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Plasma gasification of Municipal Solid Waste. Tien Diep Kevin Estacio Sebastian Iskra Linda Quan Felix Velazquez Mentor: Dennis O’Brien. Block Flow Diagram. Block Flow Diagram Continued. Schematic Flow Diagram. Data- Composition of Air. Material and Energy Balance.
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Plasma gasification of Municipal Solid Waste TienDiep Kevin Estacio Sebastian Iskra Linda Quan Felix Velazquez Mentor: Dennis O’Brien
Hand calculations • H2S+2NaOH -> Na2S+2H2O • HCl + NaOH --> NaCl + HOH • Material balances for the treatment vessel H2S Stoich (2) 11.3842 tons/day = 1.13842x10^7g/day 1.13842x10^7 g/day x (1mol H2S/34.08g H2S) x (4mol NaCl/1mol H2S) x (58.4430g/1mol NaCl) = 7.80x10^7 [g/day NaCl] x (1day/24hours) x (1lb / 453.5923 g) = 7165.023 lb/hr NaClout HClstoich 31.6723 tons/day = 3.16723x10^7g/day 3.16723x10^7g/day x (1mol HCl/36.46g) x (1mol NaOH / 1mol HCl) x (40g NaOH/1mol NaOH) = 3.4747x10^7 [g/day NaOH] x (1day/24hours) x (1lb / 453.5923 g) = 3191.834 lb/hr NaOHout
Hand Calculaitons • H = ΔHf° + • CpHCl = 0.029 [KJ/mol K] • CpH2S = 0.034 [KJ/mol K] HHCl = -92.3 KJ/mol + 0.029 KJ/kg K (363-298) = -85.696 Btu/mol (-1096.41 Btu/lb) HH2S= -86.373KJ/mol + 0.034 KJ/mol K (363-298) = -16.849 Btu/mol -224.254 Btu/lb -85.696 Btu/mol x(1mol HCl/35.453g) x (453.5923g/1lb) = -1096.41 Btu/lb -16.849 Btu/mol x (1mol H2S/34.08g) x (453.5923g/1lb) = -224.254 Btu/lb
Timeline • Block FlowDiagram • ProcessFlowDiagram • Material & Energy Balance • Calculations • AnnotatedEquipmentList • EconomicEvaluationfactoredfromEquipmentCosts
References • http://www.engineeringtoolbox.com/air-composition-d_212.html • http://web.ist.utl.pt/~ist11061/de/IndPrecos/Che-2010_04_Econ-Indic.pdf • http://www.netl.doe.gov/energy-analyses/pubs/Bituminous%20Baseline_Final%20Report.pdf • http://www.seas.columbia.edu/earth/wtert/sofos/nawtec/nawtec18/nawtec18-3515.pdf • http://www.chemicalprocessing.com/articles/2008/245.html