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author | brenda-br | 2023-03-04 11:32:15 +0530 |
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committer | brenda-br | 2023-03-04 11:32:15 +0530 |
commit | 3cbdd4238867bc860282f7cf702d73b5be6e3f86 (patch) | |
tree | 7a9323daf6923801a61bb10b5aa35ad4795c52b1 /UnitOperations.py | |
parent | 7cf8eca28f9ca77e6195aa43e3bd9ae319518b66 (diff) | |
download | Chemical-Simulator-GUI-3cbdd4238867bc860282f7cf702d73b5be6e3f86.tar.gz Chemical-Simulator-GUI-3cbdd4238867bc860282f7cf702d73b5be6e3f86.tar.bz2 Chemical-Simulator-GUI-3cbdd4238867bc860282f7cf702d73b5be6e3f86.zip |
Revert "Restructuring Finalized for App Bundling"
This reverts commit 7af3526e105cc330422f8742ec5edec1c4a0a98f.
Diffstat (limited to 'UnitOperations.py')
-rw-r--r-- | UnitOperations.py | 733 |
1 files changed, 0 insertions, 733 deletions
diff --git a/UnitOperations.py b/UnitOperations.py deleted file mode 100644 index bb1c1c2..0000000 --- a/UnitOperations.py +++ /dev/null @@ -1,733 +0,0 @@ -import os,sys -import json - -from OMChem.Flowsheet import Flowsheet -from OMChem.EngStm import EngStm -from ComponentSelector import * -from 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 = [] - self.parameters = ['Nt', 'Ni', 'Ctype', 'Pcond', 'condmode', 'C_comp', 'C_Spec', 'Preb', 'rebmode', 'rebcomp', 'R_Spec'] - 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') - return self.OM_data_init - - def OM_Flowsheet_Equation(self): - self.OM_data_eqn = '' - 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] - - 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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