Design og modellering af metanolanlæg til VEnzin-visionen Bilag

VEnzin.for
c:/dna/source/
C***********************************************************************
SUBROUTINE ELECTROLYSER(KOMTY,ANTLK,ANTEX,ANTKN,ANTPK,ANTM1,MEDIE
$ ,ANTME,VARME,antel,varel,MDOT,P,H,Q,E,PAR,RES,X_J,KOMDSC
$ ,K_PAR,K_lig,K_bet,KMEDDS,K_inp,ZA,ZANAM)
C***********************************************************************
C
C ELYSE is a component that converts water to H2 and O2 by
C elektrolysis. The component uses water (ideal gas) and not STEAM
C (real fluid). The efficiency and the temperature are parameters to
C the component.
C
C***********************************************************************
C
CA FKOMP − INPUT − Flag with the value:
CA 1: Initialize the component.
CA 2: Initialize with actual system.
CA 3: Fluid composition calculation (constant).
CA 4: Find residuals.
CA 5: Find residuals and check variables.
CA 6: Output information about component.
CA MDOT − INPUT − Massflows from nodes.
CA P − INPUT − Pressure in nodes.
CA H − INPUT − Enthalpy of massflows.
CA Q − INPUT − Exchanged heat.
CA E − INPUT − Power.
CA PAR − INPUT − Parameters of the component.
CA X_J − INPUT − Fluid composition.
CA KOMTY − OUTPUT − Component name.
CA ANTPK − OUTPUT − Number of parameters for the component.
CA ANTLK − OUTPUT − Number of equations in the component.
CA ANTEX − OUTPUT − Number of independent equations in the component.
CA ANTED − OUTPUT − Number of differential independent equations.
CA ANTKN − OUTPUT − Number of nodes connected to the component.
CA ANTM1 − OUTPUT − Number of massflows in the first conservation of
CA mass equation.
CA ANTM2 − OUTPUT − Number of massflows in the second.
CA DYCOM − OUTPUT − Type of conservation equations (static or dynamic
CA mass and internal energy on side 1 and 2 respectively;
CA and dynamic solid internal energy).
CA MEDIE − IN/OUT − Media (fluid) of the connected nodes.
CA The values mean :
CA 1 : Air.
CA 27 : Oxygen rich gas.
CA 28 : Nitrogen rich gas.
CA 200 : Power.
CA 300 : Heat.
CA ANTME − OUTPUT − Number of fluids with variable composition.
CA RES − OUTPUT − Residuals for the component.
C
CL S Entropy.
CL V Specific volume.
CL T2 Temperature in node 2.
CL T3 Temperature in node 3.
CL X Quality.
CL U Internal energy.
CL DELP Pressure drop through the plant.
CL PRO Oxygen mole ratio in oxygen rich gas.
CL MNOM Nominal mass flow through the plant.
CL ENOM Nominal power consumption of the plant.
CL M1 Mass flow into the separation plant.
CL M2 Mass flow found using PRO.
CL K_PAR Parameter description.
CL K_LIG Equation description.
CL K_BET Condition description.
CL K_MED Media description.
C
C Subroutines : COMINF
C STATES
C SPLIT
C
CP Programmer : Bent Lorentzen 1994 (Niels Emsholm 1991)
CP Lab. for Energetics, DTH, Denmark.
C***********************************************************************
C
C Including the common "environment"
C
INCLUDE ’ENVIRO.INI’
INCLUDE ’THERPROP.DEC’
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19−03−2007