Gas conserving port

Port_B = Gas;  

Option to select the thermodynamic model (Equation of State)

model = ThermodynamicModel.IdealGas;     % Thermodynamic Model

Ideal Gas | Real Gas (Peng-Robinson EoS)

Number of Species

N  = {2,'1'};   

Species Identifier

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

Molar Weights

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

Diffusion Volumes after Fuller et al.(Robert C. Reid and John M. Prausnitz and Thomas K. Sherwood, 1977).

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

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)'};  

Critical Pressures

pc = {ones(2,1),'bar'}; 

The data are only required if model is set to Real Gas (Peng-Robinson EoS).

Critical Temperatures

Tc = {298.15*ones(2,1),'K'};          

The data are only required if model is set to Real Gas (Peng-Robinson EoS).

Acentric Factors

omega = {ones(2,1),'1'};

The data are only required if model is set to Real Gas (Peng-Robinson EoS).

Binary Interaction Coefficients

k0 = {zeros(2,2),'1'};       

The data are only required if model is set to Real Gas (Peng-Robinson EoS).

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'};

Nominal Value for Departure Enthalpy

Hres_nom = {1,'kJ/mol'};