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- Politecnico di Milano
- Degree programme
- Chemical Engineering
- Subject
- Chimica Industriale
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- Exercises · By topic
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ExercisesBy topic
Esercitazione 2 Soluzione
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Chimica IndustrialeBy topic
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Template for Solution ES1 Chimica Industriale A B C D E F G Stoich F tot [mol/h] 235.6054935 668.5269 565.992 461.0863 104.9057 28.16448443 432.921 ‐2 mol fraction N2 0.245 0.217478 0.1662965 0.2025 0.00717 0.2025 0.2025 ‐1 mol fraction H2 0.735 0.652434 0.4988895 0.6075 0.02152 0.6075 0.6075 ‐3 mol fraction NH3 0 0.058282 0.2499997 0.0900 0.95324 0.0900 0.0900 2 mol fraction CH4 0.0200 0.071806 0.0848144 0.1000 0.01807 0.1000 0.1000 0 F mol N2 [mol/h] 57.72334591 145.3899 94.122483 93.3699 0.7526 5.703308096 87.6666 ‐1 F mol H2 [mol/h] 173.1700377 436.1698 282.36745 280.1097 2.2577 17.10992429 263 ‐3 F mol NH3 [mol/h] 0 38.96293 141.49782 41.4978 100.0000 2.534803598 38.9629 2 F mol CH4 [mol/h] 4.71210987 48.00425 48.004251 46.1089 1.8954 2.816448443 43.2921 0 Dati @ Ay CH4 0.0200 y N2/H2 0.9800 Stoich feeding @D y CH4 0.1000 @D y NH3 0.0900 @C y NH3 0.2500 Solubility coefficients aN2 0.0001 Nm3/bar/kgNH3 Produttivita 100 t/day NH3 bH2 0.0001 Nm3/bar/kgNH3 Pressione cond 490.0000 bar cCH4 0.0005 Nm3/bar/kgNH3 Impongo una base di calcolo 100.0000 mol/h NH3 mass flow 1.7000 kg/h N2 @ E 0.0099 0.0169 Nm3/h N2 0.7526 mol/h H2 @E 0.0298 0.0506 2.2577 mol/h CH4 @ E 0.0250 0.0425 1.8954 mol/h Lambda 51.2674 mol/h BM N2 aef 0.0000 mol/h 0.0000 mb h2 0.0000 mb nh3 0.0001 bm ch4 0.0003 NH3 in c 0.0000 Conv impiantp 0.8882 Conv reattore 0.3526 Prod full scale 100.0000 ton/day 4166.6667 KG/H Fattore di scala 2450.9804
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