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|
import os,sys
import json
current = os.path.dirname(os.path.realpath(__file__))
parent = os.path.dirname(current)
parentPath = os.path.dirname(parent)
sys.path.append(parentPath)
from python.OMChem.Flowsheet import Flowsheet
from python.OMChem.EngStm import EngStm
from python.utils.ComponentSelector import *
from python.utils.Container import *
from PyQt5.QtCore import *
class UnitOperation():
counter = 1
def __init__(self):
self.OM_data_eqn = ''
self.OM_data_init = ''
self.input_stms = {}
self.output_stms = {}
self.compounds = [c[:c.index('(')] for c in compound_selected]
self.name = ''
self.mode = None
self.mode_val = None
self.type = ''
self.no_of_inputs = 1
self.no_of_outputs = 1
self.x = 2500-30
self.y = 2500-30
self.pos = QPointF(self.x, self.y)
self.count = UnitOperation.counter
self.variables = {}
self.modes_list = []
self.parameters = []
self.extra = []
self.for_naming = []
self.multidict = []
self.thermo_pack_req = False
self.thermo_package = 'RaoultsLaw'
self.saved = False
def param_getter(self,mode=None):
params = {}
if mode == None and self.modes_list:
self.mode = self.modes_list[0]
else:
self.mode = mode
params[self.mode] = None
for i in self.parameters:
params[i] = self.variables[i]['value']
return params
def param_getter_tooltip(self,mode=None):
params = {}
if mode == None and self.modes_list:
self.mode = self.modes_list[0]
else:
self.mode = mode
params[self.mode] = None
for i in self.parameters:
params[self.variables[i]['name']] = str(self.variables[i]['value'])+' '+self.variables[i]['unit']
return params
def param_setter(self,params):
print("param_setter ", params)
try:
self.mode = list(params.keys())[0]
except Exception as e:
print(e)
for k,v in params.items():
if k == 'Thermo Package':
self.thermo_package = v
elif k != self.mode:
self.k = v
self.variables[k]['value'] = v
else:
self.variables[k]['value'] = v
self.mode_val = params[self.mode]
def add_connection(self,flag,sourceId, UnitOpr):
if flag==1: # Input stream if flag is 1
self.input_stms[sourceId] = UnitOpr
else :
self.output_stms[sourceId] = UnitOpr
def set_pos(self,pos):
self.pos = pos
def update_compounds(self):
self.compounds = [c[:c.index('(')] for c in compound_selected]
def OM_Flowsheet_Initialize(self):
self.OM_data_init = ''
if(self.thermo_pack_req):
if len(self.extra)>1:
for i in range(len(self.extra)):
latest = ''
for j in range(self.extra[i]):
if self.extra[i][j]!='.':
latest += self.extra[i][j]
self.for_naming[i] = latest
if(self.thermo_pack_req):
if len(self.extra)==1:
for i in self.extra:
self.OM_data_init += ('model '+i+str(self.counter)+'\n')
self.OM_data_init += ('extends Simulator.UnitOperations.'+i+';\n')
self.OM_data_init += ('extends Simulator.Files.ThermodynamicPackages.'+self.thermo_package+';\n')
self.OM_data_init += ('end '+i+str(self.counter)+';\n')
self.OM_data_init += i+str(self.counter) + ' ' + self.name + '(Nc = ' + str(len(self.compounds))
else:
for i in range(len(self.extra)):
if i!=(len(self.extra)-1):
self.OM_data_init += ('model '+self.for_naming[i]+str(self.counter)+'\n')
self.OM_data_init += ('extends Simulator.UnitOperations.'+self.extra[i]+';\n')
self.OM_data_init += ('extends Simulator.Files.ThermodynamicPackages.'+self.thermo_package+';\n')
self.OM_data_init += ('end '+self.for_naming[i]+str(self.counter)+';\n')
else:
self.OM_data_init += ('model '+self.for_naming[i]+str(self.counter)+'\n')
self.OM_data_init += ('extends Simulator.UnitOperations.'+self.extra[i]+';\n')
for j in range(len(self.extra)-1):
self.OM_data_init += (self.for_naming[j] + str(self.counter) +' ' + self.for_naming[j] + '#' + self.multidict[j] + ';\n')
self.OM_data_init += ('end '+self.for_naming[i]+str(self.counter)+';\n')
self.OM_data_init += self.for_naming[i] + str(self.counter) + ' ' + self.for_naming + '(Nc = ' + str(len(self.compounds))
C = str(self.compounds).strip('[').strip(']')
C = C.replace("'", "")
self.OM_data_init += ',C = {' + C + '}'
for k in self.parameters:
if(k == 'HKey_x_pc' or k == 'LKey_x_pc'):
continue
self.OM_data_init += ', '
self.OM_data_init += k + ' = ' + (json.dumps(self.variables[k]['value']) if json.dumps(self.variables[k]['value']).replace('"', '').replace('_', '').isalpha()
else json.dumps(self.variables[k]['value']).replace('[', '{').replace(']', '}').replace('"', ''))
self.OM_data_init += ');\n'
else:
self.OM_data_init += 'Simulator.UnitOperations.' + self.type + ' ' + self.name + '(Nc = ' + str(len(self.compounds))
C = str(self.compounds).strip('[').strip(']')
C = C.replace("'", "")
self.OM_data_init += ',C = {' + C + '}'
for k in self.parameters:
self.OM_data_init += ', '
self.OM_data_init += k + ' = ' + (json.dumps(self.variables[k]['value']) if json.dumps(self.variables[k]['value']).replace('"', '').replace('_', '').isalpha()
else json.dumps(self.variables[k]['value']).replace('[', '{').replace(']', '}').replace('"', ''))
self.OM_data_init += ');\n'
return self.OM_data_init
def OM_Flowsheet_Equation(self):
self.OM_data_eqn = ''
if len(self.input_stms)>1 or self.type == 'Mixer':
strcount = 1
for strm in self.input_stms.values():
self.OM_data_eqn += ('connect(' + strm.name + '.Out,' + self.name + '.In[' + str(strcount) + ']);\n')
strcount += 1
else:
print(self.input_stms)
self.OM_data_eqn += ('connect(' + self.name + '.In,' + self.input_stms[1].name + '.Out);\n')
if len(self.output_stms)>1:
strcount = 1
for strm in self.output_stms.values():
self.OM_data_eqn += ('connect(' + strm.name + '.In,' + self.name + '.Out[' + str(strcount) + ']);\n')
strcount += 1
else:
print("self.output_stms ", self.output_stms)
self.OM_data_eqn += ('connect(' + self.name + '.Out,' + self.output_stms[1].name + '.In);\n')
if self.mode:
self.OM_data_eqn += (self.name + '.' + self.mode + '=' + str(self.mode_val) + ';\n')
return self.OM_data_eqn
class ShortcutColumn(UnitOperation):
def __init__(self, CompNames = [], name='ShortcutColumn'):
UnitOperation.__init__(self)
self.name = name + str(ShortcutColumn.counter)
self.type = 'ShortcutColumn'
self.no_of_inputs = 1
self.no_of_outputs = 2
self.EngStm1 = EngStm(name='EngStm1'+self.name)
self.EngStm2 = EngStm(name='EngStm2'+self.name)
self.count = ShortcutColumn.counter
self.extra = ['ShortcutColumn']
self.for_naming = ['ShortcutColumn']
self.thermo_pack_req = True
self.parameters = ['HKey', 'LKey', 'HKey_x_pc', 'LKey_x_pc', 'Ctype', 'Pcond', 'Preb', 'RR']
self.result_parameters = ['RRmin', 'Ntmin', 'Nt', 'Intray', 'Fliqstrip', 'Fliqrec', 'Fvapstrip', 'Fvaprec', 'Qc', 'Qr']
type(self).counter += 1
self.variables = {
'HKey' : {'name':'Heavy Key', 'value': 0, 'unit':''},
'LKey' : {'name':'Light Key', 'value': 0, 'unit':''},
'HKey_x_pc' : {'name':'Heavy Key Mole Fraction', 'value':0.01, 'unit':''},
'LKey_x_pc' : {'name':'Light Key Mole Fraction', 'value':0.01, 'unit':''},
'Ctype' : {'name':'Condenser Type', 'value':'Total', 'unit':''},
'thermo_package' : {'name':'Thermo Package', 'value':'Raoults_Law', 'unit':''},
'Pcond' : {'name':'Condenser Pressure', 'value':101325, 'unit':'Pa'},
'Preb' : {'name':'Reboiler Pressure', 'value':101325, 'unit':'Pa'},
'RR' : {'name':'Reflux Ratio', 'value':1.5, 'unit':''},
'RRmin' : {'name':'Minimum Reflux Ratio', 'value': None , 'unit':''},
'Ntmin' : {'name':'Minimum Number of Stages', 'value': None, 'unit':''},
'Nt' : {'name':'Actual Number of Stages', 'value': None, 'unit':''},
'Intray' : {'name':'Optimal Feed Stage', 'value': None, 'unit':''},
'Fliqstrip' : {'name':'Stripping Liquid', 'value': None, 'unit':'mol/s'},
'Fliqrec' : {'name':'Rectification Liquid', 'value': None, 'unit':'mol/s'},
'Fvapstrip' : {'name':'Stripping Vapor', 'value': None, 'unit':'mol/s'},
'Fvaprec' : {'name':'Recification Vapour', 'value': None, 'unit':'mol/s'},
'Qc' : {'name':'Conderser Duty', 'value': None, 'unit':'W'},
'Qr' : {'name':'Reboiler Duty', 'value': None, 'unit':'W'},
}
def update_compounds(self):
self.compounds = [c[:c.index('(')] for c in compound_selected]
def param_setter(self,params):
print("param_setter ", params)
self.variables['HKey']['value'] = self.compounds.index(params[0]) + 1
self.variables['LKey']['value'] = self.compounds.index(params[1]) + 1
self.variables['HKey_x_pc']['value'] = params[2]
self.variables['LKey_x_pc']['value'] = params[3]
self.variables['Ctype']['value'] = params[4]
self.variables['Pcond']['value'] = params[5]
self.variables['Preb']['value'] = params[6]
self.variables['RR']['value'] = params[7]
self.variables['thermo_package']['value'] = params[8]
def OM_Flowsheet_Equation(self):
self.OM_data_eqn = ''
self.OM_data_eqn += ('connect(' + self.name + '.In,' + self.input_stms[1].name + '.Out);\n')
strcount = 1
for strm in self.output_stms.values():
self.OM_data_eqn += ('connect(' + strm.name + '.In,' + self.name + '.Out' + str(strcount) + ');\n')
strcount += 1
self.OM_data_eqn += (self.name + '.x_pc[2, ' + self.name + '.HKey] = ' + str(self.variables['HKey_x_pc']['value']) + ';\n')
self.OM_data_eqn += (self.name + '.x_pc[3, ' + self.name + '.LKey] = ' + str(self.variables['LKey_x_pc']['value']) + ';\n')
return self.OM_data_eqn
class DistillationColumn(UnitOperation):
def __init__(self,name='DistillationColumn'):
UnitOperation.__init__(self)
self.name = name + str(DistillationColumn.counter)
self.type = 'DistillationColumn'
self.no_of_inputs = 1
self.no_of_outputs = 2
self.EngStm1 = EngStm(name='EngStm1'+self.name)
self.EngStm2 = EngStm(name='EngStm2'+self.name)
self.count = DistillationColumn.counter
self.thermo_pack_req = True
# self.modes_list = ['RR', 'Nout', 'T']
self.modes_list = []
self.parameters = ['Nt', 'Ni', 'Ctype', 'Pcond', 'condmode', 'C_comp', 'C_Spec', 'Preb', 'rebmode', 'rebcomp', 'R_Spec']
#self.parameters = ['Nt', 'InT_s', 'In_s', 'thermo_package', 'Ctype', 'Pcond', 'Preb']
self.result_parameters = ['Cduty.Q', 'Rduty.Q']
self.Cspec_list = ['Reflux Ratio','Product Molar Flow (mol/s)', 'Temperature (K)', 'Compound Molar Fraction', 'Compound Molar Flow (mol/s)']
self.Rspec_list = ['Product Molar Flow (mol/s)', 'Temperature (K)', 'Compound Molar Fraction', 'Compound Molar Flow (mol/s)']
type(self).counter += 1
self.variables = {
'Ni' : {'name':'Number of Input', 'value':1, 'unit':''},
'RR' : {'name':'Reflux Ratio', 'value':None, 'unit':''},
'T' : {'name':'Temperature', 'value':300, 'unit':'K'},
'Nout' : {'name':'No of Sidedraws', 'value':None, 'unit':''},
'Nt' : {'name':'No of Stages', 'value':12, 'unit':''},
'InT_s' : {'name':'Feed Stage', 'value':[], 'unit':''},
'thermo_package' : {'name':'Thermo Package', 'value':'Raoults_Law', 'unit':''},
'Ctype' : {'name':'Condenser Type', 'value':'Total', 'unit':''},
'Pcond' : {'name':'Condenser Pressure', 'value':101325, 'unit':'Pa'},
'Preb' : {'name':'Reboiler Pressure', 'value':101325, 'unit':'Pa'},
'C_Spec': {'name':'Condenser Specification', 'type':self.Cspec_list[0], 'value':'', 'comp':compound_selected[0], 'unit':''},
'R_Spec': {'name':'Reboiler Specification', 'type':self.Rspec_list[0], 'value':'', 'comp':compound_selected[0], 'unit':''},
'Cduty.Q': {'name':'Condenser Duty', 'value': '', 'unit':'W'},
'Rduty.Q': {'name':'Reboiler Duty', 'value': '', 'unit': 'W'},
'Stages.T': {'name':'Stagewise Temperature', 'value':[], 'unit':'K'},
'Stages.x_pc': {'name': 'Stagewise Component Mole Fraction', 'value':[],'unit':''}
}
def update_compounds(self):
self.compounds = [c[:c.index('(')] for c in compound_selected]
def param_setter(self,params):
print("param_setter ", params)
temp = 0
self.variables['Nt']['value'] = params[0]
for i in range(self.variables['Ni']['value']):
self.variables['InT_s']['value'].append(params[i+1])
temp = i + 1
self.variables['Ctype']['value'] = params[temp+1]
self.variables['Pcond']['value'] = params[temp+2]
self.variables['C_Spec']['type'] = params[temp+3]
if 'Compound' in self.variables['C_Spec']['type']:
self.variables['C_Spec']['comp'] = params[temp+4]
# C_Spec variable value won't be updated to class here. It will be updated in result
self.variables['C_Spec']['value'] = params[temp+5]
for var in self.variables:
if self.variables[var]['name'] == self.variables['C_Spec']['type']:
self.variables[var]['value'] = params[temp+5]
self.variables['Preb']['value'] = params[temp+6]
# R_Spec variable value won't be updated to class here. It will be updated in result
self.variables['R_Spec']['type'] = params[temp+7]
if 'Compound' in self.variables['R_Spec']['type']:
self.variables['R_Spec']['comp'] = params[temp+8]
self.variables['R_Spec']['value'] = params[temp+9]
self.variables['thermo_package']['value'] = params[temp+10]
print(self.variables)
def OM_Flowsheet_Initialize(self):
self.OM_data_init = ''
self.OM_data_init = self.OM_data_init + 'model Condenser\n'
self.OM_data_init = self.OM_data_init + 'extends Simulator.UnitOperations.DistillationColumn.Cond;\n'
self.OM_data_init = self.OM_data_init + 'extends Simulator.Files.ThermodynamicPackages.' + self.thermo_package + ';\n'
self.OM_data_init = self.OM_data_init + 'end Condenser;\n'
self.OM_data_init = self.OM_data_init + 'model Tray\n'
self.OM_data_init = self.OM_data_init + 'extends Simulator.UnitOperations.DistillationColumn.DistTray;\n'
self.OM_data_init = self.OM_data_init + 'extends Simulator.Files.ThermodynamicPackages.' + self.thermo_package + ';\n'
self.OM_data_init = self.OM_data_init + 'end Tray;\n'
self.OM_data_init = self.OM_data_init + 'model Reboiler\n'
self.OM_data_init = self.OM_data_init + 'extends Simulator.UnitOperations.DistillationColumn.Reb;\n'
self.OM_data_init = self.OM_data_init + 'extends Simulator.Files.ThermodynamicPackages.' + self.thermo_package + ';\n'
self.OM_data_init = self.OM_data_init + 'end Reboiler;\n'
self.OM_data_init = self.OM_data_init + ("model distCol" + str(self.count) + "\n")
self.OM_data_init = self.OM_data_init + ("extends Simulator.UnitOperations.DistillationColumn.DistCol;\n")
self.OM_data_init = self.OM_data_init + (
"Condenser condenser(Nc = Nc, C = C, Ctype =Ctype, Bin = Bin_t[1], T(start = 300));\n")
self.OM_data_init = self.OM_data_init + (
"Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]);\n")
self.OM_data_init = self.OM_data_init + (
"Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]);\n")
self.OM_data_init = self.OM_data_init + ("end distCol" + str(self.count) + ";\n")
comp_count = len(self.compounds)
self.OM_data_init = self.OM_data_init + (
"distCol" + str(self.count) + " " + self.name + "(Nc = " + str(comp_count))
self.OM_data_init = self.OM_data_init + (", C= C")
self.OM_data_init = self.OM_data_init + "," + (
"Nt=" + str(self.variables['Nt']['value']) + "," + "Ni="
+ str(self.variables['Ni']['value']) + ",InT_s=" + "{" +
str(self.variables['InT_s']['value']).strip('[').strip(']') + "}" + ',Ctype ="' +
self.variables['Ctype']['value'] + '");\n')
# self.OM_data_init = self.OM_data_init + 'Simulator.Streams.Energy_Stream '+self.EngStm1.name+';\n'
# self.OM_data_init = self.OM_data_init + 'Simulator.Streams.Energy_Stream '+self.EngStm2.name+';\n'
return self.OM_data_init
def OM_Flowsheet_Equation(self):
self.OM_data_eqn = ''
# self.OM_data_eqn = self.name + '.pressDrop = ' + str(self.PressDrop) + ';\n'
# self.OM_data_eqn = self.OM_data_eqn + (
# 'connect(' + self.name + '.' + 'condensor_duty' + ',' + self.EngStm1.name + '.inlet);\n')
# self.OM_data_eqn = self.OM_data_eqn + (
# 'connect(' + self.name + '.reboiler_duty' + ', ' + self.EngStm2.name + '.inlet);\n')
self.OM_data_eqn = self.OM_data_eqn + (
'connect(' + self.name + '.Dist' + ", " + self.output_stms[1].name + '.In);\n')
self.OM_data_eqn = self.OM_data_eqn + (
'connect(' + self.name + '.Bot' + ", " + self.output_stms[2].name + '.In);\n')
for i in range(len(self.input_stms)):
self.OM_data_eqn = self.OM_data_eqn + (
'connect(' + self.input_stms[i +1].name + '.Out' + ", " + self.name + '.In_s[' + str(
i + 1) + ']);\n')
# ['Product Molar Flow (mol/s)', 'Temperature (K)', 'Compound Molar Fraction',
# 'Compound Molar Flow (mol/s)']
if self.variables['C_Spec']['type'] == "Reflux Ratio":
self.OM_data_eqn = self.OM_data_eqn + (
self.name + '.' + 'RR' + '=' + str(self.variables['RR']['value']) + ';\n')
elif self.variables['C_Spec']['type'] == "Product Molar Flow (mol/s)":
self.OM_data_eqn = self.OM_data_eqn + (self.output_stms[1].name + '.' + 'F_p[1] = ' + str(
self.variables['C_Spec']['value']) + ';\n')
elif self.variables['C_Spec']['type'] == "Temperature (K)":
self.OM_data_eqn = self.OM_data_eqn + (self.output_stms[1].name + '.' + 'T = ' + str(
self.variables['C_Spec']['value']) + ';\n')
elif self.variables['C_Spec']['type'] == "Compound Molar Fraction":
self.OM_data_eqn = self.OM_data_eqn + (self.output_stms[1].name + '.x_pc[1,:' +
str(self.compounds.index(self.variables['C_Spec']['comp']) + 1) + '] = ' + str(
self.variables['C_Spec']['value']) + ';\n')
elif self.variables['C_Spec']['type'] == "Compound Molar Flow (mol/s)":
self.OM_data_eqn = self.OM_data_eqn + (self.output_stms[1].name + '.F_pc[1,:' +
str(self.compounds.index(self.variables['C_Spec']['comp']) + 1) + '] = ' + str(
self.variables['C_Spec']['value']) + ';\n')
else:
self.OM_data_eqn = self.OM_data_eqn + (
self.name + '.Condenser.' + self.mode + '=' + str(self.modeVal) + ';\n')
if self.variables['R_Spec']['type'] == "Product Molar Flow (mol/s)":
self.OM_data_eqn = self.OM_data_eqn + (self.output_stms[2].name + '.' + 'F_p[1] = ' + str(
self.variables['R_Spec']['value']) + ';\n')
elif self.variables['R_Spec']['type'] == "Temperature (K)":
self.OM_data_eqn = self.OM_data_eqn + (self.output_stms[2].name + '.' + 'T = ' + str(
self.variables['R_Spec']['value']) + ';\n')
elif self.variables['R_Spec']['type'] == "Compound Molar Fraction":
self.OM_data_eqn = self.OM_data_eqn + (self.output_stms[2].name + '.x_pc[1,:' +
str(self.compounds.index(self.variables['R_Spec']['comp']) + 1) + '] = ' + str(
self.variables['R_Spec']['value']) + ';\n')
elif self.variables['R_Spec']['type'] == "Compound Molar Flow (mol/s)":
self.OM_data_eqn = self.OM_data_eqn + (self.output_stms[2].name + '.F_pc[1,:' +
str(self.compounds.index(self.variables['R_Spec']['comp']) + 1) + '] = ' + str(
self.variables['R_Spec']['value']) + ';\n')
self.OM_data_eqn = self.OM_data_eqn + self.name + '.reboiler.P=' + str(
self.variables['Preb']['value']) + ';\n'
self.OM_data_eqn = self.OM_data_eqn + self.name + '.condenser.P=' + str(
self.variables['Pcond']['value']) + ';\n'
return self.OM_data_eqn
class ConvertionReactor(UnitOperation):
def __init__(self,name='',Nr=None,b=None,X=None,Z=None,a=[],operation=None,Tdef=None):
UnitOperation.__init__(self)
self.name = name
self.type = 'ConvertionReactor'
self.Nr = str(Nr)
self.b = str(b)
self.X = str(X)
self.Z = str(Z)
self.a = json.dumps(a).replace('[','{').replace(']','}')
self.operation = str(operation)
self.Tdef = str(Tdef)
class CompoundSeparator(UnitOperation):
def __init__(self, name='CompoundSeparator'):
UnitOperation.__init__(self)
self.name = name + str(CompoundSeparator.counter)
self.type = 'CompoundSeparator'
self.no_of_inputs = 1
self.no_of_outputs = 2
self.SepFact_modes = ['Molar_Flow (mol/s)', 'Mass_Flow (g/s)', 'Inlet_Molar_Flow_Percent', 'Outlet_Molar_Flow_Percent']
type(self).counter += 1
self.variables = {
'SepStrm' : {'name':'Separation Stream', 'value':1, 'unit':''},
'SepVal_c' : {'name':'Separation Value', 'value':['']*len(self.compounds), 'unit':''},
'SepFact_c' : {'name':'Separaction Factor', 'value':['']*len(self.compounds), 'unit':''},
}
def init_variables(self):
self.variables = {
'SepStrm' : {'name':'Separation Stream', 'value':1, 'unit':''},
'SepVal_c' : {'name':'Separation Value', 'value':['']*len(self.compounds), 'unit':''},
'SepFact_c' : {'name':'Separaction Factor', 'value':['']*len(self.compounds), 'unit':''},
}
def update_compounds(self):
self.compounds = [c[:c.index('(')] for c in compound_selected]
def param_setter(self,params):
print("param_setter CompSep ", params)
if (params[0]):
self.variables['SepStrm']['value'] = 1
else:
self.variables['SepStrm']['value'] = 2
for index, i in enumerate(range(2, len(params))):
if (i %2 != 0):
self.variables['SepVal_c']['value'][index//2] = float(params[i])
else:
self.variables['SepFact_c']['value'][index//2] = params[i]
# self.variables['SepFact_c']['value'] = json.dumps(self.variables['SepFact_c']['value']).replace('[','{').replace(']','}')
# self.variables['SepStrm']['value'] = str(self.variables['SepStrm']['value'])
# self.variables['SepVal_c']['value'] = json.dumps(self.variables['SepVal_c']['value']).replace('[','{').replace(']','}')
def OM_Flowsheet_Initialize(self):
SepStrm = str(self.variables['SepStrm']['value'])
SepFact = []
for i in range(len(self.compounds)):
SepFact.append(self.variables['SepFact_c']['value'][i].split(' ')[0])
SepFact = json.dumps(SepFact).replace('[', '{').replace(']', '}')
self.OM_data_init = ''
comp_count = len(self.compounds)
self.OM_data_init = self.OM_data_init + (
"Simulator.UnitOperations.CompoundSeparator " + self.name + "(Nc = " + str(comp_count))
self.OM_data_init = self.OM_data_init + (", C = {")
comp = str(self.compounds).strip('[').strip(']')
comp = comp.replace("'", "")
self.OM_data_init = self.OM_data_init + comp + ("},")
self.OM_data_init = self.OM_data_init + ("SepFact_c = " + SepFact + ",SepStrm = " + SepStrm + ");\n")
return self.OM_data_init
def OM_Flowsheet_Equation(self):
SepVal = json.dumps(self.variables['SepVal_c']['value']).replace('[','{').replace(']','}')
self.OM_data_eqn = ''
self.OM_data_eqn += ('connect(' + self.name + '.In,' + self.input_stms[1].name + '.Out);\n')
strcount = 1
for strm in self.output_stms.values():
self.OM_data_eqn += ('connect(' + strm.name + '.In,' + self.name + '.Out' + str(strcount) + ');\n')
strcount += 1
self.OM_data_eqn += (self.name + '.SepVal_c ' + '=' + SepVal + ';\n')
return self.OM_data_eqn
class Flash(UnitOperation):
def __init__(self,name='Flash'):
UnitOperation.__init__(self)
self.name = name + str(Flash.counter)
self.type = 'Flash'
self.extra = ['Flash']
self.for_naming = ['Flash']
self.no_of_inputs = 1
self.no_of_outputs = 2
self.count = Flash.counter
self.thermo_pack_req = True
self.parameters = ['BTdef', 'Tdef', 'BPdef', 'Pdef']
type(self).counter += 1
self.variables = {
'thermo_package' : {'name':'Thermo Package', 'value':None, 'unit':''},
'BTdef' : {'name':'Separation Temperature Boolean', 'value':False, 'unit':''},
'BPdef' : {'name':'Separation Pressure Boolean', 'value':False, 'unit':''},
'Tdef' : {'name':'Separation Temperature', 'value':298.15, 'unit':'K'},
'Pdef' : {'name':'Separation Pressure', 'value':101325, 'unit':'Pa'}
}
def update_compounds(self):
self.compounds = [c[:c.index('(')] for c in compound_selected]
def param_setter(self,params):
print("param_setter ", params)
self.variables['thermo_package']['value'] = params[0]
self.variables['BTdef']['value'] = params[1]
self.variables['Tdef']['value'] = params[2]
self.variables['BPdef']['value'] = params[3]
self.variables['Pdef']['value'] = params[4]
def OM_Flowsheet_Equation(self):
self.OM_data_eqn = ''
self.OM_data_eqn += ('connect(' + self.name + '.In,' + self.input_stms[1].name + '.Out);\n')
strcount = 1
for strm in self.output_stms.values():
self.OM_data_eqn += ('connect(' + strm.name + '.In,' + self.name + '.Out' + str(strcount) + ');\n')
strcount += 1
return self.OM_data_eqn
class CentrifugalPump(UnitOperation):
def __init__(self,name='CentrifugalPump'):
UnitOperation.__init__(self)
self.name = name + str(CentrifugalPump.counter)
self.type = 'CentrifugalPump'
self.modes_list = ['Pdel', 'Pout', 'Q'] #"enFlo"
self.parameters = ['Eff']
type(self).counter += 1
self.variables = {
'Eff' : {'name':'Efficiency', 'value':1, 'unit':''},
'Pdel' : {'name':'Pressure Increase', 'value':None, 'unit':'Pa'},
'Pout' : {'name':'Outlet Pressure', 'value':None, 'unit':'Pa'},
'Q' : {'name':'Power Required', 'value':None, 'unit':'W'},
}
class Valve(UnitOperation):
def __init__(self,name='Valve'):
UnitOperation.__init__(self)
self.name = name + str(Valve.counter)
self.type = 'Valve'
self.modes_list = ['Pdel', 'Pout']
type(self).counter += 1
self.variables = {
'Pdel' : {'name':'Pressure Drop', 'value':None, 'unit':'Pa'},
'Pout' : {'name':'Outlet Pressure', 'value':None, 'unit':'Pa'}
}
class Splitter(UnitOperation):
def __init__(self,name='Splitter'):
UnitOperation.__init__(self)
self.name = name + str(Splitter.counter)
self.type = 'Splitter'
self.no_of_outputs = 2
self.CalcType_modes = ['Split_Ratio', 'Molar_Flow', 'Mass_Flow']
self.parameters = ['No', 'CalcType', 'SpecVal_s']
type(self).counter += 1
self.variables = {
'No' : {'name':'No. of Output', 'value':2, 'unit':''},
'CalcType' : {'name':'Calculation Type', 'value':self.CalcType_modes[0], 'unit':''},
'SpecVal_s' : {'name':'Specification Value', 'value':[0.5,0.5], 'unit':''}
}
specval = self.variables['SpecVal_s']['value']
self.specval = json.dumps(specval).replace('[','{').replace(']','}')
def update_compounds(self):
self.compounds = [c[:c.index('(')] for c in compound_selected]
def param_setter(self,params):
print("param_setter ", params)
self.variables['No']['value'] = int(params[0])
self.variables['CalcType']['value'] = params[1]
self.variables['SpecVal_s']['value'] = [float(params[2]), float(params[3])]
if self.variables['CalcType']['value'] == 'Molar_Flow':
self.variables['SpecVal_s']['unit'] = 'mol/s'
elif self.variables['CalcType']['value'] == 'Mass_Flow':
self.variables['SpecVal_s']['unit'] = 'g/s'
else:
self.variables['SpecVal_s']['unit'] = ''
class Mixer(UnitOperation):
def __init__(self,name='Mixer'):
UnitOperation.__init__(self)
self.name = name + str(Mixer.counter)
self.type = 'Mixer'
self.no_of_inputs = 2
self.Pout_modes = ['Inlet_Minimum', 'Inlet_Average', 'Inlet_Maximum']
self.parameters = ['NI', 'outPress']
type(self).counter += 1
self.variables = {
'NI' : {'name':'Number of Input', 'value':6, 'unit':''},
'outPress' : {'name':'Outlet Pressure', 'value':'Inlet_Average', 'unit':''},
}
def update_compounds(self):
self.compounds = [c[:c.index('(')] for c in compound_selected]
def param_setter(self, params):
self.variables['NI']['value'] = int(params[0])
self.variables['outPress']['value'] = params[1]
class Heater(UnitOperation):
def __init__(self, name='Heater'):
UnitOperation.__init__(self)
self.name = name + str(type(self).counter)
self.type = 'Heater'
self.no_of_inputs = 1
self.no_of_outputs = 1
self.modes_list = ['Q','Tout','xvapout','Tdel']
self.parameters = ['Pdel', 'Eff']
self.extra = None
self.for_naming = None
type(self).counter += 1
self.variables = {
'Pdel' : {'name':'Pressure Drop', 'value':0, 'unit':'Pa'},
'Eff' : {'name':'Efficiency', 'value':1, 'unit':''},
'Tout' : {'name':'Outlet Temperature', 'value':298.15, 'unit':'K'},
'Tdel' : {'name':'Temperature Increase', 'value':0, 'unit':'K'},
'Q' : {'name':'Heat Added', 'value':0, 'unit':'W'},
'xvapout': {'name':'Outlet Vapour', 'value':None, 'unit':''}
}
class Cooler(UnitOperation):
def __init__(self, name='Cooler'):
UnitOperation.__init__(self)
self.name = name + str(type(self).counter)
self.type = 'Cooler'
self.no_of_inputs = 1
self.no_of_outputs = 1
self.modes_list = ['Q','Tout','Tdel','xvap']
self.extra = None
self.for_naming = None
self.parameters = ['Pdel', 'Eff']
type(self).counter += 1
self.variables = {
'Pdel' : {'name':'Pressure Drop', 'value':0, 'unit':'Pa'},
'Eff' : {'name':'Efficiency', 'value':1, 'unit':''},
'Tout' : {'name':'Outlet Temperature', 'value':298.15, 'unit':'K'},
'Tdel' : {'name':'Temperature Increase', 'value':0, 'unit':'K'},
'Q' : {'name':'Heat Added', 'value':0, 'unit':'W'},
'xvap' : {'name':'Vapour Phase Mole Fraction', 'value':None, 'unit':'g/s'},
}
class AdiabaticCompressor(UnitOperation):
def __init__(self, name='AdiabaticCompressor'):
UnitOperation.__init__(self)
self.name = name + str(type(self).counter)
self.type = 'AdiabaticCompressor'
self.no_of_inputs = 1
self.no_of_outputs = 1
self.modes_list = ["Pdel","Pout","Q"]
self.extra = ['AdiabaticCompressor']
self.for_naming = ['AdiabaticCompressor']
self.thermo_pack_req = True
self.thermo_package ="RaoultsLaw"
self.parameters = ['Eff']
type(self).counter += 1
self.variables = {
'Pdel' : {'name':'Pressure Increase', 'value':0, 'unit':'Pa'},
'Tdel' : {'name':'Temperature Increase', 'value':0, 'unit':'K'},
'Pout' : {'name':'Outlet Pressure', 'value':101325, 'unit':'Pa'},
'Tout' : {'name':'Outlet Temperature', 'value':298.15, 'unit':'K'},
'Q' : {'name':'Heat Added', 'value':0, 'unit':'W'},
'Eff' : {'name':'Efficiency', 'value':1, 'unit':''}
}
def update_compounds(self):
self.compounds = [c[:c.index('(')] for c in compound_selected]
class AdiabaticExpander(UnitOperation):
def __init__(self, name='AdiabaticExpander'):
UnitOperation.__init__(self)
self.name = name + str(type(self).counter)
self.type = 'AdiabaticExpander'
self.no_of_inputs = 1
self.no_of_outputs = 1
self.modes_list = ["Pdel","Pout","Q"]
self.extra = ['AdiabaticExpander']
self.for_naming = ['AdiabaticExpander']
self.thermo_pack_req = True
self.thermo_package ="RaoultsLaw"
self.parameters = ['Eff']
type(self).counter += 1
self.variables = {
'Pdel' : {'name':'Pressure Drop', 'value':0, 'unit':'Pa'},
'Tdel' : {'name':'Temperature Increase', 'value':0, 'unit':'K'},
'Pout' : {'name':'Outlet Pressure', 'value':101325, 'unit':'Pa'},
'Tout' : {'name':'Outlet Temperature', 'value':298.15, 'unit':'K'},
'Q' : {'name':'Heat Added', 'value':0, 'unit':'W'},
'Eff' : {'name':'Efficiency', 'value':1, 'unit':''}
}
def update_compounds(self):
self.compounds = [c[:c.index('(')] for c in compound_selected]
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