[83] | 1 | #*------------------------------------------------------------------- |
---|
| 2 | * EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC. |
---|
| 3 | * |
---|
| 4 | * This LIBRARY is free software; you can distribute it and/or modify |
---|
| 5 | * it under the therms of the ALSOC FREE LICENSE as available at |
---|
| 6 | * http://www.enq.ufrgs.br/alsoc. |
---|
| 7 | * |
---|
| 8 | * EMSO Copyright (C) 2004 - 2007 ALSOC, original code |
---|
| 9 | * from http://www.rps.eng.br Copyright (C) 2002-2004. |
---|
| 10 | * All rights reserved. |
---|
| 11 | * |
---|
| 12 | * EMSO is distributed under the therms of the ALSOC LICENSE as |
---|
| 13 | * available at http://www.enq.ufrgs.br/alsoc. |
---|
| 14 | * |
---|
| 15 | *-------------------------------------------------------------------- |
---|
| 16 | * Description of a flowsheet with only one cell based on the model |
---|
| 17 | * galvanic.model. |
---|
| 18 | * |
---|
| 19 | * Model of a falvanostatic charge/open-circuit/discharge process |
---|
| 20 | * Proposed by Wu and White, 2001 |
---|
| 21 | * This example is use to analize the convergence range of the |
---|
| 22 | * initialization algorithm. |
---|
| 23 | * |
---|
| 24 | *---------------------------------------------------------------------- |
---|
| 25 | * Author: Rafael de Pelegrini Soares |
---|
| 26 | * $Id: sample_galvanic.mso 574 2008-07-25 14:18:50Z rafael $ |
---|
| 27 | *--------------------------------------------------------------------*# |
---|
[1] | 28 | |
---|
[574] | 29 | using "types"; |
---|
[1] | 30 | |
---|
| 31 | FlowSheet cell |
---|
| 32 | |
---|
| 33 | PARAMETERS |
---|
| 34 | |
---|
| 35 | iapp; |
---|
| 36 | F as Real(Brief="Faraday constant"); |
---|
| 37 | R as Real(Brief="Ideal Gas constant"); |
---|
| 38 | T as Real(Brief="Temperature"); |
---|
| 39 | |
---|
| 40 | pho; W; V; phi1; phi2; i01; i02; |
---|
| 41 | |
---|
| 42 | |
---|
| 43 | VARIABLES |
---|
| 44 | |
---|
[218] | 45 | y1 as Real(Default=0.5, Brief="Mole fraction of NiOOH"); |
---|
| 46 | y2 as Real(Default=0.5, Brief="Potential difference at the solid-liquid interface"); |
---|
[1] | 47 | |
---|
| 48 | |
---|
| 49 | EQUATIONS |
---|
| 50 | |
---|
| 51 | #pho*V/W*$(y1) = j1/F; |
---|
| 52 | |
---|
| 53 | "Equation 1(a)" |
---|
[218] | 54 | pho*V/W*diff(y1)*'s' = i01*(2*(1-y1)*exp(0.5*F/(R*T)*(y2-phi1))-2*y1*exp(-0.5*F/(R*T)*(y2-phi1)))/F; |
---|
[1] | 55 | |
---|
| 56 | "Equation 1(b)" |
---|
| 57 | i01*(2*(1-y1)*exp(0.5*F/(R*T)*(y2-phi1))-2*y1*exp(-0.5*F/(R*T)*(y2-phi1))) |
---|
| 58 | + i02*(exp(F/(R*T)*(y2-phi2))-exp(-F/(R*T)*(y2-phi2))) = iapp; |
---|
| 59 | |
---|
| 60 | |
---|
[535] | 61 | #j1+j2 = iapp; |
---|
[1] | 62 | #j1 = i01*(2*(1-y1)*exp(0.5*F/R/T*(y2-phi1))-2*y1*exp(-0.5*F/R/T*(y2-phi1))); |
---|
| 63 | #j2 = i02*(exp(F/R/T*(y2-phi2))-exp(-F/R/T*(y2-phi2))); |
---|
| 64 | |
---|
[535] | 65 | #convergence limits |
---|
[1] | 66 | # -inf < y1 < inf |
---|
| 67 | # -2.70< y2 < 2.66 |
---|
| 68 | |
---|
| 69 | |
---|
| 70 | SET |
---|
| 71 | |
---|
| 72 | F = 96487; |
---|
| 73 | R = 8.314; |
---|
| 74 | T = 298.15; |
---|
| 75 | pho= 3.4; |
---|
| 76 | W = 92.7; |
---|
| 77 | V = 1e-5; |
---|
| 78 | phi1 = 0.420; |
---|
| 79 | phi2 = 0.303; |
---|
| 80 | i01 = 1e-4; |
---|
| 81 | i02 = 1e-10; |
---|
| 82 | iapp = 1e-5; |
---|
| 83 | |
---|
| 84 | INITIAL |
---|
| 85 | #Parameters used for the initial conditions |
---|
| 86 | #y1 = 0.05; |
---|
| 87 | y2 = 0.38; |
---|
| 88 | |
---|
| 89 | |
---|
| 90 | OPTIONS |
---|
[182] | 91 | TimeStep = 100; |
---|
| 92 | TimeEnd = 4000; |
---|
[1] | 93 | end |
---|