1 | #*--------------------------------------------------------------------- |
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2 | * This file is property of the author and cannot be used, copyed |
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3 | * or modified without permission. |
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4 | * |
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5 | * Copyright (C) 2004 the author |
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6 | *---------------------------------------------------------------------- |
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7 | * Author: Rafael de P. Soares |
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8 | * Paula B. Staudt |
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9 | * $Id: cstr.mso 1 2006-06-20 17:33:53Z rafael $ |
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10 | *--------------------------------------------------------------------*# |
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11 | |
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12 | using "streams"; |
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13 | |
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14 | #* |
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15 | * Generic PFR model |
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16 | * |
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17 | * Requires the information of: |
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18 | * - Reaction values |
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19 | * - Heat of reaction |
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20 | * - Pressure profile |
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21 | *# |
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22 | Model pfr |
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23 | PARAMETERS |
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24 | ext PP as CalcObject (Brief = "External Physical Properties"); |
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25 | ext NComp as Integer(Brief="Number of components"); |
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26 | NReac as Integer(Brief="Number of reactions"); |
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27 | stoic(NComp, NReac) as Real (Brief = "Stoichiometric Matrix"); |
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28 | NDisc as Integer(Brief="Number of points of discretization", Default=10); |
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29 | Mw(NComp) as molweight (Brief="Component Mol Weight"); |
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30 | |
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31 | L as length(Brief="Reactor Length"); |
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32 | Across as area(Brief="Cross section area"); |
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33 | |
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34 | SET |
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35 | Mw = PP.MolecularWeight(); |
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36 | |
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37 | VARIABLES |
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38 | in Inlet as stream; |
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39 | out Outlet as stream; |
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40 | str(NDisc+1) as stream_therm; |
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41 | vel(NDisc+1) as velocity; |
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42 | vol(NDisc+1) as vol_mol; |
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43 | rho(NDisc+1) as dens_mass; |
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44 | |
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45 | q(NDisc) as heat_rate; |
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46 | M(NComp, NDisc) as mol (Brief = "Molar holdup"); |
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47 | C(NComp, NDisc) as conc_mol(Brief="Components concentration"); |
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48 | E(NDisc) as energy (Brief="Total Energy Holdup on element"); |
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49 | |
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50 | r(NReac, NDisc) as reaction_mol; |
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51 | Hr(NReac, NDisc) as heat_reaction; |
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52 | |
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53 | EQUATIONS |
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54 | "Vapourisation Fraction" |
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55 | str.v = Inlet.v; |
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56 | |
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57 | "Inlet boundary" |
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58 | str(1).F = Inlet.F; |
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59 | str(1).T = Inlet.T; |
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60 | str(1).P = Inlet.P; |
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61 | str(1).z = Inlet.z; |
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62 | |
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63 | "Outlet boundary" |
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64 | Outlet.F = str(NDisc+1).F; |
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65 | Outlet.T = str(NDisc+1).T; |
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66 | Outlet.P = str(NDisc+1).P; |
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67 | Outlet.z = str(NDisc+1).z; |
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68 | Outlet.h = str(NDisc+1).h; |
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69 | Outlet.v = str(NDisc+1).v; |
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70 | |
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71 | for z in [1:NDisc] |
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72 | for c in [1:NComp] |
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73 | "Component Molar Balance" |
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74 | diff(M(c,z)) = (str(z).F*str(z).z(c) - str(z+1).F*str(z+1).z(c)) |
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75 | + sum(stoic(c,:)*r(:, z)) * Across*L/NDisc; |
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76 | end |
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77 | |
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78 | "Energy Balance" |
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79 | diff(E(z)) = str(z).F*str(z).h - str(z+1).F*str(z+1).h + |
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80 | sum(Hr(:,z)*r(:,z)) * Across*L/NDisc - q(z); |
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81 | |
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82 | "Energy Holdup" |
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83 | E(z) = sum(M(:,z))*str(z+1).h - str(z+1).P*Across*L/NDisc; |
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84 | |
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85 | "Volume flow is considered constant" |
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86 | str(z+1).F*vol(z+1) = str(z).F*vol(z); # FIXME: is this correct? |
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87 | |
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88 | "Molar concentration" |
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89 | C(:,z) * Across*L/NDisc = M(:,z); |
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90 | "Molar fraction" |
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91 | str(z+1).z = C(:,z) * vol(z); # FIXME: is this correct? |
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92 | end |
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93 | |
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94 | for z in [1:NDisc+1] |
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95 | "Specific Volume" |
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96 | vol(z) = PP.VapourVolume(str(z).T, str(z).P, str(z).z); |
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97 | "Specific Mass" |
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98 | rho(z) = sum(str(z).z*Mw)/vol(z); |
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99 | |
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100 | "Velocity" |
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101 | vel(z)*Across = str(z).F*vol(z); |
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102 | end |
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103 | end |
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