def preferenceFile(self):
return os.path.join(self.tempDir, 'CKSolnList.txt')
@property
def dataZipFile(self):
return os.path.join(self.tempDir, 'XMLdata_{0}.zip'.format(self.name))
def preprocess(self):
"""
Run the Chemkin preprocessor on the chemistry input file.
"""
# Write the preprocessor execution script to a file
scriptFile = os.path.join(self.tempDir, 'RUNJOB_CKPreProcess.sh')
with open(scriptFile, 'w') as stream:
stream.write(CHEMKIN_SCRIPT_PREAMBLE)
stream.write('# Run the Chemkin preprocessor\n')
stream.write('{0} -i {1} -o {2}_gas.out -c {2}_gas.asc\n\n'.format(
os.path.join(CHEMKIN_DIR, 'bin', 'chem'),
os.path.abspath(self.chemFile),
os.path.join(self.tempDir, self.name),
))
# Execute the preprocessor script
process = subprocess.Popen(('/bin/sh', scriptFile), cwd=self.tempDir, stdout=subprocess.PIPE, stderr=subprocess.PIPE)
stdout, stderr = process.communicate()
if process.returncode != 0:
print stdout
print stderr
quit()
def run(self, jobParams, model, pro=True):
"""
Run a Chemkin job.
"""
dtdFileSrc = os.path.join(CHEMKIN_DIR, 'data', 'chemkindata.dtd')
dtdFileDest = os.path.join(self.tempDir, 'chemkindata.dtd')
scriptFile = os.path.join(self.tempDir, 'RUNJOB_CKRunProcessor.sh')
# Write the job parameters to a file
with open(self.inputFile, 'w') as stream:
stream.write(jobParams)
# Write the job execution script to a file
with open(scriptFile, 'w') as stream:
stream.write(CHEMKIN_SCRIPT_PREAMBLE)
stream.write('# Delete any intermediate files left over from a previous run\n')
stream.write('rm -f {0}\n\n'.format(self.dataZipFile))
stream.write('rm -f {0}\n\n'.format(dtdFileDest))
stream.write('# Copy files to working directory\n')
stream.write('ln -s {0} {1}\n'.format(dtdFileSrc, dtdFileDest))
stream.write('# Run the job\n')
if pro:
stream.write('CHEMKIN_MODE=Pro\n')
stream.write('export CHEMKIN_MODE\n')
stream.write('{0} -i {1} -o {2} -x {3} Pro -m {4} -c {5}\n'.format(model, self.inputFile, self.outputFile, self.dataZipFile, self.monFile, self.ascFile))
else:
stream.write('{0} -i {1} -o {2} -x {3} -m {4} -c {5}\n'.format(model, self.inputFile, self.outputFile, self.dataZipFile, self.monFile, self.ascFile))
# Execute the job script
subprocess.call(('/bin/sh', scriptFile), cwd=self.tempDir)
def postprocess(self, sens=False, rop=False, all=False, transpose=True):
"""
Run the Chemkin postprocessor.
"""
# Set default preferences and write them to the preference file
with open(self.preferenceFile, 'w') as stream:
stream.write('VARIABLE VAR ALL\n')
stream.write('VARIABLE SEN ALL\n')
stream.write('VARIABLE ROP ALL\n')
stream.write('VARIABLE volume 1 0 0\n')
stream.write('VARIABLE external_surface_area 0 0 0\n')
stream.write('VARIABLE volumetric_heat_production_rate 0 0 0\n')
stream.write('VARIABLE surface_temperature 0 0 0\n')
stream.write('VARIABLE heat_loss_rate 0 0 0\n')
stream.write('VARIABLE temperature 1 0 0\n')
stream.write('VARIABLE mass 0 0 0\n')
stream.write('VARIABLE pressure 1 0 0\n')
stream.write('VARIABLE molar_conversion 0 0 0\n')
stream.write('VARIABLE net_reaction_rate 0 0 0\n')
stream.write('VARIABLE heat_production_per_reaction 0 0 0\n')
stream.write('VARIABLE molecular_weight 0 0 0\n')
stream.write('VARIABLE mass_density 0 0 0\n')
stream.write('VARIABLE mixture_enthalpy 0 0 0\n')
stream.write('VARIABLE sensible_enthalpy 0 0 0\n')
stream.write('VARIABLE unburned_hydrocarbons 0 0 0\n')
stream.write('VARIABLE volatile_organic_compounds 0 0 0\n')
stream.write('VARIABLE exhaust_in_ppmvd 0 0 0\n')
stream.write('VARIABLE all_single_point_values 0 0 0\n')
stream.write('VARIABLE use_reaction_string_instead_of_index 1 0 0\n')
stream.write('UNIT Time (sec)\n')
stream.write('UNIT Temperature (K)\n')
stream.write('UNIT Pressure (bar)\n')
stream.write('UNIT Volume (cm3)\n')
# Write the postprocessor execution script to a file
scriptFile = os.path.join(self.tempDir, 'RUNJOB_CKPostProcessor.sh')
with open(scriptFile, 'w') as stream:
stream.write(CHEMKIN_SCRIPT_PREAMBLE)
stream.write('# Extract solution data to CKCSV\n')
stream.write('GetSolution {1}{2}{3}{4}{0}\n\n'.format(
self.dataZipFile,
'-nosen ' if not sens else '',
'-norop ' if not rop else '',
'-all ' if all else '',
'-p'+' CKSolnList.txt ',
))
if transpose:
stream.write('# Transpose the data to CSV\n')
stream.write('CKSolnTranspose -column 500 {0}\n\n'.format(self.ckcsvFile))
stream.write('# Delete postprocessor log file\n')
stream.write('rm -f {0}\n\n'.format(os.path.join(self.tempDir, 'ckpp_*.log')))
# Execute the postprocessor script
subprocess.call(('/bin/sh', scriptFile), cwd=self.tempDir)
def writeInputHomogeneousBatch(self,problemType, reactants, temperature, pressure, endTime,
Continuations=False, typeContinuation = None, Tlist = [], Plist = [],
variableVolume=False, variableVolumeProfile = None,
solverTimeStepProfile = None):
"""
Write input file for homogeneous batch reactor
"""
# Problem definition block
input_stream=("""
!
! problem type definition
!""")
if problemType.lower() == 'constrainVandSolveE'.lower():
input_stream+=("""
CONV ! Constrain Volume And Solve Energy Equation
ENRG ! Solve Gas Energy Equation""")
elif problemType.lower() == 'constrainPandSolveE'.lower():
input_stream+=("""
ENRG ! Solve Gas Energy Equation""")
elif problemType.lower() == 'constrainPandT'.lower():
input_stream+=("""
TGIV ! Constrain Pressure And Temperature
""")
elif problemType.lower() == 'constrainVandT'.lower():
input_stream+=("""
COTV ! Constrain Volume And Temperature
TGIV ! Fix Gas Temperature""")
# Solver type definition block
input_stream+=("""
TRAN ! Transient Solver""")
# Physical property
input_stream+=("""
!
! physical property
!
!Surface_Temperature ! Surface Temperature Same as Gas Temperature
IFAC 0.1 ! Ignition Noise Filtering Factor
""")
input_stream+=('PRES {0:g} ! Pressure (atm)\n'.format(pressure/1.01325))
input_stream+=('QLOS 0.0 ! Heat Loss (cal/sec)\n')
input_stream+=('TEMP {0:g} ! Temperature (K)'.format(temperature))
if variableVolume:
with open(variableVolumeProfile, 'rb') as csvfile:
reader = csv.reader(csvfile, delimiter=' ', quotechar='|')
for row in reader:
time = float(row[0].split(',')[0]) # (sec)
vol = float(row[0].split(',')[1]) # (cm3)
input_stream+=("""
VPRO {0:g} {1:g} ! Volume (cm3)""".format(time,vol))
# Species property block
input_stream+=("""
!
! species property
!
""")
for reac , conc in reactants:
input_stream+=('REAC {0} {1:g} ! Reactant Fraction (mole fraction) \n'.format(reac,conc))
# Solver control block
input_stream+=("""!
! solver control
!
ADAP ! Save Additional Adaptive Points
ASTEPS 20 ! Use Solver Integration Steps
ATLS 1.0E-6 ! Sensitivity Absolute Tolerance
ATOL 1.0E-20 ! Absolute Tolerance
MAXIT 4 ! Maximum Number of Iterations
RTLS 0.0001 ! Sensitivity Relative Tolerance
RTOL 1.0E-8 ! Relative Tolerance""")
if solverTimeStepProfile:
with open(solverTimeStepProfile, 'rb') as csvfile2:
timeStepReader = csv.reader(csvfile2, delimiter=' ', quotechar='|')
for row in timeStepReader:
time = float(row[0].split(',')[0]) # (sec)
vol = float(row[0].split(',')[1]) # (sec)
input_stream+=("""
STPTPRO {0:g} {1:g} ! Solver Maximum Step Time (sec)""".format(time,vol))
input_stream+=("""
TIME {0:g} ! End Time (sec)""".format(endTime))
input_stream+=("""
!
! output control and other misc. property
!
EPSR 0.01 ! Threshold for Rate of Production
EPSS 0.001 ! Threshold for Species Sensitivity
EPST 0.001 ! Threshold for Temperature Sensitivity
GFAC 1.0 ! Gas Reaction Rate Multiplier
PRNT 1 ! Print Level Control
SIZE 10000000 ! Solution Data Block Size (bytes)""")
if Continuations:
if numpy.array(Tlist).size:
for i in range(numpy.array(Tlist).shape[0]):
input_stream+=("""
{0}
END
TEMP {1:g}""".format(typeContinuation,numpy.array(Tlist)[i]))
if numpy.array(Plist).size:
for i in range(numpy.array(Plist).shape[0]):
input_stream+=("""
{0}
END
PRES {1:g}""".format(typeContinuation,numpy.array(Plist)[i]/1.01325))
input_stream+=('\nEND')
return input_stream
def writeInputPlugFlow(self,problemType, reactants,
startingAxialPosition, endingAxialPosition, diameter, momentum=True, massflowrate = None, sccmflowrate = None,
temperature = None, pressure = None,
temperatureProfile = None, pressureProfile = None):
"""
Write input file for typical plug flow
"""
# Problem definition block
input_stream=("""
!
! problem type definition
!
""")
if momentum:
input_stream+=("""
MOMEN ON ! Turn on Momentum Equation
""")
else:
input_stream+=("""
MOMEN OFF ! Turn off Momentum Equation
""")
input_stream+=("""
PLUG ! Plug Flow Reactor
RTIME ON ! Turn on Residence Time Calculation
""")
if problemType.lower() == 'FixGasTemperature'.lower():
input_stream+=("""
TGIV ! Fix Gas Temperature""")
elif problemType.lower() == 'solveGasEnergy'.lower():
input_stream+=("""
ENRG ! Solve Gas Energy Equation""")
# Physical property
input_stream+=("""
!
! physical property
!
!Surface_Temperature ! Surface Temperature Same as Gas Temperature
""")
if massflowrate:
input_stream+=('FLRT {0:g} ! Mass Flow Rate (g/sec)\n'.format(massflowrate))
elif sccmflowrate:
input_stream+=('SCCM {0:g} ! Volumetric Flow Rate in SCCM (standard-cm3/min@298.15K)\n'.format(sccmflowrate))
else:
raise Exception('Must indicate either a mass or sccm flow rate')
if pressureProfile:
with open(pressureProfile, 'rb') as csvfile:
reader = csv.reader(csvfile, delimiter=' ', quotechar='|')
for row in reader:
pos = float(row[0].split(',')[0]) # (cm)
pres = float(row[0].split(',')[1])*1.0/1.01325 # (atm)
input_stream+=("""
PPRO {0:g} {1:g} ! Pressure (atm)""".format(pos,pres))
else:
input_stream+=('PRES {0:g} ! Pressure (atm)\n'.format(pressure/1.01325))
if temperatureProfile:
with open(temperatureProfile, 'rb') as csvfile:
reader = csv.reader(csvfile, delimiter=' ', quotechar='|')
for row in reader:
pos = float(row[0].split(',')[0]) # (cm)
temp = float(row[0].split(',')[1]) # (K)
input_stream+=("""
TPRO {0:g} {1:g} ! Temperature (K)""".format(pos,temp))
else:
input_stream+=('TEMP {0:g} ! Temperature (K)'.format(temperature))
# reactor dimension definition
input_stream+=("""
VIS 0.0 ! Mixture Viscosity at Inlet (g/cm-sec)
!
! reactor dimension definition
!
""")
input_stream+=('DIAM {0:g} ! Diameter (cm)\n'.format(diameter))
input_stream+=('XEND {0:g} ! Ending Axial Position (cm)\n'.format(endingAxialPosition))
input_stream+=('XSTR {0:g} ! Starting Axial Position (cm)\n'.format(startingAxialPosition))
# Species property block
input_stream+=("""
!
! species property
!
""")
for reac , conc in reactants:
input_stream+=('REAC {0} {1:g} ! Reactant Fraction (mole fraction) \n'.format(reac,conc))
# Solver control block
input_stream+=("""!
!
! solver control
!
ACHG 0.0 ! Maximum Absolute Change in Site Fractions
ADAP ! Save Additional Adaptive Points
ATLS 1.0E-6 ! Sensitivity Absolute Tolerance
ATOL 1.0E-9 ! Absolute Tolerance
MAXIT 4 ! Maximum Number of Iterations
NNEG ! Force Non-negative Solution
PSV 1.0E-8 ! Scaling Factor for Relaxing Surface Equations (cm/sec)
RCHG 1.0E-6 ! Maximum Relative Change in Site Fractions
RTLS 0.0001 ! Sensitivity Relative Tolerance
RTOL 1.0E-6 ! Relative Tolerance
TSTP 1.0 ! Initial Integration Step (cm""")
input_stream+=("""
!
! output control and other misc. property
!
GFAC 1.0 ! Gas Reaction Rate Multiplier""")
input_stream+=('\nEND')
return input_stream
def writeinputJSR(self,problemType, reactants, tau,endtime, volume,
temperature = None, pressure = None,
Continuations=False, typeContinuation = None, Tlist = [], Plist = [],
temperatureProfile = None, pressureProfile = None):
"""
Write input file for JSR
"""
# Problem definition block
input_stream=("""
!
! problem type definition
!
TRAN ! Transient Solver
""")
if problemType.lower() == 'FixGasTemperature'.lower():
input_stream+=("""
TGIV ! Fix Gas Temperature""")
elif problemType.lower() == 'solveGasEnergy'.lower():
input_stream+=("""
ENRG ! Solve Gas Energy Equation""")
# Physical property
input_stream+=("""
!
! physical property
!
!Surface_Temperature ! Surface Temperature Same as Gas Temperature
""")
if pressureProfile:
with open(pressureProfile, 'rb') as csvfile:
reader = csv.reader(csvfile, delimiter=' ', quotechar='|')
for row in reader:
pos = float(row[0].split(',')[0]) # (cm)
pres = float(row[0].split(',')[1])*1.0/1.01325 # (atm)
input_stream+=("""
PPRO {0:g} {1:g} ! Pressure (atm)""".format(pos, pres))
else:
input_stream+=('PRES {0:g} ! Pressure (atm)\n'.format(pressure/1.01325))
# Residence time
input_stream+=('TAU {0:g} ! Residence time (sec)\n'.format(tau))
if temperatureProfile:
with open(temperatureProfile, 'rb') as csvfile:
reader = csv.reader(csvfile, delimiter=' ', quotechar='|')
for row in reader:
pos = float(row[0].split(',')[0]) # (cm)
temp = float(row[0].split(',')[1]) # (K)
input_stream+=("""
TPRO {0:g} {1:g} ! Temperature (K)""".format(pos,temp))
else:
input_stream+=('TEMP {0:g} ! Temperature (K)\n'.format(temperature))
# volume
input_stream+=('VOL {0:g} ! Volume (cm3)\n'.format(volume))
# Species property block
input_stream+=("""
!
! species property
!
""")
for reac , conc in reactants:
input_stream+=('REAC {0} {1:g} ! Reactant Fraction (mole fraction) \n'.format(reac,conc))
# For transient solver you also need estimates of species initial gas fraction
for reac , conc in reactants:
input_stream+=('XEST {0} {1:g} ! Initial Gas Fraction (mole fraction) \n'.format(reac,conc))
# solver control
input_stream+=("""
!
! solver control
!
ADAP ! Save Additional Adaptive Points
""")
input_stream+=('TIME {0:g} ! End Time (sec) \n'.format(endtime))
# output control and other misc. property
input_stream+=("""
!
! output control and other misc. property
!
GFAC 1.0 ! Gas Reaction Rate Multiplier
""")
if Continuations:
if numpy.array(Tlist).size:
for i in range(numpy.array(Tlist).shape[0]):
input_stream+=("""
{0}
END
TEMP {1:g}""".format(typeContinuation,numpy.array(Tlist)[i]))
if numpy.array(Plist).size:
for i in range(numpy.array(Plist).shape[0]):
input_stream+=("""
{0}
END
PRES {1:g}""".format(typeContinuation,numpy.array(Plist)[i]/1.01325))
input_stream+=('\nEND')
return input_stream
################################################################################
def getVariable(ckcsvFile, variable=None):
"""
Return the time and variable data (i.e. Pressure, Volume, or Temperature) from the given CKCSV file. Returns the data
in the form of [time_soln1, timesoln2, ...] [variable_data_soln1, variable_data_soln2,...]
Returns time in units of [seconds]. Returns temperature in units of [K].
Returns pressure in units of [bar]. Returns volume in units of [cm3].
"""
if variable.lower() not in ['pressure','volume','temperature']:
raise Exception('Can only parse Pressure, Volume, or Temperature from CKCSV file.')
timeData = []; varData = []
units = {'k': 1.0, 'bar': 1, 'mpa': 10, 'pa': 1e-5, 'atm': 1.01325, 'cm3': 1.0, 'm3': 1e6}
with open(ckcsvFile, 'r') as stream:
reader = csv.reader(stream)
for row in reader:
label = row[0].strip()
tokens = label.split('_')
if tokens[0] == 'Time':
tdata = numpy.array([float(r) for r in row[2:]], numpy.float)
tunits = row[1].strip()[1:-1].lower()
tdata *= {'sec': 1.0, 'min': 60., 'hr': 3600., 'msec': 1e-3, 'microsec': 1e-6}[tunits]
timeData.append(tdata)
if tokens[0].lower() == variable.lower():
vdata = numpy.array([float(r) for r in row[2:]], numpy.float)
vunits = row[1].strip()[1:-1].lower()
vdata = vdata*units[vunits]
varData.append(vdata)
return timeData, varData
def getMoleFraction(ckcsvFile, species=[]):
"""
Return the time and mole fraction data from the given CKCSV file. Returns the data
in the form of [time_soln1, timesoln2, ...] specdata[species_name]=[spec_molefrac_soln1, spec_molefrac_soln2,...].
Time is returned in units of [seconds].
"""
timeData = []; distanceData = []; specData = {}
for spec in species:
specData[spec] = []
with open(ckcsvFile, 'r') as stream:
reader = csv.reader(stream)
for row in reader:
label = row[0].strip()
tokens = label.split('_')
if tokens[0] == 'Time':
tdata = numpy.array([float(r) for r in row[2:]], numpy.float)
tunits = row[1].strip()[1:-1].lower()
tdata *= {'sec': 1.0, 'min': 60., 'hr': 3600., 'msec': 1e-3, 'microsec': 1e-6}[tunits]
timeData.append(tdata)
if tokens[0] == 'Distance':
ddata = numpy.array([float(r) for r in row[2:]], numpy.float)
dunits = row[1].strip()[1:-1].lower()
ddata *= {'cm': 1.0, 'mm': 0.1, 'm': 100.}[dunits]
distanceData.append(ddata)
if label.startswith('Mole_fraction'):
for spec in species:
if tokens[2] == spec:
specData[spec].append(numpy.array([float(r) for r in row[2:]], numpy.float))
if timeData:
return timeData, specData
elif distanceData:
return distanceData, specData
else:
return
def getTotalMoles(ckcsvFile):
"""
Return the time and total moles data from the given CKCSV file.
Returns the data in the form of [time_soln1, timesoln2, ...], [total_moles_soln1, total_moles_soln2, ...]
Moles is returned in units of [moles].
"""
tempData = []; presData = []; volData = []; totalMolesData = []
with open(ckcsvFile, 'r') as stream:
reader = csv.reader(stream)
for row in reader:
label = row[0].strip()
tokens = label.split('_')
if tokens[0] == 'Temperature':
Tdata = numpy.array([float(r) for r in row[2:]], numpy.float)
Tunits = row[1].strip()[1:-1].lower()
try:
Tdata *= {'k': 1.0}[Tunits]
except KeyError:
print 'Unknown units {0} for temperature. Cannot obtain total moles.'.format(Tunits)
tempData.append(Tdata)
if tokens[0] == 'Pressure':
Pdata = numpy.array([float(r) for r in row[2:]], numpy.float)
Punits = row[1].strip()[1:-1].lower()
try:
Pdata *= {'bar': 0.1, 'mpa': 1.0, 'pa': 1e-6, 'atm': 0.101325}[Punits]
except KeyError:
print 'Unknown units {0} for pressure. Cannot obtain total moles.'.format(Punits)
presData.append(Pdata)
if tokens[0] == 'Volume':
Vdata = numpy.array([float(r) for r in row[2:]], numpy.float)
Vunits = row[1].strip()[1:-1].lower()
try:
Vdata *= {'cm3': 1.0, 'm3': 1e6}[Vunits]
except KeyError:
print 'Unknown units {0} for volume. Cannot obtain total moles.'.format(Vunits)
volData.append(Vdata)
R = 8.3145
for i in range(len(tempData)):
totalMolesData.append(presData[i]*volData[i]/R/tempData[i])
return totalMolesData
################################################################################
def getIgnitionDelay(ckcsvFile, tol=1.0, species = []):
"""
Return the ignition delay time from the given CKCSV file. This function
uses (dP/dt)_max to find the ignition delay time. A ValueError is raised if
this dP/dt value is below a certain threshold.
Alternatively, provide a list of species which are maximized at tau.
If the list contains a single species label, ie. ['OH'] the ignition delay will be given as the
time at which the concentraiton of that species is maximized. If a list of species is given,
then the multiplicative max of the concentrations of those species is returned. ie. if
it is desired to calculated the ignition delay using max([CH][O]), then the species list
['CH','O'] should be inputted.
"""
tdata = None; Pdata = None; specdata = []
with open(ckcsvFile, 'r') as stream:
reader = csv.reader(stream)
for row in reader:
label = row[0].strip()
if label.startswith('Time'):
tdata = numpy.array([float(r) for r in row[2:]], numpy.float)
tunits = row[1].strip()[1:-1].lower()
tdata *= {'sec': 1.0, 'min': 60., 'hr': 3600., 'msec': 1e-3, 'microsec': 1e-6}[tunits]
elif label.startswith('Pressure'):
Pdata = numpy.array([float(r) for r in row[2:]], numpy.float)
Punits = row[1].strip()[1:-1].lower()
Pdata *= {'dyne/cm2': 0.1, 'atm': 101325., 'Pa': 1.0, 'bar': 1e5, 'torr': 133.322368, 'mtorr': 0.133322368, 'psi': 6894.75729}[Punits] * 1e-5
for spec in species:
if spec in label:
specdata.append(numpy.array([float(r) for r in row[2:]], numpy.float))
if tdata is None or Pdata is None:
raise Exception('Unable to read time and/or pressure data from the given CKCSV file.')
if species:
if len(species) == 1:
max_index = specdata[0].argmax()
OHmetric = max(specdata[0])/2 # 0.0015136805 the particular value for GRI-Mech 3.0
mindata = abs(specdata[0][0:max_index]-OHmetric)
index = mindata.argmin()
return tdata[index]
else:
multdata = numpy.ones(len(specdata[0]))
ind1 = specdata[0].argmax()
ind2 = specdata[1].argmax()
for spec in specdata:
multdata *= spec
print multdata
print tdata
print 'time max for species 1'
print tdata[ind1]
print 'time max for species 2'
print tdata[ind2]
index = multdata.argmax()
print 'time max for multiplied together'
print tdata[index]
return tdata[index]
else:
dPdt = (Pdata[1:] - Pdata[:-1]) / (tdata[1:] - tdata[:-1])
dPdt = dPdt[numpy.isfinite(dPdt)]
#index = dPdt.argmax()
index = next(i for i,d in enumerate(dPdt) if d==max(dPdt))
if dPdt[index] < tol:
raise ValueError('No ignition occurred in the given simulation.')
return 0.5 * (tdata[index] + tdata[index+1])
################################################################################
def runIgnitionReactionSensitivity(runChemkinJob, inputFile, dictionaryFile):
"""
Supply a runChemkinJob python function which returns the ignition delay with a
chemkin file input. This will run finite difference reaction sensitivities and
save them to a csv file.
"""
from rmgpy.chemkin import loadChemkinFile, saveChemkinFile
speciesList, reactionList = loadChemkinFile(inputFile, dictionaryPath = dictionaryFile, readComments = False)
num_reactions = len(reactionList)
factor_high = 1.05
factor_low = 1. / factor_high
worksheet = csv.writer(file('ignition_rxn_sensitivity.csv', 'w'))
worksheet.writerow(['Index', 'Reaction', 'd[ln k]','tau_high','tau_low','d[ln tau]/d[ln k]'])
logging.info('Running reaction sensitivity analysis using finite differences...')
for index, reaction in enumerate(reactionList):
rxn_index = index + 1
rxn_string = reaction.toChemkin(kinetics = False)
logging.info('At reaction {0} of {1}. {2}'.format(rxn_index, num_reactions, rxn_string))
reaction.kinetics.changeRate(factor_high)
saveChemkinFile('chem_temp.inp', speciesList, reactionList, verbose = False)
tau_high = runChemkinJob('chem_temp.inp')
reaction.kinetics.changeRate(1./factor_high) # reset the kinetics
reaction.kinetics.changeRate(factor_low)
saveChemkinFile('chem_temp.inp', speciesList, reactionList, verbose = False)
tau_low = runChemkinJob('chem_temp.inp')
reaction.kinetics.changeRate(1./factor_low) # reset the kinetics
if tau_high != 0 and tau_low != 0:
sens = numpy.log(tau_high / tau_low) / numpy.log(factor_high / factor_low)
else:
sens = 0
worksheet.writerow([rxn_index, rxn_string, numpy.log(factor_high / factor_low), tau_high, tau_low, sens])
################################################################################
def runIgnitionThermoSensitivity(runChemkinJob, inputFile, dictionaryFile):
"""
Supply a runChemkinJob python function which returns the ignition delay with a
chemkin file input. This will run finite difference sensitivities to enthalpies and
save them to a csv file.
"""
from rmgpy.chemkin import loadChemkinFile, saveChemkinFile, getSpeciesIdentifier
from rmgpy.quantity import Quantity
speciesList, reactionList = loadChemkinFile(inputFile, dictionaryPath = dictionaryFile, readComments = False)
num_species = len(speciesList)
deltaH = Quantity(0.5, 'kcal/mol').value_si
worksheet = csv.writer(file('ignition_thermo_sensitivity.csv', 'w'))
worksheet.writerow(['Species', 'd[del H] (kcal/mol)', 'tau_high', 'tau_low', 'd[ln tau]/d[del H]'])
logging.info('Running thermo sensitivity analysis using finite differences...')
for index, species in enumerate(speciesList):
species_index = index + 1
species_string = getSpeciesIdentifier(species)
logging.info('At species {0} of {1}. {2}'.format(species_index, num_species, species_string))
species.thermo.changeBaseEnthalpy(deltaH)
saveChemkinFile('chem_temp.inp', speciesList, reactionList, verbose = False)
tau_high = runChemkinJob('chem_temp.inp')
species.thermo.changeBaseEnthalpy(-deltaH) # reset the thermo
species.thermo.changeBaseEnthalpy(-deltaH)
saveChemkinFile('chem_temp.inp', speciesList, reactionList, verbose = False)
tau_low = runChemkinJob('chem_temp.inp')
species.thermo.changeBaseEnthalpy(deltaH) # reset the kinetics
if tau_high != 0 and tau_low != 0:
sens = numpy.log(tau_high / tau_low) / (2 * deltaH)
else:
sens = 0
worksheet.writerow([species_string, '1', tau_high, tau_low, sens])
def getIgnitionDelayOH(ckcsvFile, tol=1.0):
"""
Return the ignition delay time from the given CKCSV file. This function
uses (OH)_max to find the ignition delay time.
"""
tdata = None; OHdata = None
with open(ckcsvFile, 'r') as stream:
reader = csv.reader(stream)
for row in reader:
label = row[0].strip()
if label.startswith('Time'):
tdata = numpy.array([float(r) for r in row[2:]], numpy.float)
tunits = row[1].strip()[1:-1].lower()
tdata *= {'sec': 1.0, 'min': 60., 'hr': 3600., 'msec': 1e-3, 'microsec': 1e-6}[tunits]
elif label.startswith('Mole_fraction_OH'):
OHdata = numpy.array([float(r) for r in row[2:]], numpy.float)
if tdata is None or OHdata is None:
raise Exception('Unable to read time and/or OH data from the given CKCSV file.')
OHdata = OHdata[numpy.isfinite(OHdata)]
index = OHdata.argmax()
if index == len(OHdata)-1:
raise ValueError('No ignition occurred in the given simulation.')
return 0.5 * (tdata[index])
################################################################################
def getPeakOQOOHTime(ckcsvFile,spc, tol=1.0):
"""
Return the ignition delay time from the given CKCSV file. This function
uses (OQOOH)_max to find the ignition delay time.
"""
tdata = None; OQOOHdata = None
spc_label = 'Mole_fraction_'+spc
with open(ckcsvFile, 'r') as stream:
reader = csv.reader(stream)
for row in reader:
label = row[0].strip()
if label.startswith('Time'):
tdata = numpy.array([float(r) for r in row[2:]], numpy.float)
tunits = row[1].strip()[1:-1].lower()
tdata *= {'sec': 1.0, 'min': 60., 'hr': 3600., 'msec': 1e-3, 'microsec': 1e-6}[tunits]
elif label.startswith(spc_label):
OQOOHdata = numpy.array([float(r) for r in row[2:]], numpy.float)
if tdata is None or OQOOHdata is None:
raise Exception('Unable to read time and/or OH data from the given CKCSV file.')
OQOOHdata = OQOOHdata[numpy.isfinite(OQOOHdata)]
index = OQOOHdata.argmax()
if index == len(OQOOHdata)-1:
raise ValueError('No OQOOH peak found in the given simulation.')
return (tdata[index])
################################################################################
def getIgnitionDelayStage1(ckcsvFile,stepsize = 1500,tol=1.0):
"""
Return the ignition delay time from the given CKCSV file. This function
uses (d2T/dt2) inflection to find the first stage ignition delay time. A ValueError is raised if
this dT/dt value is below a certain threshold.
"""
tdata = None; Tdata = None
with open(ckcsvFile, 'r') as stream:
reader = csv.reader(stream)
for row in reader:
label = row[0].strip()
if label.startswith('Time'):
tdata = numpy.array([float(r) for r in row[2:]], numpy.float)
tunits = row[1].strip()[1:-1].lower()
tdata *= {'sec': 1.0, 'min': 60., 'hr': 3600., 'msec': 1e-3, 'microsec': 1e-6}[tunits]
elif label.startswith('Temperature'):
Tdata = numpy.array([float(r) for r in row[2:]], numpy.float)
if tdata is None or Tdata is None:
raise Exception('Unable to read time and/or temperature data from the given CKCSV file.')
from scipy import interpolate
s = interpolate.interp1d(tdata[:], Tdata[:])
xs = numpy.linspace(0.0, tdata[-1], stepsize)
ys = s(xs)
dT_dt = (ys[1:]-ys[:-1])/(xs[1:]-xs[:-1])
xs1 = xs[1:]
dT2_dt2 = (dT_dt[1:]-dT_dt[:-1])/(xs1[1:]-xs1[:-1])
xs2 = xs1[1:]
try:
time_index_Tinflection = next(x[0] for x in enumerate(dT2_dt2) if x[1] < -100 )
except StopIteration:
raise ValueError('No T kink found.')
#time_index_Tinflection = len(xs2)
Time_inflection = xs2[time_index_Tinflection]
return Time_inflection
################################################################################