Liquid conserving port

Port_B = Liquid;  

Option to select the thermodynamic model (activity model).

model = ThermodynamicModel.IdealLiquid;     % Thermodynamic Model

Ideal Liquid | Real Liquid (NRTL)

Number of Species

N  = {2,'1'};   

Species Identifier

Ids = {[1;2],'1'};

Molar Weights

Mw = {zeros(N,1),'g/mol'};                

Temperature Table

table_T = {[200,400],'K'}; 

with nT als the number of entries of array table_T. For details see Domain.

Specific Heats Table

table_cp = {zeros(nT,N),'J/(mol*K)'};      

Enthalpy Table

table_H  = {zeros(nT,N),'kJ/mol'};        

Gibbs Energy Table

table_G = {zeros(nT,N),'kJ/mol'};    

Dynamic Viscosity Table

table_mu = {zeros(nT,N),'Pa*s'};          

Heat Conductivity Table

table_lambda  = {zeros(nT,N),'W/(m*K)'};  

Molar Volume Table

table_Vm = {zeros(nT,N),'l/mol'};         

Heat of Vaporization Table

table_Hv = {zeros(nT,N),'kJ/mol'};        

Vaporization Pressure Table

table_pvap = {zeros(nT,N),'bar'};  

Binary Interaction Parameters

A = {eye(N,N),'cal/mol'}; 

The data are only required if model is set to Real Liquid (NRTL).

NRTL Interaction Parameter alpha

alpha = {zeros(N,N),'1'};

The data are only required if model is set to Real Liquid (NRTL).

Nominal Value for Molar Flow Rates

F_nom = {1.0e-06,'mol/s'};

Nominal Value for Energy Flow Rate

Phi_nom = {1.0,'W'};

Nominal Value for Molar Enthalpies

H_nom = {1.0e+02,'kJ/mol'};