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Cantera CTML writer
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units(length = "cm", time = "s", quantity = "mol", act_energy = "cal/mol") | |
RedlichKwongMFTP(name = "carbondioxide", | |
elements = " C O H ", | |
species = """ CO2 H2O """, | |
activity_coefficients = (pureFluidParameters(species="CO2", a_coeff = [7.54e12, -4.13e9], b_coeff = 27.80), | |
pureFluidParameters(species="H2O", a_coeff = [1.7458E13, -8.0E9], b_coeff = 18.18), | |
crossFluidParameters(species="CO2 H2O", a_coeff = [7.897e12, 0]) ), | |
initial_state = state(temperature = 300.0, | |
pressure = OneAtm, | |
mole_fractions = 'CO2:0.9999, H2O:0.0001') ) | |
#------------------------------------------------------------------------------- | |
# Species data | |
#------------------------------------------------------------------------------- | |
species(name = "CO2", | |
atoms = " C:1 O:2 ", | |
thermo = ( | |
NASA( [ 200.00, 1000.00], [ 2.356773520E+00, 8.984596770E-03, | |
-7.123562690E-06, 2.459190220E-09, -1.436995480E-13, | |
-4.837196970E+04, 9.901052220E+00] ), | |
NASA( [ 1000.00, 3500.00], [ 3.857460290E+00, 4.414370260E-03, | |
-2.214814040E-06, 5.234901880E-10, -4.720841640E-14, | |
-4.875916600E+04, 2.271638060E+00] ) | |
), | |
) | |
species(name = "H2O", | |
atoms = " H:2 O:1 ", | |
thermo = ( | |
NASA( [ 273.00, 1000.00], [ 4.198640560E+00, -2.036434100E-03, | |
6.520402110E-06, -5.487970620E-09, 1.771978170E-12, | |
-3.029372670E+04, -8.490322080E-01] ), | |
NASA( [ 1000.00, 1600.00], [ 3.033992490E+00, 2.176918040E-03, | |
-1.640725180E-07, -9.704198700E-11, 1.682009920E-14, | |
-3.000429710E+04, 4.966770100E+00] ) | |
), | |
) |
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#!/usr/bin/env python | |
## | |
# @file ctml_writer.py | |
# | |
# Cantera .cti input file processor | |
# @defgroup pygroup Cantera Python Interface | |
# | |
# The functions and classes in this module process Cantera .cti input | |
# files and produce CTML files. It can be imported as a module, or used | |
# as a script. | |
# | |
# script usage: | |
# | |
# python ctml_writer.py infile.cti | |
# | |
# This will produce CTML file 'infile.xml' | |
from __future__ import print_function | |
class CTI_Error(Exception): | |
"""Exception raised if an error is encountered while | |
parsing the input file. | |
@ingroup pygroup""" | |
def __init__(self, msg): | |
print('\n\n***** Error parsing input file *****\n\n') | |
print(msg) | |
print() | |
indent = ['', | |
' ', | |
' ', | |
' ', | |
' ', | |
' ', | |
' ', | |
' ', | |
' ', | |
' ', | |
' ', | |
' ', | |
' ', | |
' ', | |
' ', | |
' '] | |
#----------------------------------------------------- | |
class XMLnode(object): | |
"""This is a minimal class to allow easy creation of an XML tree | |
from Python. It can write XML, but cannot read it.""" | |
def __init__(self, name="--", value = ""): | |
"""Create a new node. Usually this only needs to be explicitly | |
called to create the root element. Method addChild calls this | |
constructor to create the new child node.""" | |
self._name = name | |
# convert 'value' to a string if it is not already, and | |
# strip leading whitespace | |
if not isinstance(value, str): | |
self._value = repr(value).lstrip() | |
else: | |
self._value = value.lstrip() | |
self._attribs = {} # dictionary of attributes | |
self._children = [] # list of child nodes | |
self._childmap = {} # dictionary of child nodes | |
def name(self): | |
"""The tag name of the node.""" | |
return self._name | |
def nChildren(self): | |
"""Number of child elements.""" | |
return len(self._children) | |
def addChild(self, name, value=""): | |
"""Add a child with tag 'name', and set its value if the value | |
parameter is supplied.""" | |
# create a new node for the child | |
c = XMLnode(name = name, value = value) | |
# add it to the list of children, and to the dictionary | |
# of children | |
self._children.append(c) | |
self._childmap[name] = c | |
return c | |
def addComment(self, comment): | |
"""Add a comment.""" | |
self.addChild(name = '_comment_', value = comment) | |
def value(self): | |
"""A string containing the element value.""" | |
return self._value | |
def child(self, name=""): | |
"""The child node with specified name.""" | |
return self._childmap[name] | |
def children(self): | |
""" An iterator over the child nodes """ | |
for c in self._children: | |
yield c | |
def __getitem__(self, key): | |
"""Get an attribute using the syntax node[key]""" | |
return self._attribs[key] | |
def __setitem__(self, key, value): | |
"""Set a new attribute using the syntax node[key] = value.""" | |
self._attribs[key] = value | |
def __call__(self): | |
"""Allows getting the value using the syntax 'node()'""" | |
return self._value | |
def write(self, filename): | |
"""Write out the XML tree to a file.""" | |
f = open(filename, 'w') | |
f.write('<?xml version="1.0"?>\n') | |
self._write(f, 0) | |
f.write('\n') | |
def _write(self, f, level = 0): | |
"""Internal method used to write the XML representation of | |
each node.""" | |
if self._name == "": return | |
indnt = indent[level] | |
# handle comments | |
if self._name == '_comment_': | |
f.write('\n'+indnt+'<!--') | |
if len(self._value) > 0: | |
if self._value[0] != ' ': | |
self._value = ' '+self._value | |
if self._value[-1] != ' ': | |
self._value = self._value+' ' | |
f.write(self._value+'-->') | |
return | |
# write the opening tag and attributes | |
f.write(indnt + '<' + self._name) | |
for a in self._attribs.keys(): | |
f.write(' '+a+'="'+self._attribs[a]+'"') | |
if (self._value == "" and self.nChildren() == 0): | |
f.write('/>') | |
else: | |
f.write('>') | |
if self._value != "": | |
vv = self._value.lstrip() | |
ieol = vv.find('\n') | |
if ieol >= 0: | |
while 1 > 0: | |
ieol = vv.find('\n') | |
if ieol >= 0: | |
f.write('\n '+indnt+vv[:ieol]) | |
vv = vv[ieol+1:].lstrip() | |
else: | |
f.write('\n '+indnt+vv) | |
break | |
else: | |
f.write(self._value) | |
for c in self._children: | |
f.write('\n') | |
c._write(f, level + 2) | |
if (self.nChildren() > 0): | |
f.write('\n'+indnt) | |
f.write('</'+self._name+'>') | |
#-------------------------------------------------- | |
# constants that can be used in .cti files | |
OneAtm = 1.01325e5 | |
OneBar = 1.0e5 | |
# Conversion from eV to J/kmol (electronCharge * Navrog) | |
eV = 9.64853364595687e7 | |
# Electron Mass in kg | |
ElectronMass = 9.10938291e-31 | |
import math, copy | |
# default units | |
_ulen = 'm' | |
_umol = 'kmol' | |
_umass = 'kg' | |
_utime = 's' | |
_ue = 'J/kmol' | |
_uenergy = 'J' | |
_upres = 'Pa' | |
# used to convert reaction pre-exponentials | |
_length = {'cm':0.01, 'm':1.0, 'mm':0.001} | |
_moles = {'kmol':1.0, 'mol':0.001, 'molec':1.0/6.02214129e26} | |
_time = {'s':1.0, 'min':60.0, 'hr':3600.0} | |
# default std state pressure | |
_pref = 1.0e5 # 1 bar | |
_name = 'noname' | |
# these lists store top-level entries | |
_elements = [] | |
_species = [] | |
_speciesnames = [] | |
_phases = [] | |
_reactions = [] | |
_atw = {} | |
_enames = {} | |
_valsp = '' | |
_valrxn = '' | |
_valexport = '' | |
_valfmt = '' | |
def export_species(filename, fmt = 'CSV'): | |
global _valexport | |
global _valfmt | |
_valexport = filename | |
_valfmt = fmt | |
def validate(species = 'yes', reactions = 'yes'): | |
global _valsp | |
global _valrxn | |
_valsp = species | |
_valrxn = reactions | |
def isnum(a): | |
"""True if a is an integer or floating-point number.""" | |
if isinstance(a, (int, float)): | |
return 1 | |
else: | |
return 0 | |
def is_local_species(name): | |
"""true if the species named 'name' is defined in this file""" | |
if name in _speciesnames: | |
return 1 | |
return 0 | |
def dataset(nm): | |
"Set the dataset name. Invoke this to change the name of the xml file." | |
global _name | |
_name = nm | |
def standard_pressure(p0): | |
"""Set the default standard-state pressure.""" | |
global _pref | |
_pref = p0 | |
def units(length = '', quantity = '', mass = '', time = '', | |
act_energy = '', energy = '', pressure = ''): | |
""" | |
Set the default units. | |
:param length: | |
The default units for length. Default: ``'m'`` | |
:param mass: | |
The default units for mass. Default: ``'kg'`` | |
:param quantity: | |
The default units to specify number of molecules. Default: ``'kmol'`` | |
:param time: | |
The default units for time. Default: ``'s'`` | |
:param energy: | |
The default units for energies. Default: ``'J'`` | |
:param act_energy: | |
The default units for activation energies. Default: ``'K'`` | |
:param pressure: | |
The default units for pressure. Default: ``'Pa'`` | |
""" | |
global _ulen, _umol, _ue, _utime, _umass, _uenergy, _upres | |
if length: _ulen = length | |
if quantity: _umol = quantity | |
if act_energy: _ue = act_energy | |
if time: _utime = time | |
if mass: _umass = mass | |
if energy: _uenergy = energy | |
if pressure: _upres = pressure | |
def ufmt(base, n): | |
"""return a string representing a unit to a power n.""" | |
if n == 0: return '' | |
if n == 1: return '-'+base | |
if n == -1: return '/'+base | |
if n > 0: return '-'+base+str(n) | |
if n < 0: return '/'+base+str(-n) | |
def write(outName=None): | |
"""write the CTML file.""" | |
x = XMLnode("ctml") | |
v = x.addChild("validate") | |
v["species"] = _valsp | |
v["reactions"] = _valrxn | |
if _elements: | |
ed = x.addChild("elementData") | |
for e in _elements: | |
e.build(ed) | |
for ph in _phases: | |
ph.build(x) | |
s = species_set(name = _name, species = _species) | |
s.build(x) | |
r = x.addChild('reactionData') | |
r['id'] = 'reaction_data' | |
for rx in _reactions: | |
rx.build(r) | |
if outName is not None: | |
x.write(outName) | |
elif _name != 'noname': | |
x.write(_name+'.xml') | |
else: | |
print(x) | |
if _valexport: | |
f = open(_valexport,'w') | |
for s in _species: | |
s.export(f, _valfmt) | |
f.close() | |
def addFloat(x, nm, val, fmt='', defunits=''): | |
""" | |
Add a child element to XML element x representing a | |
floating-point number. | |
""" | |
u = '' | |
s = '' | |
if isnum(val): | |
fval = float(val) | |
if fmt: | |
s = fmt % fval | |
else: | |
s = repr(fval) | |
xc = x.addChild(nm, s) | |
if defunits: | |
xc['units'] = defunits | |
else: | |
v = val[0] | |
u = val[1] | |
if fmt: | |
s = fmt % v | |
else: | |
s = repr(v) | |
xc = x.addChild(nm, s) | |
xc['units'] = u | |
def getAtomicComp(atoms): | |
if isinstance(atoms, dict): return atoms | |
a = atoms.replace(',',' ') | |
toks = a.split() | |
d = {} | |
for t in toks: | |
b = t.split(':') | |
d[b[0]] = int(b[1]) | |
return d | |
def getReactionSpecies(s): | |
"""Take a reaction string and return a | |
dictionary mapping species names to stoichiometric | |
coefficients. If any species appears more than once, | |
the returned stoichiometric coefficient is the sum. | |
>>> s = 'CH3 + 3 H + 5.2 O2 + 0.7 H' | |
>>> getReactionSpecies(s) | |
>>> {'CH3':1, 'H':3.7, 'O2':5.2} | |
""" | |
# get rid of the '+' signs separating species. Only plus signs | |
# surrounded by spaces are replaced, so that plus signs may be | |
# used in species names (e.g. 'Ar3+') | |
toks = s.replace(' + ',' ').split() | |
d = {} | |
n = 1.0 | |
for t in toks: | |
# try to convert the token to a number. | |
try: | |
n = float(t) | |
if n < 0.0: | |
raise CTI_Error("negative stoichiometric coefficient:" | |
+s) | |
#if t > '0' and t < '9': | |
# n = int(t) | |
#else: | |
# token isn't a number, so it must be a species name | |
except: | |
# already seen this token so increment its value by the last | |
# value of n | |
if t in d: | |
d[t] += n | |
else: | |
# first time this token has been seen, so set its value to n | |
d[t] = n | |
# reset n to 1.0 for species that do not specify a stoichiometric | |
# coefficient | |
n = 1 | |
return d | |
class element(object): | |
""" An atomic element or isotope. """ | |
def __init__(self, symbol = '', | |
atomic_mass = 0.01, | |
atomic_number = 0): | |
""" | |
:param symbol: | |
The symbol for the element or isotope. | |
:param atomic_mass: | |
The atomic mass in amu. | |
""" | |
self._sym = symbol | |
self._atw = atomic_mass | |
self._num = atomic_number | |
global _elements | |
_elements.append(self) | |
def build(self, db): | |
e = db.addChild("element") | |
e["name"] = self._sym | |
e["atomicWt"] = repr(self._atw) | |
e["atomicNumber"] = repr(self._num) | |
class species_set(object): | |
def __init__(self, name = '', species = []): | |
self._s = species | |
self._name = name | |
#self.type = SPECIES_SET | |
def build(self, p): | |
p.addComment(' species definitions ') | |
sd = p.addChild("speciesData") | |
sd["id"] = "species_data" | |
for s in self._s: | |
#if s.type == SPECIES: | |
s.build(sd) | |
#else: | |
# raise 'wrong object type in species_set: '+s.__class__ | |
class species(object): | |
"""A constituent of a phase or interface.""" | |
def __init__(self, | |
name = 'missing name!', | |
atoms = '', | |
note = '', | |
thermo = None, | |
transport = None, | |
charge = -999, | |
size = 1.0): | |
""" | |
:param name: | |
The species name (or formula). The name may be arbitrarily long, | |
although usually a relatively short, abbreviated name is most | |
convenient. Required parameter. | |
:param atoms: | |
The atomic composition, specified by a string containing | |
space-delimited <element>:<atoms> pairs. The number of atoms may be | |
either an integer or a floating-point number. | |
:param thermo: | |
The parameterization to use to compute the reference-state | |
thermodynamic properties. This must be one of the entry types | |
described in :ref:`sec-thermo-models`. To specify multiple | |
parameterizations, each for a different temperature range, | |
group them in parentheses. | |
:param transport: | |
An entry specifying parameters to compute this species' | |
contribution to the transport properties. This must be one of the | |
entry types described in :ref:`sec-species-transport-models`, and | |
must be consistent with the transport model of the phase into which | |
the species is imported. To specify parameters for multiple | |
transport models, group the entries in parentheses. | |
:param size: | |
The species "size". Currently used only for surface species, | |
where it represents the number of sites occupied. | |
:param charge: | |
The charge, in multiples of :math:`|e|`. If not specified, the | |
charge will be calculated from the number of "atoms" of element | |
``E``, which represents an electron. | |
""" | |
self._name = name | |
self._atoms = getAtomicComp(atoms) | |
self._comment = note | |
if thermo: | |
self._thermo = thermo | |
else: | |
self._thermo = const_cp() | |
self._transport = transport | |
chrg = 0 | |
self._charge = charge | |
if 'E' in self._atoms: | |
chrg = -self._atoms['E'] | |
if self._charge != -999: | |
if self._charge != chrg: | |
raise CTI_Error('specified charge inconsistent with number of electrons') | |
else: | |
self._charge = chrg | |
self._size = size | |
global _species | |
global _enames | |
_species.append(self) | |
global _speciesnames | |
if name in _speciesnames: | |
raise CTI_Error('species '+name+' multiply defined.') | |
_speciesnames.append(name) | |
for e in self._atoms.keys(): | |
_enames[e] = 1 | |
def export(self, f, fmt = 'CSV'): | |
global _enames | |
if fmt == 'CSV': | |
s = self._name+',' | |
for e in _enames: | |
if e in self._atoms: | |
s += repr(self._atoms[e])+',' | |
else: | |
s += '0,' | |
f.write(s) | |
if isinstance(self._thermo, thermo): | |
self._thermo.export(f, fmt) | |
else: | |
nt = len(self._thermo) | |
for n in range(nt): | |
self._thermo[n].export(f, fmt) | |
f.write('\n') | |
def build(self, p): | |
hdr = ' species '+self._name+' ' | |
p.addComment(hdr) | |
s = p.addChild("species") | |
s["name"] = self._name | |
a = '' | |
for e in self._atoms.keys(): | |
a += e+':'+str(self._atoms[e])+' ' | |
s.addChild("atomArray",a) | |
if self._comment: | |
s.addChild("note",self._comment) | |
if self._charge != -999: | |
s.addChild("charge",self._charge) | |
if self._size != 1.0: | |
s.addChild("size",self._size) | |
if self._thermo: | |
t = s.addChild("thermo") | |
if isinstance(self._thermo, thermo): | |
self._thermo.build(t) | |
else: | |
nt = len(self._thermo) | |
for n in range(nt): | |
self._thermo[n].build(t) | |
if self._transport: | |
t = s.addChild("transport") | |
if isinstance(self._transport, transport): | |
self._transport.build(t) | |
else: | |
nt = len(self._transport) | |
for n in range(nt): | |
self._transport[n].build(t) | |
class thermo(object): | |
"""Base class for species standard-state thermodynamic properties.""" | |
def _build(self, p): | |
return p.addChild("thermo") | |
def export(self, f, fmt = 'CSV'): | |
pass | |
class Mu0_table(thermo): | |
"""Properties are computed by specifying a table of standard | |
chemical potentials vs. T.""" | |
def __init__(self, Trange = (0.0, 0.0), | |
h298 = 0.0, | |
mu0 = None, | |
p0 = -1.0): | |
self._t = Trange | |
self._h298 = h298 | |
self._mu0 = mu0 | |
self._pref = p0 | |
def build(self, t): | |
n = t.addChild("Mu0") | |
n['Tmin'] = repr(self._t[0]) | |
n['Tmax'] = repr(self._t[1]) | |
if self._pref <= 0.0: | |
n['P0'] = repr(_pref) | |
else: | |
n['P0'] = repr(self._pref) | |
energy_units = _uenergy+'/'+_umol | |
addFloat(n,"H298", self._h298, defunits = energy_units) | |
n.addChild("numPoints", len(self._mu0)) | |
mustr = '' | |
tstr = '' | |
col = 0 | |
for v in self._mu0: | |
mu0 = v[1] | |
t = v[0] | |
tstr += '%17.9E, ' % t | |
mustr += '%17.9E, ' % mu0 | |
col += 1 | |
if col == 3: | |
tstr = tstr[:-2]+'\n' | |
mustr = mustr[:-2]+'\n' | |
col = 0 | |
u = n.addChild("floatArray", mustr) | |
u["size"] = "numPoints" | |
u["name"] = "Mu0Values" | |
u = n.addChild("floatArray", tstr) | |
u["size"] = "numPoints" | |
u["name"] = "Mu0Temperatures" | |
class NASA(thermo): | |
"""The 7-coefficient NASA polynomial parameterization.""" | |
def __init__(self, Trange = (0.0, 0.0), coeffs = [], p0 = -1.0): | |
r""" | |
:param Trange: | |
The temperature range over which the parameterization is valid. | |
This must be entered as a sequence of two temperature values. | |
Required. | |
:param coeffs: | |
Array of seven coefficients :math:`(a_0, \ldots , a_6)` | |
:param p0: | |
The reference-state pressure, usually 1 atm or 1 bar. If omitted, | |
the default value is used, which is set by the ``standard_pressure`` | |
directive. | |
""" | |
self._t = Trange | |
self._pref = p0 | |
if len(coeffs) != 7: | |
raise CTI_Error('NASA coefficient list must have length = 7') | |
self._coeffs = coeffs | |
def export(self, f, fmt='CSV'): | |
if fmt == 'CSV': | |
s = 'NASA,'+str(self._t[0])+','+str(self._t[1])+',' | |
for i in range(7): | |
s += '%17.9E, ' % self._coeffs[i] | |
f.write(s) | |
def build(self, t): | |
n = t.addChild("NASA") | |
n['Tmin'] = repr(self._t[0]) | |
#n['Tmid'] = repr(self._t[1]) | |
n['Tmax'] = repr(self._t[1]) | |
if self._pref <= 0.0: | |
n['P0'] = repr(_pref) | |
else: | |
n['P0'] = repr(self._pref) | |
s = '' | |
for i in range(4): | |
s += '%17.9E, ' % self._coeffs[i] | |
s += '\n' | |
s += '%17.9E, %17.9E, %17.9E' % (self._coeffs[4], | |
self._coeffs[5], self._coeffs[6]) | |
#if i > 0 and 3*((i+1)/3) == i: s += '\n' | |
#s = s[:-2] | |
u = n.addChild("floatArray", s) | |
u["size"] = "7" | |
u["name"] = "coeffs" | |
class NASA9(thermo): | |
"""NASA9 polynomial parameterization for a single temperature region.""" | |
def __init__(self, Trange = (0.0, 0.0), | |
coeffs = [], p0 = -1.0): | |
self._t = Trange # Range of the polynomial representation | |
self._pref = p0 # Reference pressure | |
if len(coeffs) != 9: | |
raise CTI_Error('NASA9 coefficient list must have length = 9') | |
self._coeffs = coeffs | |
def export(self, f, fmt='CSV'): | |
if fmt == 'CSV': | |
s = 'NASA9,'+str(self._t[0])+','+str(self._t[1])+',' | |
for i in range(9): | |
s += '%17.9E, ' % self._coeffs[i] | |
f.write(s) | |
def build(self, t): | |
n = t.addChild("NASA9") | |
n['Tmin'] = repr(self._t[0]) | |
n['Tmax'] = repr(self._t[1]) | |
if self._pref <= 0.0: | |
n['P0'] = repr(_pref) | |
else: | |
n['P0'] = repr(self._pref) | |
s = '' | |
for i in range(4): | |
s += '%17.9E, ' % self._coeffs[i] | |
s += '\n' | |
s += '%17.9E, %17.9E, %17.9E, %17.9E,' % (self._coeffs[4], self._coeffs[5], | |
self._coeffs[6], self._coeffs[7]) | |
s += '\n' | |
s += '%17.9E' % (self._coeffs[8]) | |
u = n.addChild("floatArray", s) | |
u["size"] = "9" | |
u["name"] = "coeffs" | |
class activityCoefficients(object): | |
pass | |
class pureFluidParameters(activityCoefficients): | |
""" | |
""" | |
def __init__(self, species = None, a_coeff = [], b_coeff = 0): | |
""" | |
""" | |
self._species = species | |
self._acoeff = a_coeff | |
self._bcoeff = b_coeff | |
def build(self,a): | |
f= a.addChild("pureFluidParameters") | |
f['species'] = self._species | |
s = '%10.4E, %10.4E \n' % (self._acoeff[0], self._acoeff[1]) | |
ac = f.addChild("a_coeff",s) | |
ac["units"] = _upres+'-'+_ulen+'6/'+_umol+'2' | |
ac["model"] = "linear_a" | |
s = '%0.2f \n' % self._bcoeff | |
bc = f.addChild("b_coeff",s) | |
bc["units"] = _ulen+'3/'+_umol | |
class crossFluidParameters(activityCoefficients): | |
def __init__(self, species = None, a_coeff = [], b_coeff = []): | |
self._species1, self._species2 = species.split(' ') | |
self._acoeff = a_coeff | |
self._bcoeff = b_coeff | |
def build(self,a): | |
f= a.addChild("crossFluidParameters") | |
f["species2"] = self._species2 | |
f["species1"] = self._species1 | |
s = '%10.4E, %10.4E \n' % (self._acoeff[0], self._acoeff[1]) | |
ac = f.addChild("a_coeff",s) | |
ac["units"] = _upres+'-'+_ulen+'6/'+_umol+'2' | |
ac["model"] = "linear_a" | |
if self._bcoeff: | |
s = '%0.2f \n' % self._bcoeff | |
bc = f.addChild("b_coeff",s) | |
bc["units"] = _ulen+'3/'+_umol | |
class Shomate(thermo): | |
"""Shomate polynomial parameterization.""" | |
def __init__(self, Trange = (0.0, 0.0), coeffs = [], p0 = -1.0): | |
r""" | |
:param Trange: | |
The temperature range over which the parameterization is valid. | |
This must be entered as a sequence of two temperature values. | |
Required input. | |
:param coeffs: | |
Sequence of seven coefficients :math:`(A, \ldots ,G)` | |
:param p0: | |
The reference-state pressure, usually 1 atm or 1 bar. If omitted, | |
the default value set by the ``standard_pressure`` directive is used. | |
""" | |
self._t = Trange | |
self._pref = p0 | |
if len(coeffs) != 7: | |
raise CTI_Error('Shomate coefficient list must have length = 7') | |
self._coeffs = coeffs | |
def build(self, t): | |
n = t.addChild("Shomate") | |
n['Tmin'] = repr(self._t[0]) | |
n['Tmax'] = repr(self._t[1]) | |
if self._pref <= 0.0: | |
n['P0'] = repr(_pref) | |
else: | |
n['P0'] = repr(self._pref) | |
s = '' | |
for i in range(4): | |
s += '%17.9E, ' % self._coeffs[i] | |
s += '\n' | |
s += '%17.9E, %17.9E, %17.9E' % (self._coeffs[4], | |
self._coeffs[5], self._coeffs[6]) | |
u = n.addChild("floatArray", s) | |
u["size"] = "7" | |
u["name"] = "coeffs" | |
class Adsorbate(thermo): | |
"""Adsorbed species characterized by a binding energy and a set of | |
vibrational frequencies.""" | |
def __init__(self, Trange = (0.0, 0.0), | |
binding_energy = 0.0, | |
frequencies = [], p0 = -1.0): | |
self._t = Trange | |
self._pref = p0 | |
self._freqs = frequencies | |
self._be = binding_energy | |
def build(self, t): | |
n = t.addChild("adsorbate") | |
n['Tmin'] = repr(self._t[0]) | |
n['Tmax'] = repr(self._t[1]) | |
if self._pref <= 0.0: | |
n['P0'] = repr(_pref) | |
else: | |
n['P0'] = repr(self._pref) | |
energy_units = _uenergy+'/'+_umol | |
addFloat(n,'binding_energy',self._be, defunits = energy_units) | |
s = "" | |
nfreq = len(self._freqs) | |
for i in range(nfreq): | |
s += '%17.9E, ' % self._freqs[i] | |
s += '\n' | |
u = n.addChild("floatArray", s) | |
u["size"] = repr(nfreq) | |
u["name"] = "freqs" | |
class const_cp(thermo): | |
"""Constant specific heat.""" | |
def __init__(self, | |
t0 = 298.15, cp0 = 0.0, h0 = 0.0, s0 = 0.0, | |
tmax = 5000.0, tmin = 100.0): | |
""" | |
:param t0: | |
Temperature parameter T0. Default: 298.15 K. | |
:param cp0: | |
Reference-state molar heat capacity (constant). Default: 0.0. | |
:param h0: | |
Reference-state molar enthalpy at temperature T0. Default: 0.0. | |
:param s0: | |
Reference-state molar entropy at temperature T0. Default: 0.0. | |
""" | |
self._t = [tmin, tmax] | |
self._c = [t0, h0, s0, cp0] | |
def build(self, t): | |
#t = self._build(p) | |
c = t.addChild('const_cp') | |
if self._t[0] >= 0.0: c['Tmin'] = repr(self._t[0]) | |
if self._t[1] >= 0.0: c['Tmax'] = repr(self._t[1]) | |
energy_units = _uenergy+'/'+_umol | |
addFloat(c,'t0',self._c[0], defunits = 'K') | |
addFloat(c,'h0',self._c[1], defunits = energy_units) | |
addFloat(c,'s0',self._c[2], defunits = energy_units+'/K') | |
addFloat(c,'cp0',self._c[3], defunits = energy_units+'/K') | |
class transport(object): | |
pass | |
class gas_transport(transport): | |
""" | |
Species-specific Transport coefficients for ideal gas transport models. | |
""" | |
def __init__(self, geom = 'nonlin', | |
diam = 0.0, well_depth = 0.0, dipole = 0.0, | |
polar = 0.0, rot_relax = 0.0): | |
""" | |
:param geom: | |
A string specifying the molecular geometry. One of ``atom``, | |
``linear``, or ``nonlin``. Required. | |
:param diam: | |
The Lennard-Jones collision diameter in Angstroms. Required. | |
:param well_depth: | |
The Lennard-Jones well depth in Kelvin. Required. | |
:param dipole: | |
The permanent dipole moment in Debye. Default: 0.0 | |
:param polar: | |
The polarizability in A^3. Default: 0.0 | |
:param rot_relax: | |
The rotational relaxation collision number at 298 K. Dimensionless. | |
Default: 0.0 | |
""" | |
self._geom = geom | |
self._diam = diam | |
self._well_depth = well_depth | |
self._dipole = dipole | |
self._polar = polar | |
self._rot_relax = rot_relax | |
def build(self, t): | |
#t = s.addChild("transport") | |
t['model'] = 'gas_transport' | |
# t.addChild("geometry", self._geom) | |
tg = t.addChild('string',self._geom) | |
tg['title'] = 'geometry' | |
addFloat(t, "LJ_welldepth", (self._well_depth, 'K'), '%8.3f') | |
addFloat(t, "LJ_diameter", (self._diam, 'A'),'%8.3f') | |
addFloat(t, "dipoleMoment", (self._dipole, 'Debye'),'%8.3f') | |
addFloat(t, "polarizability", (self._polar, 'A3'),'%8.3f') | |
addFloat(t, "rotRelax", self._rot_relax,'%8.3f') | |
class rate_expression(object): | |
pass | |
class Arrhenius(rate_expression): | |
def __init__(self, | |
A = 0.0, | |
n = 0.0, | |
E = 0.0, | |
coverage = [], | |
rate_type = ''): | |
""" | |
:param A: | |
The pre-exponential coefficient. Required input. If entered without | |
units, the units will be computed considering all factors that | |
affect the units. The resulting units string is written to the CTML | |
file individually for each reaction pre-exponential coefficient. | |
:param n: | |
The temperature exponent. Dimensionless. Default: 0.0. | |
:param E: | |
Activation energy. Default: 0.0. | |
""" | |
self._c = [A, n, E] | |
self._type = rate_type | |
if coverage: | |
if isinstance(coverage[0], str): | |
self._cov = [coverage] | |
else: | |
self._cov = coverage | |
else: | |
self._cov = None | |
def build(self, p, units_factor = 1.0, | |
gas_species = [], name = '', rxn_phase = None): | |
a = p.addChild('Arrhenius') | |
if name: a['name'] = name | |
# check for sticking probability | |
if self._type: | |
a['type'] = self._type | |
if self._type == 'stick': | |
ngas = len(gas_species) | |
if ngas != 1: | |
raise CTI_Error(""" | |
Sticking probabilities can only be used for reactions with one gas-phase | |
reactant, but this reaction has """+str(ngas)+': '+str(gas_species)) | |
else: | |
a['species'] = gas_species[0] | |
units_factor = 1.0 | |
# if a pure number is entered for A, multiply by the conversion | |
# factor to SI and write it to CTML as a pure number. Otherwise, | |
# pass it as-is through to CTML with the unit string. | |
if isnum(self._c[0]): | |
addFloat(a,'A',self._c[0]*units_factor, fmt = '%14.6E') | |
elif len(self._c[0]) == 2 and self._c[0][1] == '/site': | |
addFloat(a,'A',self._c[0][0]/rxn_phase._sitedens, | |
fmt = '%14.6E') | |
else: | |
addFloat(a,'A',self._c[0], fmt = '%14.6E') | |
# The b coefficient should be dimensionless, so there is no | |
# need to use 'addFloat' | |
a.addChild('b', repr(self._c[1])) | |
# If a pure number is entered for the activation energy, | |
# add the default units, otherwise use the supplied units. | |
addFloat(a,'E', self._c[2], fmt = '%f', defunits = _ue) | |
# for surface reactions, a coverage dependence may be specified. | |
if self._cov: | |
for cov in self._cov: | |
c = a.addChild('coverage') | |
c['species'] = cov[0] | |
addFloat(c, 'a', cov[1], fmt = '%f') | |
c.addChild('m', repr(cov[2])) | |
addFloat(c, 'e', cov[3], fmt = '%f', defunits = _ue) | |
def stick(A = 0.0, n = 0.0, E = 0.0, coverage = []): | |
return Arrhenius(A = A, n = n, E = E, coverage = coverage, rate_type = 'stick') | |
def getPairs(s): | |
toks = s.split() | |
m = {} | |
for t in toks: | |
key, val = t.split(':') | |
m[key] = float(val) | |
return m | |
class reaction(object): | |
""" | |
A homogeneous chemical reaction with pressure-independent rate coefficient | |
and mass-action kinetics. | |
""" | |
def __init__(self, | |
equation = '', | |
kf = None, | |
id = '', | |
order = '', | |
options = []): | |
""" | |
:param equation: | |
A string specifying the chemical equation. | |
:param rate_coeff: | |
The rate coefficient for the forward direction. If a sequence of | |
three numbers is given, these will be interpreted as [A, n,E] in | |
the modified Arrhenius function :math:`A T^n exp(-E/\hat{R}T)`. | |
:param id: | |
An optional identification string. If omitted, it defaults to a | |
four-digit numeric string beginning with 0001 for the first | |
reaction in the file. | |
:param options: | |
Processing options, as described in :ref:`sec-phase-options`. | |
""" | |
self._id = id | |
self._e = equation | |
self._order = order | |
if isinstance(options, str): | |
self._options = [options] | |
else: | |
self._options = options | |
global _reactions | |
self._num = len(_reactions)+1 | |
r = '' | |
p = '' | |
for e in ['<=>', '=>', '=']: | |
if self._e.find(e) >= 0: | |
r, p = self._e.split(e) | |
if e in ['<=>','=']: self.rev = 1 | |
else: self.rev = 0 | |
break | |
self._r = getReactionSpecies(r) | |
self._p = getReactionSpecies(p) | |
self._rxnorder = copy.copy(self._r) | |
if self._order: | |
order = getPairs(self._order) | |
for o in order.keys(): | |
if o in self._rxnorder: | |
self._rxnorder[o] = order[o] | |
else: | |
raise CTI_Error("order specified for non-reactant: "+o) | |
self._kf = kf | |
self._igspecies = [] | |
self._dims = [0]*4 | |
self._rxnphase = None | |
self._type = '' | |
_reactions.append(self) | |
def unit_factor(self): | |
""" | |
Conversion factor from given rate constant units to the MKS (+kmol) | |
used internally by Cantera, taking into account the reaction order. | |
""" | |
return (math.pow(_length[_ulen], -self.ldim) * | |
math.pow(_moles[_umol], -self.mdim) / _time[_utime]) | |
def build(self, p): | |
if self._id: | |
id = self._id | |
else: | |
if self._num < 10: | |
nstr = '000'+str(self._num) | |
elif self._num < 100: | |
nstr = '00'+str(self._num) | |
elif self._num < 1000: | |
nstr = '0'+str(self._num) | |
else: | |
nstr = str(self._num) | |
id = nstr | |
self.mdim = 0 | |
self.ldim = 0 | |
rstr = '' | |
rxnph = [] | |
for s in self._r.keys(): | |
ns = self._rxnorder[s] | |
nm = -999 | |
nl = -999 | |
rstr += s+':'+str(self._r[s])+' ' | |
mindim = 4 | |
for ph in _phases: | |
if ph.has_species(s): | |
nm, nl = ph.conc_dim() | |
if ph.is_ideal_gas(): | |
self._igspecies.append(s) | |
if not ph in rxnph: | |
rxnph.append(ph) | |
self._dims[ph._dim] += 1 | |
if ph._dim < mindim: | |
self._rxnphase = ph | |
mindim = ph._dim | |
break | |
if nm == -999: | |
raise CTI_Error("species "+s+" not found") | |
self.mdim += nm*ns | |
self.ldim += nl*ns | |
p.addComment(" reaction "+id+" ") | |
r = p.addChild('reaction') | |
r['id'] = id | |
if self.rev: | |
r['reversible'] = 'yes' | |
else: | |
r['reversible'] = 'no' | |
noptions = len(self._options) | |
for nss in range(noptions): | |
s = self._options[nss] | |
if s == 'duplicate': | |
r['duplicate'] = 'yes' | |
elif s == 'negative_A': | |
r['negative_A'] = 'yes' | |
ee = self._e.replace('<','[') | |
ee = ee.replace('>',']') | |
r.addChild('equation',ee) | |
if self._order: | |
for osp in self._rxnorder.keys(): | |
o = r.addChild('order',self._rxnorder[osp]) | |
o['species'] = osp | |
# adjust the moles and length powers based on the dimensions of | |
# the rate of progress (moles/length^2 or moles/length^3) | |
if self._type == 'surface': | |
self.mdim += -1 | |
self.ldim += 2 | |
p = self._dims[:3] | |
if p[0] != 0 or p[1] != 0 or p[2] > 1: | |
raise CTI_Error(self._e +'\nA surface reaction may contain at most '+ | |
'one surface phase.') | |
elif self._type == 'edge': | |
self.mdim += -1 | |
self.ldim += 1 | |
p = self._dims[:2] | |
if p[0] != 0 or p[1] > 1: | |
raise CTI_Error(self._e+'\nAn edge reaction may contain at most '+ | |
'one edge phase.') | |
else: | |
self.mdim += -1 | |
self.ldim += 3 | |
# add the reaction type as an attribute if it has been specified. | |
if self._type: | |
r['type'] = self._type | |
# The default rate coefficient type is Arrhenius. If the rate | |
# coefficient has been specified as a sequence of three | |
# numbers, then create a new Arrhenius instance for it; | |
# otherwise, just use the supplied instance. | |
nm = '' | |
kfnode = r.addChild('rateCoeff') | |
if self._type == '': | |
self._kf = [self._kf] | |
elif self._type == 'surface': | |
self._kf = [self._kf] | |
elif self._type == 'edge': | |
self._kf = [self._kf] | |
elif self._type == 'threeBody': | |
self._kf = [self._kf] | |
self.mdim += 1 | |
self.ldim -= 3 | |
elif self._type == 'chebyshev': | |
self._kf = [] | |
if self._type == 'edge': | |
if self._beta > 0: | |
electro = kfnode.addChild('electrochem') | |
electro['beta'] = repr(self._beta) | |
for kf in self._kf: | |
if isinstance(kf, rate_expression): | |
k = kf | |
else: | |
k = Arrhenius(A = kf[0], n = kf[1], E = kf[2]) | |
k.build(kfnode, self.unit_factor(), gas_species = self._igspecies, | |
name = nm, rxn_phase = self._rxnphase) | |
if self._type == 'falloff': | |
# set values for low-pressure rate coeff if falloff rxn | |
self.mdim += 1 | |
self.ldim -= 3 | |
nm = 'k0' | |
rstr = rstr[:-1] | |
r.addChild('reactants',rstr) | |
pstr = '' | |
for s in self._p.keys(): | |
ns = self._p[s] | |
pstr += s+':'+repr(ns)+' ' | |
pstr = pstr[:-1] | |
r.addChild('products',pstr) | |
return r | |
#------------------- | |
class three_body_reaction(reaction): | |
""" | |
A three-body reaction. | |
""" | |
def __init__(self, | |
equation = '', | |
kf = None, | |
efficiencies = '', | |
id = '', | |
options = [] | |
): | |
""" | |
:param equation: | |
A string specifying the chemical equation. The reaction can be | |
written in either the association or dissociation directions, and | |
may be reversible or irreversible. | |
:param rate_coeff: | |
The rate coefficient for the forward direction. If a sequence of | |
three numbers is given, these will be interpreted as [A,n,E] in | |
the modified Arrhenius function. | |
:param efficiencies: | |
A string specifying the third-body collision efficiencies. | |
The efficiencies for unspecified species are set to 1.0. | |
:param id: | |
An optional identification string. If omitted, it defaults to a | |
four-digit numeric string beginning with 0001 for the first | |
reaction in the file. | |
:param options: | |
Processing options, as described in :ref:`sec-phase-options`. | |
""" | |
reaction.__init__(self, equation, kf, id, '', options) | |
self._type = 'threeBody' | |
self._effm = 1.0 | |
self._eff = efficiencies | |
# clean up reactant and product lists | |
for r in list(self._r.keys()): | |
if r == 'M' or r == 'm': | |
del self._r[r] | |
for p in list(self._p.keys()): | |
if p == 'M' or p == 'm': | |
del self._p[p] | |
def build(self, p): | |
r = reaction.build(self, p) | |
if r == 0: return | |
kfnode = r.child('rateCoeff') | |
if self._eff: | |
eff = kfnode.addChild('efficiencies',self._eff) | |
eff['default'] = repr(self._effm) | |
#--------------- | |
class falloff_reaction(reaction): | |
""" A gas-phase falloff reaction. """ | |
def __init__(self, equation, kf0, kf, | |
efficiencies='', falloff=None, id='', options=[]): | |
""" | |
:param equation: | |
A string specifying the chemical equation. | |
:param rate_coeff_inf: | |
The rate coefficient for the forward direction in the high-pressure | |
limit. If a sequence of three numbers is given, these will be | |
interpreted as [A, n,E] in the modified Arrhenius function. | |
:param rate_coeff_0: | |
The rate coefficient for the forward direction in the low-pressure | |
limit. If a sequence of three numbers is given, these will be | |
interpreted as [A, n,E] in the modified Arrhenius function. | |
:param efficiencies: | |
A string specifying the third-body collision efficiencies. The | |
efficiency for unspecified species is set to 1.0. | |
:param falloff: | |
An embedded entry specifying a falloff function. If omitted, a | |
unity falloff function (Lindemann form) will be used. | |
:param id: | |
An optional identification string. If omitted, it defaults to a | |
four-digit numeric string beginning with 0001 for the first | |
reaction in the file. | |
:param options: | |
Processing options, as described in :ref:`sec-phase-options`. | |
""" | |
kf2 = (kf, kf0) | |
reaction.__init__(self, equation, kf2, id, '', options) | |
self._type = 'falloff' | |
# use a Lindemann falloff function by default | |
self._falloff = falloff | |
if self._falloff == None: | |
self._falloff = Lindemann() | |
self._effm = 1.0 | |
self._eff = efficiencies | |
# clean up reactant and product lists | |
del self._r['(+'] | |
del self._p['(+'] | |
if 'M)' in self._r: | |
del self._r['M)'] | |
del self._p['M)'] | |
elif 'm)' in self._r: | |
del self._r['m)'] | |
del self._p['m)'] | |
else: | |
for r in list(self._r.keys()): | |
if r[-1] == ')' and r.find('(') < 0: | |
species = r[:-1] | |
if self._eff: | |
raise CTI_Error('(+ '+species+') and '+self._eff+' cannot both be specified') | |
self._eff = species+':1.0' | |
self._effm = 0.0 | |
del self._r[r] | |
del self._p[r] | |
def build(self, p): | |
r = reaction.build(self, p) | |
if r == 0: return | |
kfnode = r.child('rateCoeff') | |
if self._eff and self._effm >= 0.0: | |
eff = kfnode.addChild('efficiencies',self._eff) | |
eff['default'] = repr(self._effm) | |
if self._falloff: | |
self._falloff.build(kfnode) | |
class pdep_arrhenius(reaction): | |
""" | |
Pressure-dependent rate calculated by interpolating between Arrhenius | |
expressions at different pressures. | |
:param equation: | |
A string specifying the chemical equation. | |
:param args: | |
Each additiona argument is a sequence of four elements specifying the | |
pressure and the Arrhenius parameters at that pressure. | |
""" | |
def __init__(self, equation='', *args, **kwargs): | |
self.pressures = [] | |
self.arrhenius = [] | |
for p, A, n, Ea in args: | |
self.pressures.append(p) | |
self.arrhenius.append((A, n, Ea)) | |
reaction.__init__(self, equation, self.arrhenius, **kwargs) | |
self._type = 'plog' | |
def build(self, p): | |
r = reaction.build(self, p) | |
kfnode = r.child('rateCoeff') | |
for i,c in enumerate(kfnode.children()): | |
assert c.name() == 'Arrhenius' | |
addFloat(c, 'P', self.pressures[i]) | |
class chebyshev_reaction(reaction): | |
""" | |
Pressure-dependent rate calculated in terms of a bivariate Chebyshev | |
polynomial. | |
:param equation: | |
A string specifying the chemical equation. | |
:param Tmin: | |
The minimum temperature at which the rate expression is defined | |
:param Tmax: | |
the maximum temperature at which the rate expression is defined | |
:param Pmin: | |
The minimum pressure at which the rate expression is defined | |
:param Pmax: | |
The maximum pressure at which the rate expression is defined | |
:param coeffs: | |
A 2D array of the coefficients defining the rate expression. For a | |
polynomial with M points in temperature and N points in pressure, this | |
should be a list of M lists each with N elements. | |
""" | |
def __init__(self, equation='', Tmin=300.0, Tmax=2500.0, | |
Pmin=(0.001, 'atm'), Pmax=(100.0, 'atm'), | |
coeffs=[[]], **kwargs): | |
reaction.__init__(self, equation, **kwargs) | |
self._type = 'chebyshev' | |
self.Pmin = Pmin | |
self.Pmax = Pmax | |
self.Tmin = Tmin | |
self.Tmax = Tmax | |
self.coeffs = coeffs | |
# clean up reactant and product lists | |
del self._r['(+'] | |
del self._p['(+'] | |
if 'M)' in self._r: | |
del self._r['M)'] | |
del self._p['M)'] | |
if 'm)' in self._r: | |
del self._r['m)'] | |
del self._p['m)'] | |
def build(self, p): | |
r = reaction.build(self, p) | |
kfnode = r.child('rateCoeff') | |
addFloat(kfnode, 'Tmin', self.Tmin) | |
addFloat(kfnode, 'Tmax', self.Tmax) | |
addFloat(kfnode, 'Pmin', self.Pmin) | |
addFloat(kfnode, 'Pmax', self.Pmax) | |
self.coeffs[0][0] += math.log10(self.unit_factor()); | |
lines = [] | |
for line in self.coeffs: | |
lines.append(', '.join('{0:12.5e}'.format(val) | |
for val in line)) | |
coeffNode = kfnode.addChild('floatArray', ',\n'.join(lines)) | |
coeffNode['name'] = 'coeffs' | |
coeffNode['degreeT'] = str(len(self.coeffs)) | |
coeffNode['degreeP'] = str(len(self.coeffs[0])) | |
class surface_reaction(reaction): | |
""" | |
A heterogeneous chemical reaction with pressure-independent rate | |
coefficient and mass-action kinetics. | |
""" | |
def __init__(self, equation='', kf=None, id='', order='', options=[]): | |
""" | |
:param equation: | |
A string specifying the chemical equation. | |
:param rate_coeff: | |
The rate coefficient for the forward direction. If a sequence of | |
three numbers is given, these will be interpreted as [A, n,E] in | |
the modified Arrhenius function. | |
:param sticking_prob: | |
The reactive sticking probability for the forward direction. This | |
can only be specified if there is only one bulk-phase reactant and | |
it belongs to an ideal gas phase. If a sequence of three numbers is | |
given, these will be interpreted as [A, n,E] in the modified | |
Arrhenius function. | |
:param id: | |
An optional identification string. If omitted, it defaults to a | |
four-digit numeric string beginning with 0001 for the first | |
reaction in the file. | |
:param options: | |
Processing options, as described in :ref:`sec-phase-options`. | |
""" | |
reaction.__init__(self, equation, kf, id, order, options) | |
self._type = 'surface' | |
class edge_reaction(reaction): | |
def __init__(self, | |
equation = '', | |
kf = None, | |
id = '', | |
order = '', | |
beta = 0.0, | |
options = []): | |
reaction.__init__(self, equation, kf, id, order, options) | |
self._type = 'edge' | |
self._beta = beta | |
#-------------- | |
class state(object): | |
""" | |
An embedded entry that specifies the thermodynamic state of a phase | |
or interface. | |
""" | |
def __init__(self, | |
temperature = None, | |
pressure = None, | |
mole_fractions = None, | |
mass_fractions = None, | |
density = None, | |
coverages = None, | |
solute_molalities = None): | |
""" | |
:param temperature: | |
The temperature. | |
:param pressure: | |
The pressure. | |
:param density: | |
The density. Cannot be specified if the phase is incompressible. | |
:param mole_fractions: | |
A string specifying the species mole fractions. Unspecified species | |
are set to zero. | |
:param mass_fractions: | |
A string specifying the species mass fractions. Unspecified species | |
are set to zero. | |
:param coverages: | |
A string specifying the species coverages. Unspecified species are | |
set to zero. Can only be specified for interfaces. | |
""" | |
self._t = temperature | |
self._p = pressure | |
self._rho = density | |
self._x = mole_fractions | |
self._y = mass_fractions | |
self._c = coverages | |
self._m = solute_molalities | |
def build(self, ph): | |
st = ph.addChild('state') | |
if self._t: addFloat(st, 'temperature', self._t, defunits = 'K') | |
if self._p: addFloat(st, 'pressure', self._p, defunits = _upres) | |
if self._rho: addFloat(st, 'density', self._rho, defunits = _umass+'/'+_ulen+'3') | |
if self._x: st.addChild('moleFractions', self._x) | |
if self._y: st.addChild('massFractions', self._y) | |
if self._c: st.addChild('coverages', self._c) | |
if self._m: st.addChild('soluteMolalities', self._m) | |
class phase(object): | |
"""Base class for phases of matter.""" | |
def __init__(self, | |
name = '', | |
dim = 3, | |
elements = '', | |
species = '', | |
reactions = 'none', | |
initial_state = None, | |
options = []): | |
""" | |
:param name: | |
A string to identify the phase. Must be unique among the phase | |
names within the file. | |
:param elements: | |
The elements. A string of element symbols. | |
:param species: | |
The species. A string or sequence of strings in the format | |
described in :ref:`sec-defining-species`. | |
:param reactions: | |
The homogeneous reactions. If omitted, no reactions will be | |
included. A string or sequence of strings in the format described | |
in :ref:`sec-declaring-reactions`. This field is not allowed for | |
stoichiometric_solid and stoichiometric_liquid entries. | |
:param kinetics: | |
The kinetics model. Optional; if omitted, the default model for the | |
phase type will be used. | |
:param transport: | |
The transport property model. Optional. If omitted, transport | |
property calculation will be disabled. | |
:param initial_state: | |
Initial thermodynamic state, specified with an embedded state entry. | |
:param options: | |
Special processing options. Optional. | |
""" | |
self._name = name | |
self._dim = dim | |
self._el = elements | |
self._sp = [] | |
self._rx = [] | |
if isinstance(options, str): | |
self._options = [options] | |
else: | |
self._options = options | |
self.debug = 0 | |
if 'debug' in options: | |
self.debug = 1 | |
#-------------------------------- | |
# process species | |
#-------------------------------- | |
# if a single string is entered, make it a list | |
if isinstance(species, str): | |
self._species = [species] | |
else: | |
self._species = species | |
self._skip = 0 | |
# dictionary of species names | |
self._spmap = {} | |
# for each species string, check whether or not the species | |
# are imported or defined locally. If imported, the string | |
# contains a colon (:) | |
for sp in self._species: | |
icolon = sp.find(':') | |
if icolon > 0: | |
#datasrc, spnames = sp.split(':') | |
datasrc = sp[:icolon].strip() | |
spnames = sp[icolon+1:] | |
self._sp.append((datasrc+'.xml', spnames)) | |
else: | |
spnames = sp | |
self._sp.append(('', spnames)) | |
# strip the commas, and make the list of species names | |
# 10/31/03: commented out the next line, so that species names may contain commas | |
#sptoks = spnames.replace(',',' ').split() | |
sptoks = spnames.split() | |
for s in sptoks: | |
# check for stray commas | |
if s != ',': | |
if s[0] == ',': s = s[1:] | |
if s[-1] == ',': s = s[:-1] | |
if s != 'all' and s in self._spmap: | |
raise CTI_Error('Multiply-declared species '+s+' in phase '+self._name) | |
self._spmap[s] = self._dim | |
self._rxns = reactions | |
# check that species have been declared | |
if len(self._spmap) == 0: | |
raise CTI_Error('No species declared for phase '+self._name) | |
# and that only one species is declared if it is a pure phase | |
if self.is_pure() and len(self._spmap) > 1: | |
raise CTI_Error('Stoichiometric phases must declare exactly one species, \n'+ | |
'but phase '+self._name+' declares '+str(len(self._spmap))+'.') | |
self._initial = initial_state | |
# add this phase to the global phase list | |
global _phases | |
_phases.append(self) | |
def is_ideal_gas(self): | |
"""True if the entry represents an ideal gas.""" | |
return 0 | |
def is_pure(self): | |
return 0 | |
def has_species(self, s): | |
"""Return 1 is a species with name 's' belongs to the phase, | |
or 0 otherwise.""" | |
if s in self._spmap: return 1 | |
return 0 | |
def conc_dim(self): | |
"""Concentration dimensions. Used in computing the units for reaction | |
rate coefficients.""" | |
return (1, -self._dim) | |
def buildrxns(self, p): | |
if isinstance(self._rxns, str): | |
self._rxns = [self._rxns] | |
# for each reaction string, check whether or not the reactions | |
# are imported or defined locally. If imported, the string | |
# contains a colon (:) | |
for r in self._rxns: | |
icolon = r.find(':') | |
if icolon > 0: | |
#datasrc, rnum = r.split(':') | |
datasrc = r[:icolon].strip() | |
rnum = r[icolon+1:] | |
self._rx.append((datasrc+'.xml', rnum)) | |
else: | |
rnum = r | |
self._rx.append(('', rnum)) | |
for r in self._rx: | |
datasrc = r[0] | |
ra = p.addChild('reactionArray') | |
ra['datasrc'] = datasrc+'#reaction_data' | |
rk = None | |
if 'skip_undeclared_species' in self._options: | |
rk = ra.addChild('skip') | |
rk['species'] = 'undeclared' | |
if 'skip_undeclared_third_bodies' in self._options: | |
if not rk: | |
rk = ra.addChild('skip') | |
rk['third_bodies'] = 'undeclared' | |
rtoks = r[1].split() | |
if rtoks[0] != 'all': | |
i = ra.addChild('include') | |
#i['prefix'] = 'reaction_' | |
i['min'] = rtoks[0] | |
if len(rtoks) > 2 and (rtoks[1] == 'to' or rtoks[1] == '-'): | |
i['max'] = rtoks[2] | |
else: | |
i['max'] = rtoks[0] | |
def build(self, p): | |
p.addComment(' phase '+self._name+' ') | |
ph = p.addChild('phase') | |
ph['id'] = self._name | |
ph['dim'] = repr(self._dim) | |
# ------- error tests ------- | |
#err = ph.addChild('validation') | |
#err.addChild('duplicateReactions','halt') | |
#err.addChild('thermo','warn') | |
e = ph.addChild('elementArray',self._el) | |
e['datasrc'] = 'elements.xml' | |
for s in self._sp: | |
datasrc, names = s | |
sa = ph.addChild('speciesArray',names) | |
sa['datasrc'] = datasrc+'#species_data' | |
if 'skip_undeclared_elements' in self._options: | |
sk = sa.addChild('skip') | |
sk['element'] = 'undeclared' | |
if self._rxns != 'none': | |
self.buildrxns(ph) | |
#self._eos.build(ph) | |
if self._initial: | |
self._initial.build(ph) | |
return ph | |
class ideal_gas(phase): | |
"""An ideal gas mixture.""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
reactions = 'none', | |
kinetics = 'GasKinetics', | |
transport = 'None', | |
initial_state = None, | |
options = []): | |
""" | |
The parameters correspond to those of :class:`.phase`, with the | |
following modifications: | |
:param kinetics: | |
The kinetics model. Usually this field is omitted, in which case | |
kinetics model GasKinetics, appropriate for reactions in ideal gas | |
mixtures, is used. | |
:param transport: | |
The transport property model. One of the strings ``'none'``, | |
``'multi'``, or ``'mix'``. Default: ``'none'``. | |
""" | |
phase.__init__(self, name, 3, elements, species, reactions, | |
initial_state, options) | |
self._pure = 0 | |
self._kin = kinetics | |
self._tr = transport | |
if self.debug: | |
print('Read ideal_gas entry '+self._name) | |
try: | |
print('in file '+__name__) | |
except: | |
pass | |
def build(self, p): | |
ph = phase.build(self, p) | |
e = ph.addChild("thermo") | |
e['model'] = 'IdealGas' | |
k = ph.addChild("kinetics") | |
k['model'] = self._kin | |
t = ph.addChild('transport') | |
t['model'] = self._tr | |
def is_ideal_gas(self): | |
return 1 | |
class stoichiometric_solid(phase): | |
""" | |
A solid compound or pure element. Stoichiometric solid phases contain | |
exactly one species, which always has unit activity. The solid is assumed | |
to have constant density. Therefore the rates of reactions involving these | |
phases do not contain any concentration terms for the (one) species in the | |
phase, since the concentration is always the same.""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
density = None, | |
transport = 'None', | |
initial_state = None, | |
options = []): | |
""" | |
See :class:`.phase` for descriptions of the parameters. | |
""" | |
phase.__init__(self, name, 3, elements, species, 'none', | |
initial_state, options) | |
self._dens = density | |
self._pure = 1 | |
if self._dens is None: | |
raise CTI_Error('density must be specified.') | |
self._tr = transport | |
def conc_dim(self): | |
"""A stoichiometric solid always has unit activity, so the | |
generalized concentration is 1 (dimensionless).""" | |
return (0,0) | |
def build(self, p): | |
ph = phase.build(self, p) | |
e = ph.addChild("thermo") | |
e['model'] = 'StoichSubstance' | |
addFloat(e, 'density', self._dens, defunits = _umass+'/'+_ulen+'3') | |
if self._tr: | |
t = ph.addChild('transport') | |
t['model'] = self._tr | |
k = ph.addChild("kinetics") | |
k['model'] = 'none' | |
class stoichiometric_liquid(stoichiometric_solid): | |
""" | |
An incompressible stoichiometric liquid. Currently, there is no | |
distinction between stoichiometric liquids and solids. | |
""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
density = -1.0, | |
transport = 'None', | |
initial_state = None, | |
options = []): | |
""" | |
See :class:`.phase` for descriptions of the parameters. | |
""" | |
stoichiometric_solid.__init__(self, name, elements, | |
species, density, transport, | |
initial_state, options) | |
class metal(phase): | |
"""A metal.""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
density = -1.0, | |
transport = 'None', | |
initial_state = None, | |
options = []): | |
phase.__init__(self, name, 3, elements, species, 'none', | |
initial_state, options) | |
self._dens = density | |
self._pure = 0 | |
self._tr = transport | |
def conc_dim(self): | |
return (0,0) | |
def build(self, p): | |
ph = phase.build(self, p) | |
e = ph.addChild("thermo") | |
e['model'] = 'Metal' | |
addFloat(e, 'density', self._dens, defunits = _umass+'/'+_ulen+'3') | |
if self._tr: | |
t = ph.addChild('transport') | |
t['model'] = self._tr | |
k = ph.addChild("kinetics") | |
k['model'] = 'none' | |
class semiconductor(phase): | |
"""A semiconductor.""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
density = -1.0, | |
bandgap = 1.0 * eV, | |
effectiveMass_e = 1.0 * ElectronMass, | |
effectiveMass_h = 1.0 * ElectronMass, | |
transport = 'None', | |
initial_state = None, | |
options = []): | |
phase.__init__(self, name, 3, elements, species, 'none', | |
initial_state, options) | |
self._dens = density | |
self._pure = 0 | |
self._tr = transport | |
self._emass = effectiveMass_e | |
self._hmass = effectiveMass_h | |
self._bandgap = bandgap | |
def conc_dim(self): | |
return (1,-3) | |
def build(self, p): | |
ph = phase.build(self, p) | |
e = ph.addChild("thermo") | |
e['model'] = 'Semiconductor' | |
addFloat(e, 'density', self._dens, defunits = _umass+'/'+_ulen+'3') | |
addFloat(e, 'effectiveMass_e', self._emass, defunits = _umass) | |
addFloat(e, 'effectiveMass_h', self._hmass, defunits = _umass) | |
addFloat(e, 'bandgap', self._bandgap, defunits = 'eV') | |
if self._tr: | |
t = ph.addChild('transport') | |
t['model'] = self._tr | |
k = ph.addChild("kinetics") | |
k['model'] = 'none' | |
class incompressible_solid(phase): | |
"""An incompressible solid.""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
density = -1.0, | |
transport = 'None', | |
initial_state = None, | |
options = []): | |
phase.__init__(self, name, 3, elements, species, 'none', | |
initial_state, options) | |
self._dens = density | |
self._pure = 0 | |
if self._dens < 0.0: | |
raise CTI_Error('density must be specified.') | |
self._tr = transport | |
def conc_dim(self): | |
return (1,-3) | |
def build(self, p): | |
ph = phase.build(self, p) | |
e = ph.addChild("thermo") | |
e['model'] = 'Incompressible' | |
addFloat(e, 'density', self._dens, defunits = _umass+'/'+_ulen+'3') | |
if self._tr: | |
t = ph.addChild('transport') | |
t['model'] = self._tr | |
k = ph.addChild("kinetics") | |
k['model'] = 'none' | |
class lattice(phase): | |
def __init__(self, name = '', | |
elements = '', | |
species = '', | |
reactions = 'none', | |
transport = 'None', | |
initial_state = None, | |
options = [], | |
site_density = -1.0, | |
vacancy_species = ''): | |
phase.__init__(self, name, 3, elements, species, 'none', | |
initial_state, options) | |
self._tr = transport | |
self._n = site_density | |
self._vac = vacancy_species | |
self._species = species | |
if name == '': | |
raise CTI_Error('sublattice name must be specified') | |
if species == '': | |
raise CTI_Error('sublattice species must be specified') | |
if site_density < 0.0: | |
raise CTI_Error('sublattice '+name | |
+' site density must be specified') | |
def build(self,p, visible = 0): | |
#if visible == 0: | |
# return | |
ph = phase.build(self, p) | |
e = ph.addChild('thermo') | |
e['model'] = 'Lattice' | |
addFloat(e, 'site_density', self._n, defunits = _umol+'/'+_ulen+'3') | |
if self._vac: | |
e.addChild('vacancy_species',self._vac) | |
if self._tr: | |
t = ph.addChild('transport') | |
t['model'] = self._tr | |
k = ph.addChild("kinetics") | |
k['model'] = 'none' | |
class lattice_solid(phase): | |
"""A solid crystal consisting of one or more sublattices.""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
lattices = [], | |
transport = 'None', | |
initial_state = None, | |
options = []): | |
# find elements | |
elist = [] | |
for lat in lattices: | |
e = lat._el.split() | |
for el in e: | |
if not el in elist: | |
elist.append(el) | |
elements = ' '.join(elist) | |
# find species | |
slist = [] | |
for lat in lattices: | |
_sp = "" | |
for spp in lat._species: | |
_sp = _sp + spp | |
s = _sp.split() | |
for sp in s: | |
if not sp in slist: | |
slist.append(sp) | |
species = ' '.join(slist) | |
phase.__init__(self, name, 3, elements, species, 'none', | |
initial_state, options) | |
self._lattices = lattices | |
if lattices == []: | |
raise CTI_Error('One or more sublattices must be specified.') | |
self._pure = 0 | |
self._tr = transport | |
def conc_dim(self): | |
return (0,0) | |
def build(self, p): | |
ph = phase.build(self, p) | |
e = ph.addChild("thermo") | |
e['model'] = 'LatticeSolid' | |
if self._lattices: | |
lat = e.addChild('LatticeArray') | |
for n in self._lattices: | |
n.build(lat, visible = 1) | |
if self._tr: | |
t = ph.addChild('transport') | |
t['model'] = self._tr | |
k = ph.addChild("kinetics") | |
k['model'] = 'none' | |
class liquid_vapor(phase): | |
"""A fluid with a complete liquid/vapor equation of state. | |
This entry type selects one of a set of predefined fluids with | |
built-in liquid/vapor equations of state. The substance_flag | |
parameter selects the fluid. See purefluids.py for the usage | |
of this entry type.""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
substance_flag = 0, | |
initial_state = None, | |
options = []): | |
phase.__init__(self, name, 3, elements, species, 'none', | |
initial_state, options) | |
self._subflag = substance_flag | |
self._pure = 1 | |
def conc_dim(self): | |
return (0,0) | |
def build(self, p): | |
ph = phase.build(self, p) | |
e = ph.addChild("thermo") | |
e['model'] = 'PureFluid' | |
e['fluid_type'] = repr(self._subflag) | |
k = ph.addChild("kinetics") | |
k['model'] = 'none' | |
class RedlichKwongMFTP(phase): | |
"""A fluid with a complete liqui/vapor equation of state. | |
This entry type selects one of a set of predefined fluids with | |
built-in liquid/vapor equations of state. The substance_flag | |
parameter selects the fluid. See purefluids.py for the usage | |
of this entry type.""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
initial_state = None, | |
activity_coefficients = None, | |
options = []): | |
phase.__init__(self,name, 3, elements, species, 'none', | |
initial_state,options) | |
self._pure = 0 | |
self._activityCoefficients = activity_coefficients | |
def conc_dim(self): | |
return (0,0) | |
def build(self, p): | |
ph = phase.build(self,p) | |
e = ph.addChild("thermo") | |
e['model'] = 'RedlichKwongMFTP' | |
if self._activityCoefficients: | |
a = e.addChild("activityCoefficients") | |
if isinstance(self._activityCoefficients, activityCoefficients): | |
self._activityCoefficients.build(a) | |
else: | |
na = len(self._activityCoefficients) | |
for n in range(na): | |
self._activityCoefficients[n].build(a) | |
k = ph.addChild("kinetics") | |
k['model'] = 'none' | |
class redlich_kwong(phase): | |
"""A fluid with a complete liquid/vapor equation of state. | |
This entry type selects one of a set of predefined fluids with | |
built-in liquid/vapor equations of state. The substance_flag | |
parameter selects the fluid. See purefluids.py for the usage | |
of this entry type.""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
substance_flag = 7, | |
initial_state = None, | |
Tcrit = 1.0, | |
Pcrit = 1.0, | |
options = []): | |
phase.__init__(self, name, 3, elements, species, 'none', | |
initial_state, options) | |
self._subflag = 7 | |
self._pure = 1 | |
self._tc = 1 | |
self._pc = 1 | |
def conc_dim(self): | |
return (0,0) | |
def build(self, p): | |
ph = phase.build(self, p) | |
e = ph.addChild("thermo") | |
e['model'] = 'PureFluid' | |
e['fluid_type'] = repr(self._subflag) | |
addFloat(e, 'Tc', self._tc, defunits = "K") | |
addFloat(e, 'Pc', self._pc, defunits = "Pa") | |
addFloat(e, 'MolWt', self._mw, defunits = _umass+"/"+_umol) | |
ph.addChild("kinetics") | |
k['model'] = 'none' | |
class ideal_interface(phase): | |
"""A chemically-reacting ideal surface solution of multiple species.""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
reactions = 'none', | |
site_density = 0.0, | |
phases = [], | |
kinetics = 'Interface', | |
transport = 'None', | |
initial_state = None, | |
options = []): | |
""" | |
The parameters correspond to those of :class:`.phase`, with the | |
following modifications: | |
:param reactions: | |
The heterogeneous reactions at this interface. If omitted, no | |
reactions will be included. A string or sequence of strings in the | |
format described in :ref:`sec-declaring-reactions`. | |
:param site_density: | |
The number of adsorption sites per unit area. | |
:param phases: | |
A string listing the bulk phases that participate in reactions | |
at this interface. | |
""" | |
self._type = 'surface' | |
phase.__init__(self, name, 2, elements, species, reactions, | |
initial_state, options) | |
self._pure = 0 | |
self._kin = kinetics | |
self._tr = transport | |
self._phases = phases | |
self._sitedens = site_density | |
def build(self, p): | |
ph = phase.build(self, p) | |
e = ph.addChild("thermo") | |
e['model'] = 'Surface' | |
addFloat(e, 'site_density', self._sitedens, defunits = _umol+'/'+_ulen+'2') | |
k = ph.addChild("kinetics") | |
k['model'] = self._kin | |
t = ph.addChild('transport') | |
t['model'] = self._tr | |
p = ph.addChild('phaseArray',self._phases) | |
def conc_dim(self): | |
return (1, -2) | |
class edge(phase): | |
"""A 1D boundary between two surface phases.""" | |
def __init__(self, | |
name = '', | |
elements = '', | |
species = '', | |
reactions = 'none', | |
site_density = 0.0, | |
phases = [], | |
kinetics = 'Edge', | |
transport = 'None', | |
initial_state = None, | |
options = []): | |
self._type = 'edge' | |
phase.__init__(self, name, 1, elements, species, reactions, | |
initial_state, options) | |
self._pure = 0 | |
self._kin = kinetics | |
self._tr = transport | |
self._phases = phases | |
self._sitedens = site_density | |
def build(self, p): | |
ph = phase.build(self, p) | |
e = ph.addChild("thermo") | |
e['model'] = 'Edge' | |
addFloat(e, 'site_density', self._sitedens, defunits = _umol+'/'+_ulen) | |
k = ph.addChild("kinetics") | |
k['model'] = self._kin | |
t = ph.addChild('transport') | |
t['model'] = self._tr | |
p = ph.addChild('phaseArray',self._phases) | |
def conc_dim(self): | |
return (1, -1) | |
## class binary_salt_parameters: | |
## def __init__(self, | |
## cation = "", | |
## anion = "", | |
## beta0 = None, | |
## beta1 = None, | |
## beta2 = None, | |
## Cphi = None, | |
## Alpha1 = -1.0): | |
## self._cation = cation | |
## self._anion = anion | |
## self._beta0 = beta0 | |
## self._beta1 = beta1 | |
## self._Cphi = Cphi | |
## self._Alpha1 = Alpha1 | |
## def build(self, a): | |
## s = a.addChild("binarySaltParameters") | |
## s["cation"] = self._cation | |
## s["anion"] = self._anion | |
## s.addChild("beta0", self._beta0) | |
## s.addChild("beta1", self._beta1) | |
## s.addChild("beta2", self._beta2) | |
## s.addChild("Cphi", self._Cphi) | |
## s.addChild("Alpha1", self._Alpha1) | |
## class theta_anion: | |
## def __init__(self, | |
## anions = None, | |
## theta = 0.0): | |
## self._anions = anions | |
## self._theta = theta | |
## def build(self, a): | |
## s = a.addChild("thetaAnion") | |
## s["anion1"] = self._anions[0] | |
## s["anion2"] = self._anions[1] | |
## s.addChild("Theta", self._theta) | |
## class psi_common_cation: | |
## def __init__(self, | |
## anions = None, | |
## cation = '', | |
## theta = 0.0, | |
## psi = 0.0): | |
## self._anions = anions | |
## self._cation = cation | |
## self._theta = theta | |
## self._psi = psi | |
## def build(self, a): | |
## s = a.addChild("psiCommonCation") | |
## s["anion1"] = self._anions[0] | |
## s["anion2"] = self._anions[1] | |
## s["cation"] = self._cation | |
## s.addChild("Theta", self._theta) | |
## s.addChild("Psi", self._psi) | |
## class psi_common_anion: | |
## def __init__(self, | |
## anion = '', | |
## cations = None, | |
## theta = 0.0, | |
## psi = 0.0): | |
## self._anion = anion | |
## self._cations = cations | |
## self._theta = theta | |
## self._psi = psi | |
## def build(self, a): | |
## s = a.addChild("psiCommonAnion") | |
## s["anion1"] = self._cations[0] | |
## s["anion2"] = self._cations[1] | |
## s["cation"] = self._anion | |
## s.addChild("Theta", self._theta) | |
## s.addChild("Psi", self._psi) | |
## class theta_cation: | |
## def __init__(self, | |
## cations = None, | |
## theta = 0.0): | |
## self._cations = cations | |
## self._theta = theta | |
## def build(self, a): | |
## s = a.addChild("thetaCation") | |
## s["cation1"] = self._anions[0] | |
## s["cation2"] = self._anions[1] | |
## s.addChild("Theta", self._theta) | |
## class pitzer: | |
## def __init__(self, | |
## temp_model = "", | |
## A_Debye = "", | |
## default_ionic_radius = -1.0, | |
## class electrolyte(phase): | |
## """An electrolye solution obeying the HMW model.""" | |
## def __init__(self, | |
## name = '', | |
## elements = '', | |
## species = '', | |
## transport = 'None', | |
## initial_state = None, | |
## solvent = '', | |
## standard_concentration = '', | |
## activity_coefficients = None, | |
## options = []): | |
## phase.__init__(self, name, 3, elements, species, 'none', | |
## initial_state, options) | |
## self._pure = 0 | |
## self._solvent = solvent | |
## self._stdconc = standard_concentration | |
## def conc_dim(self): | |
## return (1,-3) | |
## def build(self, p): | |
## ph = phase.build(self, p) | |
## e = ph.addChild("thermo") | |
## sc = e.addChild("standardConc") | |
## sc['model'] = self._stdconc | |
## e['model'] = 'HMW' | |
## e.addChild("activity_coefficients") | |
## addFloat(e, 'density', self._dens, defunits = _umass+'/'+_ulen+'3') | |
## if self._tr: | |
## t = ph.addChild('transport') | |
## t['model'] = self._tr | |
## k = ph.addChild("kinetics") | |
## k['model'] = 'none' | |
#------------------------------------------------------------------- | |
# falloff parameterizations | |
class Troe(object): | |
"""The Troe falloff function.""" | |
def __init__(self, A = 0.0, T3 = 0.0, T1 = 0.0, T2 = -999.9): | |
""" | |
Parameters: *A*, *T3*, *T1*, *T2*. These must be entered as pure | |
numbers with no attached dimensions. | |
""" | |
if T2 != -999.9: | |
self._c = (A, T3, T1, T2) | |
else: | |
self._c = (A, T3, T1) | |
def build(self, p): | |
s = '' | |
for num in self._c: | |
s += '%g ' % num | |
f = p.addChild('falloff', s) | |
f['type'] = 'Troe' | |
class SRI(object): | |
""" The SRI falloff function.""" | |
def __init__(self, A = 0.0, B = 0.0, C = 0.0, D = -999.9, E=-999.9): | |
""" | |
Parameters: *A*, *B*, *C*, *D*, *E*. These must be entered as | |
pure numbers without attached dimensions. | |
""" | |
if D != -999.9 and E != -999.9: | |
self._c = (A, B, C, D, E) | |
else: | |
self._c = (A, B, C) | |
def build(self, p): | |
s = '' | |
for num in self._c: | |
s += '%g ' % num | |
f = p.addChild('falloff', s) | |
f['type'] = 'SRI' | |
class Lindemann(object): | |
"""The Lindemann falloff function.""" | |
def __init__(self): | |
""" This falloff function takes no parameters.""" | |
pass | |
def build(self, p): | |
f = p.addChild('falloff') | |
f['type'] = 'Lindemann' | |
#get_atomic_wts() | |
validate() | |
def convert(filename, outName=None): | |
import os, sys | |
base = os.path.basename(filename) | |
root, _ = os.path.splitext(base) | |
dataset(root) | |
try: | |
with open(filename) as f: | |
code = compile(f.read(), filename, 'exec') | |
exec(code) | |
except SyntaxError as err: | |
# Show more context than the default SyntaxError message | |
# to help see problems in multi-line statements | |
text = open(filename).readlines() | |
print('%s in "%s" on line %i:\n' % (err.__class__.__name__, | |
err.filename, | |
err.lineno)) | |
print('| Line |') | |
for i in range(max(err.lineno-6, 0), | |
min(err.lineno+3, len(text))): | |
print('| % 5i |' % (i+1), text[i].rstrip()) | |
if i == err.lineno-1: | |
print(' '* (err.offset+9) + '^') | |
print() | |
sys.exit(3) | |
except TypeError as err: | |
import traceback | |
text = open(filename).readlines() | |
tb = traceback.extract_tb(sys.exc_info()[2]) | |
lineno = tb[-1][1] | |
print('%s on line %i of %s:' % (err.__class__.__name__, lineno, filename)) | |
print(err) | |
print('\n| Line |') | |
for i in range(max(lineno-6, 0), | |
min(lineno+3, len(text))): | |
if i == lineno-1: | |
print('> % 4i >' % (i+1), text[i].rstrip()) | |
else: | |
print('| % 4i |' % (i+1), text[i].rstrip()) | |
sys.exit(4) | |
write(outName) | |
if __name__ == "__main__": | |
import sys | |
if len(sys.argv) not in (2,3): | |
raise ValueError('Incorrect number of command line arguments.') | |
convert(*sys.argv[1:]) |
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Starting from version from Cantera trunk as of Subversion revision 2391