def _make_ccache(self):
pseudo = json.load(open('/home/user/code/thermodynamics/thermodynamics_data/kegg_pseudoisomers.json'))
rxns = []
cnt = 0
for i, item in enumerate(pseudo):
rxns.append('1 ' + item['CID'] + ' <=> 1 ' + item['CID'])
cnt = cnt + 1
if cnt>2000:
model = KeggModel.from_formulas(rxns)
model.ccache.dump()
rxns = []
cnt = 0
model = KeggModel.from_formulas(rxns)
model.ccache.dump()
def calculate_deltaG0s(model,
kegg_compounds,
pH=default_pH,
I=default_I,
T=default_T):
""" Calculate standard Gibbs Energy for reactions in model (as many as possible) using eQuilibrator.
Args:
model (CBModel): model
kegg_compounds (list): KEGG compounds accepted by eQuilibrator
pH (float): pH (default: 7.0)
I (float): ionic strenght (default: 0.25)
T (float): temperature (default: 298.15 K (25.0 C))
Returns:
dict: standard Gibbs Energies indexed by reaction ids
dict: estimation error indexed by reaction ids
"""
kegg_rxns = build_kegg_reactions(model, kegg_compounds)
kmodel = KeggModel.from_formulas(kegg_rxns.values(), raise_exception=True)
kmodel.add_thermo(CC.init())
dG0, sdG0, _ = kmodel.get_transformed_dG0(pH, I, T)
dG0 = dict(zip(kegg_rxns.keys(), dG0.A1))
sdG0 = dict(zip(kegg_rxns.keys(), sdG0.A1))
return dG0, sdG0
def _make_ccache(self):
pseudo = json.load(
open(
'/home/user/code/thermodynamics/thermodynamics_data/kegg_pseudoisomers.json'
))
rxns = []
cnt = 0
for i, item in enumerate(pseudo):
rxns.append('1 ' + item['CID'] + ' <=> 1 ' + item['CID'])
cnt = cnt + 1
if cnt > 2000:
model = KeggModel.from_formulas(rxns)
model.ccache.dump()
rxns = []
cnt = 0
model = KeggModel.from_formulas(rxns)
model.ccache.dump()
def generate_kegg_model(self, reactions):
rstrings = []
for r in reactions:
k = r.kegg_reaction
if k:
if k.is_balanced() and not k.is_empty():
rstrings.append(k.write_formula())
self.reactions.append(r)
else:
self._not_balanced.append(r)
return KeggModel.from_formulas(rstrings)
def generate_kegg_model(self, reactions):
rstrings = []
for r in reactions:
k = r.kegg_reaction
if k:
if k.is_balanced() and not k.is_empty():
rstrings.append(k.write_formula())
self.reactions.append(r)
else:
self._not_balanced.append(r)
return KeggModel.from_formulas(rstrings)
def KeggFile2ModelList(pathway_file):
kegg_file = ParsedKeggFile.FromKeggFile(pathway_file)
entries = kegg_file.entries()
pathways = []
for entry in entries:
fields = kegg_file[entry]
rids, fluxes, reactions = ParsedKeggFile.ParseReactionModule(fields)
bounds = ParsedKeggFile.ParseBoundModule(fields)
model = KeggModel.from_formulas(reactions)
model.rids = rids
pH = fields.GetFloatField("PH", 7.5)
I = fields.GetFloatField("I", 0.2)
T = fields.GetFloatField("T", 298.15)
pathways.append({"entry": entry, "model": model, "fluxes": fluxes, "bounds": bounds, "pH": pH, "I": I, "T": T})
return pathways
def KeggFile2ModelList(pathway_file):
kegg_file = ParsedKeggFile.FromKeggFile(pathway_file)
entries = kegg_file.entries()
pathways = []
for entry in entries:
fields = kegg_file[entry]
rids, fluxes, reactions = ParsedKeggFile.ParseReactionModule(fields)
bounds = ParsedKeggFile.ParseBoundModule(fields)
model = KeggModel.from_formulas(reactions)
model.rids = rids
pH = fields.GetFloatField('PH', 7.5)
I = fields.GetFloatField('I', 0.2)
T = fields.GetFloatField('T', 298.15)
pathways.append({'entry': entry, 'model': model, 'fluxes': fluxes,
'bounds': bounds, 'pH': pH, 'I': I, 'T': T})
return pathways
def _component_contribution_wrapper(self, reaction_list_I, pH_I,
temperature_I, ionic_strength_I):
"""wrapper for component contribution"""
# Orginal implementation involves an input of a reaction list
# the dG_prime and dG_std for each reaction are then calculated.
# Because we are interested in accounting for transportation
# and metabolite concentration,
# we need to extraction out the dG_prime and dG_std
# of formation and calculated the dG_prime and
# dG_std for each reaction after accounting for
# transportation and metabolite concentration.
# TODO: change input from reaction list to metabolite list
# however this may be problematic due to the implementation
# of component_contribution (i.e., the group contribution
# and reactant contribution are calculated along orthoganol planes
# in order to gain greater coverage and accuracy of predicted
# dG_f values)
# Debugging:
#wolf = ['C00049 + C00002 <=> C03082 + C00008',
# 'C00026 + C00049 <=> C00025 + C00036',
# 'C00158 <=> C00311',
# 'C00631 <=> C00001 + C00074',
# 'C00354 <=> C00111 + C00118',
# 'C00020 + C00002 <=> 2 C00008',
# 'C00002 + C00001 <=> C00008 + C00009',
# 'C00015 + C00002 <=> C00075 + C00008',
# 'C00033 + C00002 + C00010 <=> C00024 + C00020 + C00013']
#model = KeggModel.from_formulas(wolf)
model = KeggModel.from_formulas(reaction_list_I)
td = TrainingData()
cc = ComponentContribution(td)
model.add_thermo(cc)
dG0_prime_f, dG0_var_f = model.get_transformed_dG0(pH=pH_I,
I=ionic_strength_I,
T=temperature_I)
return dG0_prime_f, dG0_var_f
def reaction2udG0_prime(self):
'''
Calculates the dG0 of a list of a reaction.
Uses the component-contribution package (Noor et al) to estimate
the standard Gibbs Free Energy of reactions based on
component contribution approach and measured values (NIST and Alberty)
Arguments:
List of cobra model reaction ids
Returns:
Array of dG0 values and standard deviation of estimates
'''
Kmodel = KeggModel.from_formulas(self.reaction_strings)
Kmodel.add_thermo(self.cc)
dG0_prime, dG0_cov = Kmodel.get_transformed_dG0(pH=7.5,
I=0.2,
T=298.15)
dG0_std = 1.96 * np.diag(dG0_cov.round(1))
return unumpy.uarray((dG0_prime.flat, dG0_std.flat))
def __init__(self):
self.prepare_mappings()
reactions = self.get_reactions_from_model()
self.reactions = []
self._not_balanced = []
self.rstrings = []
for r in reactions:
k = r.kegg_reaction
if k:
if k.is_balanced() and not k.is_empty():
self.rstrings.append(k.write_formula())
self.reactions.append(r)
else:
self._not_balanced.append(r)
self.Kmodel = KeggModel.from_formulas(self.rstrings)
self.cc = ComponentContribution.init()
self.pH = 7.3
self.I = 0.25
self.RT = R * default_T
def reaction2dG0(reaction_list):
'''
Calculates the dG0 of a list of a reaction.
Uses the component-contribution package (Noor et al) to estimate
the standard Gibbs Free Energy of reactions based on
component contribution approach and measured values (NIST and Alberty)
Arguments:
List of reaction strings
Returns:
Array of dG0 values and standard deviation of estimates
'''
cc = ComponentContribution.init()
Kmodel = KeggModel.from_formulas(reaction_list)
Kmodel.add_thermo(cc)
dG0_prime, dG0_std = Kmodel.get_transformed_dG0(pH=7.5, I=0.2, T=298.15)
dG0_prime = np.array(map(lambda x: x[0,0], dG0_prime))
dG0_prime = unumpy.uarray(dG0_prime, np.diag(dG0_std))
return dG0_prime
def __init__(self):
self.prepare_mappings()
reactions = self.get_reactions_from_model()
self.reactions = []
self._not_balanced = []
self.rstrings = []
for r in reactions:
k = r.kegg_reaction
if k:
if k.is_balanced() and not k.is_empty():
self.rstrings.append(k.write_formula())
self.reactions.append(r)
else:
self._not_balanced.append(r)
self.Kmodel = KeggModel.from_formulas(self.rstrings)
self.cc = ComponentContribution.init()
self.pH = 7.3
self.I = 0.25
self.RT = R * default_T
def _component_contribution_wrapper(self,reaction_list_I,pH_I,temperature_I,ionic_strength_I):
"""wrapper for component contribution"""
# Orginal implementation involves an input of a reaction list
# the dG_prime and dG_std for each reaction are then calculated.
# Because we are interested in accounting for transportation
# and metabolite concentration,
# we need to extraction out the dG_prime and dG_std
# of formation and calculated the dG_prime and
# dG_std for each reaction after accounting for
# transportation and metabolite concentration.
# TODO: change input from reaction list to metabolite list
# however this may be problematic due to the implementation
# of component_contribution (i.e., the group contribution
# and reactant contribution are calculated along orthoganol planes
# in order to gain greater coverage and accuracy of predicted
# dG_f values)
# Debugging:
#wolf = ['C00049 + C00002 <=> C03082 + C00008',
# 'C00026 + C00049 <=> C00025 + C00036',
# 'C00158 <=> C00311',
# 'C00631 <=> C00001 + C00074',
# 'C00354 <=> C00111 + C00118',
# 'C00020 + C00002 <=> 2 C00008',
# 'C00002 + C00001 <=> C00008 + C00009',
# 'C00015 + C00002 <=> C00075 + C00008',
# 'C00033 + C00002 + C00010 <=> C00024 + C00020 + C00013']
#model = KeggModel.from_formulas(wolf)
model = KeggModel.from_formulas(reaction_list_I)
td = TrainingData()
cc = ComponentContribution(td)
model.add_thermo(cc)
dG0_prime_f, dG0_var_f = model.get_transformed_dG0(pH=pH_I, I=ionic_strength_I, T=temperature_I)
return dG0_prime_f, dG0_var_f
import numpy as np
from component_contribution.thermodynamic_constants import default_RT
from component_contribution.component_contribution_trainer import ComponentContribution
from component_contribution.kegg_model import KeggModel
import os
example_path = os.path.dirname(os.path.realpath(__file__))
REACTION_FNAME = os.path.join(example_path, 'wolf_reactions.txt')
cc = ComponentContribution.init()
with open(REACTION_FNAME, 'r') as fp:
reaction_strings = fp.readlines()
model = KeggModel.from_formulas(reaction_strings, raise_exception=True)
model.add_thermo(cc)
dG0_prime, dG0_std, sqrt_Sigma = model.get_transformed_dG0(7.0, 0.1, 298.15)
mM_conc = 1e-3 * np.matrix(np.ones((len(model.cids), 1)))
if 'C00001' in model.cids:
mM_conc[model.cids.index('C00001'), 0] = 1.0
dGm_prime = dG0_prime + default_RT * model.S.T * np.log(mM_conc)
for i, r in enumerate(reaction_strings):
print '-' * 50
print r.strip()
print "dG0 = %8.1f +- %5.1f" % (model.dG0[i, 0], dG0_std[i, 0] * 1.96)
print "dG'0 = %8.1f +- %5.1f" % (dG0_prime[i, 0], dG0_std[i, 0] * 1.96)
print "dG'm = %8.1f +- %5.1f" % (dGm_prime[i, 0], dG0_std[i, 0] * 1.96)
import logging
from scipy.io import savemat
from component_contribution.component_contribution import ComponentContribution
from component_contribution.kegg_model import KeggModel
REACTION_FNAME = '../examples/simeon_reactions.txt'
OUTPUT_FNAME = '../res/simeon.mat'
logger = logging.getLogger('')
logger.setLevel(logging.INFO)
cc = ComponentContribution.init()
reaction_strings = open(REACTION_FNAME, 'r').readlines()
model = KeggModel.from_formulas(reaction_strings)
model.add_thermo(cc)
dG0_prime, dG0_std, _ = model.get_transformed_dG0(7.0, 0.2, 298.15)
print "For a linear problem, define two vector variables 'x' and 'y', each of length Nr (i.e. " + \
"the same length as the list of reactions). Then add these following " + \
"constraints: \n" + \
"-1 <= y <= 1\n" + \
"x = dG0_prime + 3 * dG0_std * y\n" + \
"Then use 'x' as the value of the standard Gibbs energy for all reactions."
print "The results are writteng to: " + OUTPUT_FNAME
savemat(OUTPUT_FNAME,
{'dG0_prime': dG0_prime, 'dG0_std': dG0_std},
oned_as='row')