def __init__(self, ID='', ins=None, outs=(), saccharified_slurry_split = 0.1, P=101325):
Unit.__init__(self, ID, ins, outs)
self.P = P
# Split to outs[2]
self.saccharified_slurry_split = saccharified_slurry_split
#: [ParallelReaction] Enzymatic hydrolysis reactions including from downstream batch tank in co-fermentation.
self.saccharification = ParallelRxn([
# Reaction definition Reactant Conversion
Rxn('Glucan -> GlucoseOligomer', 'Glucan', 0.0400),
Rxn('Glucan + 0.5 H2O -> 0.5 Cellobiose', 'Glucan', 0.0120),
Rxn('Glucan + H2O -> Glucose', 'Glucan', 0.8000),#changed
Rxn('GlucoseOligomer + H2O -> Glucose', 'GlucoseOligomer', 1.0000),
Rxn('Cellobiose + H2O -> Glucose', 'Cellobiose', 1.0000),
Rxn('Xylan -> XyloseOligomer', 'Xylan', 0.0400),
Rxn('Xylan + H2O -> Xylose', 'Xylan', 0.9000)
])
self.loss = ParallelRxn([
# Reaction definition Reactant Conversion
Rxn('Glucose -> 2 LacticAcid', 'Glucose', 0.0300),
Rxn('3 Xylose -> 5 LacticAcid', 'Xylose', 0.0300),
Rxn('3 Arabinose -> 5 LacticAcid', 'Arabinose', 0.0300),
Rxn('Galactose -> 2 LacticAcid', 'Galactose', 0.0300),
Rxn('Mannose -> 2 LacticAcid', 'Mannose', 0.0300),])
self.cofermentation = ParallelRxn([
# Reaction definition Reactant Conversion
Rxn('Glucose -> 2 Ethanol + 2 CO2', 'Glucose', 0.8300),#changed
Rxn('Glucose + 0.62 NH3 + 2.17 O2 -> 3.65 S_cerevisiae + 3.71 H2O + 2.34 CO2', 'Glucose', 0.0130),
Rxn('Glucose + 2 H2O -> 2 Glycerol + O2', 'Glucose', 0.0040),
Rxn('2 Glucose + 1.5 O2 -> 3 SuccinicAcid + 3 H2O', 'Glucose', 0.0060),
])
self.saccharified_stream = tmo.Stream(None)
def __init__(self, ID='', ins=None, outs=()):
Unit.__init__(self, ID, ins, outs)
self.reactions = ParallelRxn([
# Reaction definition Reactant Conversion
Rxn('Glucose -> 2 Ethanol + 2 CO2', 'Glucose', 0.0400),##0.04
Rxn('Glucose + 0.62 NH3 + 2.17 O2 -> 3.65 S_cerevisiae + 3.71 H2O + 2.34 CO2', 'Glucose', 0.2400),##0.90
Rxn('Glucose + 2 H2O -> 2 Glycerol + O2', 'Glucose', 0.0040),
Rxn('2 Glucose + 1.5 O2 -> 3 SuccinicAcid + 3 H2O', 'Glucose', 0.0060)
])
def __init__(self,
ID='',
ins=None,
outs=(),
*,
reactions,
sludge_split,
T):
Unit.__init__(self, ID, ins, outs)
self.reactions = reactions
self.sludge_split = sludge_split
self.multi_stream = tmo.MultiStream()
self.T = T
def __init__(self, ID='', ins=None, outs=()):
Unit.__init__(self, ID, ins, outs)
self.reactions = ParallelRxn([
# Reaction definition Reactant Conversion
Rxn('Glucose -> 2 Ethanol + 2 CO2', 'Glucose', 0.9000),
Rxn('Glucose + 8.463 CSL + 0.018 DAP -> 6 Z_mobilis + 2.4 H2O',
'Glucose', 0.0400),
Rxn('Glucose + 2 H2O -> 2 Glycerol + O2', 'Glucose', 0.0040),
Rxn('Glucose + 2 CO2 -> 2 SuccinicAcid + O2', 'Glucose', 0.0060),
Rxn('3 Xylose -> 5 Ethanol + 5 CO2', 'Xylose', 0.8000),
Rxn('Xylose + 7.052 CSL + 0.015 DAP -> 5 Z_mobilis + 2 H2O',
'Xylose', 0.0400),
Rxn('3 Xylose + 5 H2O -> 5 Glycerol + 2.5 O2', 'Xylose', 0.0030),
Rxn('Xylose + H2O -> Xylitol + 0.5 O2', 'Xylose', 0.0460),
Rxn('3 Xylose + 5 CO2 -> 5 SuccinicAcid + 2.5 O2', 'Xylose', 0.0090)])
def __init__(self, ID='', ins=None, outs=()):
Unit.__init__(self, ID, ins, outs)
self._multistream = MultiStream(None)
self.reactions = ParallelRxn([
# Reaction definition Reactant Conversion
Rxn('Glucan + H2O -> Glucose', 'Glucan', 0.0510),#
Rxn('Glucan + H2O -> GlucoseOligomer', 'Glucan', 0.0750),#
Rxn('Glucan -> HMF + 2 H2O', 'Glucan', 0.0043),#
Rxn('Xylan + H2O -> Xylose', 'Xylan', 0.5190),#
Rxn('Xylan + H2O -> XyloseOligomer', 'Xylan', 0.2610),#
Rxn('Xylan -> Furfural + 2 H2O', 'Xylan', 0.0860),#
Rxn('Arabinan + H2O -> Arabinose', 'Arabinan', 1.0000),#
Rxn('Arabinan + H2O -> ArabinoseOligomer', 'Arabinan', 0.0000),#
Rxn('Arabinan -> Furfural + 2 H2O', 'Arabinan', 0.0000),#
Rxn('Acetate -> AceticAcid', 'Acetate', 1.0000),
Rxn('Lignin -> SolubleLignin', 'Lignin', 0.0470),
Rxn('Extract -> ExtractVol', 'Extract', 0.7000),
Rxn('Extract -> ExtractNonVol', 'Extract', 0.3000)])
vapor, liquid = self.outs
vapor.phase = 'g'
def __init__(self, ID='', ins=None, outs=(), P=101325):
Unit.__init__(self, ID, ins, outs)
self.P = P
#: [ParallelReaction] Enzymatic hydrolysis reactions including from downstream batch tank in co-fermentation.
self.saccharification = ParallelRxn([
# Reaction definition Reactant Conversion
Rxn('Glucan -> GlucoseOligomer', 'Glucan', 0.0400),
Rxn('Glucan + 0.5 H2O -> 0.5 Cellobiose', 'Glucan', 0.0120),
Rxn('Glucan + H2O -> Glucose', 'Glucan', 0.9000),
Rxn('Cellobiose + H2O -> Glucose', 'Cellobiose', 1.0000)
])
self.cofermentation = ParallelRxn([
# Reaction definition Reactant Conversion
Rxn('Glucose -> 2 Ethanol + 2 CO2', 'Glucose', 0.9500),
Rxn('Glucose + 0.047 CSL + 0.018 DAP -> 6 Z_mobilis + 2.4 H2O',
'Glucose', 0.0200),
Rxn('Glucose + 2 H2O -> 2 Glycerol + O2', 'Glucose', 0.0040),
Rxn('Glucose + 2 CO2 -> 2 SuccinicAcid + O2', 'Glucose', 0.0060),
Rxn('3 Xylose -> 5 Ethanol + 5 CO2', 'Xylose', 0.8500),
Rxn('Xylose + 0.039 CSL + 0.015 DAP -> 5 Z_mobilis + 2 H2O',
'Xylose', 0.0190),
Rxn('3 Xylose + 5 H2O -> 5 Glycerol + 2.5 O2', 'Xylose', 0.0030),
Rxn('Xylose + H2O -> Xylitol + 0.5 O2', 'Xylose', 0.0460),
Rxn('3 Xylose + 5 CO2 -> 5 SuccinicAcid + 2.5 O2', 'Xylose',
0.0090),
# Losses
Rxn('Glucose -> 2 LacticAcid', 'Glucose', 0.0300),
Rxn('3 Xylose -> 5 LacticAcid', 'Xylose', 0.0300),
Rxn('3 Arabinose -> 5 LacticAcid', 'Arabinose', 0.0300),
Rxn('Galactose -> 2 LacticAcid', 'Galactose', 0.0300),
Rxn('Mannose -> 2 LacticAcid', 'Mannose', 0.0300),
])
self.CSL2constituents = Rxn(
'CSL -> 0.5 H2O + 0.25 LacticAcid + 0.25 Protein', 'CSL', 1.0000)
self.saccharified_stream = bst.Stream(None)
def __init__(self, ID='', ins=None, outs=()):
Unit.__init__(self, ID, ins, outs)
self._multistream = MultiStream(None)
self.reactions = ParallelRxn([
# Reaction definition Reactant Conversion
Rxn('Glucan + H2O -> Glucose', 'Glucan', 0.0990),
Rxn('Glucan + H2O -> GlucoseOligomer', 'Glucan', 0.0030),
Rxn('Glucan -> HMF + 2 H2O', 'Glucan', 0.0030),
Rxn('Galactan + H2O -> GalactoseOligomer', 'Galactan', 0.0030),
Rxn('Galactan -> HMF + 2 H2O', 'Galactan', 0.0030),
Rxn('Mannan + H2O -> MannoseOligomer', 'Mannan', 0.0030),
Rxn('Mannan -> HMF + 2 H2O', 'Mannan', 0.0030),
Rxn('Sucrose -> HMF + Glucose + 2H2O', 'Sucrose', 1.0000),
Rxn('Xylan + H2O -> Xylose', 'Xylan', 0.9000),
Rxn('Xylan + H2O -> XyloseOligomer', 'Xylan', 0.0024),
Rxn('Xylan -> Furfural + 2 H2O', 'Xylan', 0.0050),
Rxn('Arabinan + H2O -> Arabinose', 'Arabinan', 0.9000),
Rxn('Arabinan + H2O -> ArabinoseOligomer', 'Arabinan', 0.0024),
Rxn('Arabinan -> Furfural + 2 H2O', 'Arabinan', 0.0050),
Rxn('Acetate -> AceticAcid', 'Acetate', 1.0000),
Rxn('Lignin -> SolubleLignin', 'Lignin', 0.0050)])
vapor, liquid = self.outs
vapor.phase = 'g'
def __init__(self, ID='', ins=None, outs=(), *, reactions):
Unit.__init__(self, ID, ins, outs)
self.reactions = reactions
def __init__(self, ID='', ins=None, outs=(), *, reactions, sludge_split):
Unit.__init__(self, ID, ins, outs)
self.reactions = reactions
self.sludge_split = sludge_split
self.mixed_stream = bst.MixedStream()
def __init__(self, ID='', ins=None, outs=()):
Unit.__init__(self, ID, ins, outs)