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Perspektiver for dansk ammoniak- eller methanolfremstilling, som ...

Perspektiver for dansk ammoniak- eller methanolfremstilling, som ...

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PSO 2005-2 6422<br />

Shift reaktor Ammoniak reaktor<br />

Tryk Bar 39 Tryk Bar 190<br />

Temp C 229 Temp C 460<br />

VMG-Sim Ind [mol%] Ud [mol%] VMG-Sim Ind [mol%] Ud [mol%]<br />

CH4 0.004 0.004 CH4 0.082 0.0942<br />

CO2 0.049 0.138 CO2 0.000 0.0000<br />

CO 0.091 0.002 CO 0.000 0.0000<br />

Ar 0.002 0.002 Ar 0.029 0.0332<br />

H2 0.365 0.454 H2 0.612 0.4802<br />

N2 0.158 0.158 N2 0.235 0.1960<br />

H2O 0.331 0.242 H2O 0.000 0.0000<br />

NH3 0.042 0.1964<br />

Sum 1.000 1.000 Sum 1.000 1.0000<br />

Plant data (M. Appl) Plant data (M. Appl)<br />

CH4 0.004 0.004 CH4 0.082 0.0915<br />

CO2 0.049 0.138 CO2 0.000 0.0000<br />

CO 0.091 0.003 CO 0.000 0.0000<br />

Ar 0.002 0.002 Ar 0.029 0.0323<br />

H2 0.365 0.456 H2 0.612 0.5079<br />

N2 0.158 0.159 N2 0.235 0.2043<br />

H2O 0.331 0.238 H2O 0.000 0.0000<br />

NH3 0.042 0.1640<br />

Sum 1.000 1.000 Sum 1.000 1.0000<br />

Tabel 12. Simulering med ligevægtsbetingelser sammenlignet med M. Appl, ref. 28. Tal<br />

fra M. Appl svarer til en approachtemperatur på cirka 15 C i <strong>ammoniak</strong>reaktoren.<br />

Ammonia production HHV LHV<br />

Ammonia specific heating value 22.54 18.60 MJ/kg<br />

Ammonia heating value 103.4 85.4 MW<br />

Biomass input 226.3 200 MW<br />

Power consumption:<br />

O2_compressor 2.4<br />

Air_separation 5.5<br />

Feed gas compression 8.9<br />

Recyle compre 0.3<br />

CO2_absorption pump 0.7<br />

Ammonia Cooler 0.6<br />

Boiler _feedPump 0.6<br />

Auxilary 0.9<br />

Biomasse crushing (torrefied) 2.0<br />

Total power consumption 21.9 MW<br />

Power production: Simple GT+District heat Simple GT<br />

Gasturbine 14.5 14.5<br />

Steam turbines: High pressure 12.4 12.4<br />

Medium pressure 7.5 7.5<br />

Low pressure 6.2 12.3<br />

Efficiency gear+genset 96% 96%<br />

Total power production 39.0 MW 44.9 MW<br />

Net power 17.1 MW 22.9 MW<br />

District heat 70.2 MW 0 MW<br />

HHV LHV HHV LHV<br />

Total useful products [MW] 190.7 172.6 126.4 108.3<br />

Efficiencies:<br />

NH3/Biomass input 0.457 0.427 0.457 0.427<br />

(NH3+power)/Biomass input 0.533 0.512 0.558 0.541<br />

(NH3+power+District heat)//Biomass input 0.843 0.863 0.558 0.541<br />

(NH3+power/0.45+District heat)/Biomass input 0.935 0.968 0.682 0.682<br />

Tabel 13. Energi<strong>for</strong>deling på elproduktion, el<strong>for</strong>brug, fjernvarme og <strong>ammoniak</strong>. Nederst<br />

virkningsgrader (øvre brændværdi i venstre og nedre brændværdi i højre kolonne).<br />

53

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