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author | brenda-br | 2023-01-30 23:57:17 +0530 |
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committer | brenda-br | 2023-01-30 23:57:17 +0530 |
commit | 60f3a5a1d15274d43d2a929922b5f001fe7d9e51 (patch) | |
tree | cc5f368597f8546c44474050cad4422dcbb7add0 /Streams.py | |
parent | a9e09576c8e977e9fc838fabf2116d5e2cae9e7e (diff) | |
download | Chemical-Simulator-GUI-60f3a5a1d15274d43d2a929922b5f001fe7d9e51.tar.gz Chemical-Simulator-GUI-60f3a5a1d15274d43d2a929922b5f001fe7d9e51.tar.bz2 Chemical-Simulator-GUI-60f3a5a1d15274d43d2a929922b5f001fe7d9e51.zip |
Fix #50 Mixture Mass Flow Value added to phase properties tab in result
Diffstat (limited to 'Streams.py')
-rw-r--r-- | Streams.py | 72 |
1 files changed, 41 insertions, 31 deletions
@@ -35,19 +35,20 @@ class MaterialStream(): self.variables = { 'P' : {'name':'Pressure', 'value':101325, 'unit':'Pa'}, 'T' : {'name':'Temperature', 'value':300, 'unit':'K'}, + + 'xvap' : {'name':'Vapour Mole Fraction', 'value':None, 'unit':''}, + 'H_p[1]' : {'name':'Mixture Molar Entalpy', 'value':None, 'unit':'J/mol'}, + 'S_p[1]' : {'name':'Mixture Molar Entropy', 'value':None, 'unit':'J/mol.K'}, + 'F_p[1]' : {'name':'Mixture Molar Flow', 'value':100, 'unit':'mol/s'}, + 'Fm_p[1]' : {'name':'Mixture Mass Flow', 'value':None, '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':'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[2]' : {'name':'Liquid Molar Entalpy', 'value':None, 'unit':'J/mol'}, + 'S_p[2]' : {'name':'Liquid Molar Entropy', 'value':None, 'unit':'J/mol.K'}, + 'F_p[2]' : {'name':'Liquid Molar Flow', 'value':None, 'unit':'mol/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'}, + 'H_p[3]' : {'name':'Vapour Molar Entalpy', 'value':None, 'unit':'J/mol'}, + 'S_p[3]' : {'name':'Vapour Molar Entropy', 'value':None, 'unit':'J/mol.K'}, + 'F_p[3]' : {'name':'Vapour Molar Flow', 'value':None, 'unit':'mol/s'}, 'x_pc' : {'name':'Mole Fraction', 'value':[], 'unit':''}, 'xm_pc' : {'name':'Mass Fraction', 'value':None, 'unit':''}, @@ -140,26 +141,35 @@ class MaterialStream(): def param_getter_tooltip_selectedVar(self): dict = {} - var1_name = self.variables['P']['name'] - var1_val = self.variables['P']['value'] - var1_unit = self.variables['P']['unit'] - var2_name = self.variables['T']['name'] - var2_val = self.variables['T']['value'] - var2_unit = self.variables['T']['unit'] - var3_name = self.variables['H_p[1]']['name'] - var3_val = self.variables['H_p[1]']['value'] - var3_unit = self.variables['H_p[1]']['unit'] - var4_name = self.variables['S_p[1]']['name'] - var4_val = self.variables['S_p[1]']['value'] - var4_unit = self.variables['S_p[1]']['unit'] - var5_name = self.variables['xvap']['name'] - var5_val = self.variables['xvap']['value'] - var5_unit = self.variables['xvap']['unit'] - dict = {var1_name:str(var1_val)+' '+var1_unit, - var2_name:str(var2_val)+' '+var2_unit, - var3_name:str(var3_val)+' '+var3_unit, - var4_name:str(var4_val)+' '+var4_unit, - var5_name:str(var5_val)+' '+var5_unit, } + pressure_name = self.variables['P']['name'] + pressure_val = self.variables['P']['value'] + pressure_unit = self.variables['P']['unit'] + temp_name = self.variables['T']['name'] + temp_val = self.variables['T']['value'] + temp_unit = self.variables['T']['unit'] + mixMolEntal_name = self.variables['H_p[1]']['name'] + mixMolEntal_val = round(float(self.variables['H_p[1]']['value']),2) + mixMolEntal_unit = self.variables['H_p[1]']['unit'] + mixMolEntro_name = self.variables['S_p[1]']['name'] + mixMolEntro_val = round(float(self.variables['S_p[1]']['value']),2) + mixMolEntro_unit = self.variables['S_p[1]']['unit'] + vapMolFrac_name = self.variables['xvap']['name'] + vapMolFrac_val = self.variables['xvap']['value'] + vapMolFrac_unit = self.variables['xvap']['unit'] + mixMolFlo_name = self.variables['F_pc']['name'] + mixMolFlo_val = self.variables['F_pc']['value'] + mixMolFlo_unit = self.variables['F_pc']['unit'] + mixMassFlo_name = self.variables['Fm_p[1]']['name'] + mixMassFlo_val = self.variables['Fm_p[1]']['value'] + mixMassFlo_unit = self.variables['Fm_p[1]']['unit'] + + dict = {pressure_name:str(pressure_val)+' '+pressure_unit, + temp_name:str(temp_val)+' '+temp_unit, + vapMolFrac_name:str(vapMolFrac_val)+' '+vapMolFrac_unit, + mixMolEntal_name:str(mixMolEntal_val)+' '+mixMolEntal_unit, + mixMolEntro_name:str(mixMolEntro_val)+' '+mixMolEntro_unit, + mixMolFlo_name:str(mixMolFlo_val)+' '+mixMolFlo_unit, + mixMassFlo_name:str(mixMassFlo_val)+' '+mixMassFlo_unit} return dict def param_getter(self,mode): |