| 1 |
REQUIRE "simpleUnits.AWW.a4c"; |
| 2 |
REQUIRE "atoms.AWW.a4c"; |
| 3 |
|
| 4 |
MODEL H2basis; |
| 5 |
|
| 6 |
tmf IS_A traceMoleFraction_constant; |
| 7 |
comps IS_A set OF symbol_constant; |
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comps :== ['hydrogen','methane','ethane','oxygen','carbon_dioxide','water']; |
| 9 |
cdComps IS_A components_data(comps, 'water'); |
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pdV IS_A phases_data('V','Pitzer_vapor_mixture','none','none'); |
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equil IS_A boolean; |
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|
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Qin IS_A energy_rate; |
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feed IS_A stream(cdComps, pdV, equil); |
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product IS_A stream(cdComps, pdV, equil); |
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react IS_A unitOneInOneOut(Qin, feed, product); |
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|
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METHODS |
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|
| 20 |
METHOD default_self; |
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RUN react.default_self; |
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END default_self; |
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|
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METHOD values; |
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equil := TRUE; |
| 26 |
feed.T := 298 {K}; |
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feed.P := 1.0 {atm}; |
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feed.f[comps] := tmf*1.0 {mol/h}; |
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react.stoichCoef[comps] := 0.0; |
| 30 |
react.turnover := 1.0 {mol/h}; |
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END values; |
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|
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METHOD valuesH2Combustion; |
| 34 |
(* H2 + 0.5O2 = H20 *) |
| 35 |
RUN values; |
| 36 |
feed.f['hydrogen'] := 1.0 {mol/h}; |
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feed.f['oxygen'] := 0.5 {mol/h}; |
| 38 |
react.stoichCoef['hydrogen'] := -1.0; |
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react.stoichCoef['oxygen'] := -0.5; |
| 40 |
react.stoichCoef['water'] := 1.0; |
| 41 |
END valuesH2Combustion; |
| 42 |
|
| 43 |
METHOD valuesCH4Combustion; |
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(* CH4 + 2O2 = C02 + 2H2O *) |
| 45 |
RUN values; |
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feed.f['methane'] := 1.0 {mol/h}; |
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feed.f['oxygen'] := 2.0 {mol/h}; |
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react.stoichCoef['methane'] := -1.0; |
| 49 |
react.stoichCoef['oxygen'] := -2.0; |
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react.stoichCoef['carbon_dioxide'] := 1.0; |
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react.stoichCoef['water'] := 2.0; |
| 52 |
END valuesCH4Combustion; |
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|
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METHOD specify; |
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RUN react.specify; |
| 56 |
FREE react.Qin; |
| 57 |
FIX react.delT; |
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END specify; |
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|
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END H2basis; |
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