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| author | pravindalve | 2020-11-04 21:16:12 +0530 |
|---|---|---|
| committer | pravindalve | 2020-11-04 21:16:12 +0530 |
| commit | 0a695c879d79b326b901c4e56b78737d165ba849 (patch) | |
| tree | 3f0ca6004849450b5a9f4609bfce4efec6709505 | |
| parent | 9a52d596501a5f75eae84476455bdb1693aef6e4 (diff) | |
| download | Chemical-Simulator-GUI-0a695c879d79b326b901c4e56b78737d165ba849.tar.gz Chemical-Simulator-GUI-0a695c879d79b326b901c4e56b78737d165ba849.tar.bz2 Chemical-Simulator-GUI-0a695c879d79b326b901c4e56b78737d165ba849.zip | |
Units updated
| -rw-r--r-- | Streams.py | 36 | ||||
| -rw-r--r-- | Undo.dat | bin | 3169 -> 3191 bytes | |||
| -rw-r--r-- | UnitOperations.py | 6 |
3 files changed, 21 insertions, 21 deletions
@@ -33,21 +33,21 @@ class MaterialStream(): 'P' : {'name':'Pressure', 'value':101325, 'unit':'Pa'}, 'T' : {'name':'Temperature', 'value':300, 'unit':'K'}, - 'xvap' : {'name':'Vapour Phase Mole Fraction', 'value':None, 'unit':'g/s'}, - 'H_p[1]' : {'name':'Mixture Phase Molar Entalpy', 'value':None, 'unit':'g/s'}, - 'S_p[1]' : {'name':'Mixture Phase Molar Entropy', 'value':None, 'unit':'g/s'}, - 'F_p[1]' : {'name':'Mixture Molar Flow Rate', 'value':100, 'unit':'g/s'}, + 'xvap' : {'name':'Vapour Phase Mole Fraction', 'value':None, 'unit':''}, + 'H_p[1]' : {'name':'Mixture Phase Molar Entalpy', 'value':None, 'unit':'J/mol'}, + 'S_p[1]' : {'name':'Mixture Phase Molar Entropy', 'value':None, 'unit':'J/mol.K'}, + 'F_p[1]' : {'name':'Mixture Molar Flow Rate', 'value':100, 'unit':'mol/s'}, - 'H_p[2]' : {'name':'Liquid Phase Molar Entalpy', 'value':None, 'unit':'g/s'}, - 'S_p[2]' : {'name':'Liquid Phase Molar Entropy', 'value':None, 'unit':'g/s'}, - 'F_p[2]' : {'name':'Liquid Molar Flow Rate', 'value':None, 'unit':'g/s'}, + 'H_p[2]' : {'name':'Liquid Phase Molar Entalpy', 'value':None, 'unit':'J/mol'}, + 'S_p[2]' : {'name':'Liquid Phase Molar Entropy', 'value':None, 'unit':'J/mol.K'}, + 'F_p[2]' : {'name':'Liquid Molar Flow Rate', 'value':None, 'unit':'mol/s'}, - 'H_p[3]' : {'name':'Vapour Phase Molar Entalpy', 'value':None, 'unit':'g/s'}, - 'S_p[3]' : {'name':'Vapour Phase Molar Entropy', 'value':None, 'unit':'g/s'}, - 'F_p[3]' : {'name':'Vapour Molar Flow Rate', 'value':None, 'unit':'g/s'}, + 'H_p[3]' : {'name':'Vapour Phase Molar Entalpy', 'value':None, 'unit':'J/mol'}, + 'S_p[3]' : {'name':'Vapour Phase Molar Entropy', 'value':None, 'unit':'J/mol.K'}, + 'F_p[3]' : {'name':'Vapour Molar Flow Rate', 'value':None, 'unit':'mol/s'}, - 'x_pc' : {'name':'Mole Fraction', 'value':[], 'unit':'mol/s'}, - 'xm_pc' : {'name':'Mass Fraction', 'value':None, 'unit':'g/s'}, + 'x_pc' : {'name':'Mole Fraction', 'value':[], 'unit':''}, + 'xm_pc' : {'name':'Mass Fraction', 'value':None, 'unit':''}, 'F_pc' : {'name':'Mole Flow', 'value':100, 'unit':'mol/s'}, 'Fm_pc' : {'name':'Mass Flow', 'value':None, 'unit':'g/s'}, @@ -57,18 +57,18 @@ class MaterialStream(): def init_variables(self): Nc = len(self.compound_names) for i, val in enumerate(self.compound_names): - self.variables['x_pc[1,'+ str(i+1)+']'] = {'name':val + ' Mixture Mole Fraction', 'value':round(1/Nc,4), 'unit':'mol/s'} - self.variables['xm_pc[1,'+ str(i+1)+']'] = {'name':val + ' Mixture Mass Fraction', 'value':None, 'unit':'g/s'} + self.variables['x_pc[1,'+ str(i+1)+']'] = {'name':val + ' Mixture Mole Fraction', 'value':round(1/Nc,4), 'unit':''} + self.variables['xm_pc[1,'+ str(i+1)+']'] = {'name':val + ' Mixture Mass Fraction', 'value':None, 'unit':''} self.variables['F_pc[1,'+ str(i+1)+']'] = {'name':val + ' Mixture Mole Flow', 'value':None, 'unit':'mol/s'} self.variables['Fm_pc[1,'+ str(i+1)+']'] = {'name':val + ' Mixture Mass Flow', 'value':None, 'unit':'g/s'} - self.variables['x_pc[2,'+ str(i+1)+']'] = {'name':[val + ' Liquid Mole Fraction'], 'value':None, 'unit':'mol/s'} - self.variables['xm_pc[2,'+ str(i+1)+']'] = {'name':[val + ' Liquid Mass Fraction'], 'value':None, 'unit':'g/s'} + self.variables['x_pc[2,'+ str(i+1)+']'] = {'name':[val + ' Liquid Mole Fraction'], 'value':None, 'unit':''} + self.variables['xm_pc[2,'+ str(i+1)+']'] = {'name':[val + ' Liquid Mass Fraction'], 'value':None, 'unit':''} self.variables['F_pc[2,'+ str(i+1)+']'] = {'name':[val + ' Liquid Mole Flow'], 'value':None, 'unit':'mol/s'} self.variables['Fm_pc[2,'+ str(i+1)+']'] = {'name':[val + ' Liquid Mass Flow'], 'value':None, 'unit':'g/s'} - self.variables['x_pc[3,'+ str(i+1)+']'] = {'name':[val + ' Vapour Mole Fraction'], 'value':None, 'unit':'mol/s'} - self.variables['xm_pc[3,'+ str(i+1)+']'] = {'name':[val + ' Vapour Mass Fraction'], 'value':None, 'unit':'g/s'} + self.variables['x_pc[3,'+ str(i+1)+']'] = {'name':[val + ' Vapour Mole Fraction'], 'value':None, 'unit':''} + self.variables['xm_pc[3,'+ str(i+1)+']'] = {'name':[val + ' Vapour Mass Fraction'], 'value':None, 'unit':''} self.variables['F_pc[3,'+ str(i+1)+']'] = {'name':[val + ' Vapour Mole Flow'], 'value':None, 'unit':'mol/s'} self.variables['Fm_pc[3,'+ str(i+1)+']'] = {'name':[val + ' Vapour Mass Flow'], 'value':None, 'unit':'g/s'} diff --git a/UnitOperations.py b/UnitOperations.py index 5c53f59..410cdd1 100644 --- a/UnitOperations.py +++ b/UnitOperations.py @@ -178,8 +178,8 @@ class ShortcutColumn(UnitOperation): self.variables = { 'HKey' : {'name':'Heavy Key', 'value':None, 'unit':''}, 'LKey' : {'name':'Light Key', 'value':None, 'unit':''}, - 'HKey_x_pc' : {'name':'Heavy Key Mole Fraction', 'value':0.01, 'unit':'mol/s'}, - 'LKey_x_pc' : {'name':'Light Key Mole Fraction', 'value':0.01, 'unit':'mol/s'}, + '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':'Condensor Type', 'value':None, 'unit':''}, 'thermo_package' : {'name':'Thermo Package', 'value':'Raoults_Law', 'unit':''}, 'Pcond' : {'name':'Condensor Pressure', 'value':101325, 'unit':'Pa'}, @@ -306,7 +306,7 @@ class CompoundSeparator(UnitOperation): self.no_of_inputs = 1 self.no_of_outputs = 2 - self.SepFact_modes = ['Molar_Flow (mol/s)', 'Mass_Flow (kg/s)', 'Inlet_Molar_Flow_Percent', 'Outlet_Molar_Flow_Percent'] + 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 = { |