id	author	title	date	pages	extension	mime	words	sentence	flesch	summary	cache	txt
cet-5718		cet-5718		6	.pdf	application/pdf	3369	115	38	The mass and energy balances resulted from simulation are then used to assess the main techno-economic and environmental indicators of the evaluated cases, like plant energy efficiency, ancillary power consumption, carbon capture energy and cost penalty, specific CO2 emissions, capital costs, specific capital investment per kW, operation and maintenance (O&M) costs, cost of electricity, CO2 removal and avoidance costs, cash flow analysis. Oxygen purity: 95 % O2; Power consumption: 225 kWh/t O2 Water gas shift (WGS) Sour shift; 3 catalytic beds; Steam/CO ratio: 2.5; CO conversion: >95 % Acid Gas Removal (AGR) Selexol®-based gas-liquid absorption - desorption cycle CO2 drying and compression Delivery pressure: 120 bar; Drying solvent: TEG Gas turbine Type: M701G2 (MHI); Net power output: 334 MW; 39.5 % efficiency Steam cycle Steam pressure: 120 bar / 34 bar / 3 bar Condenser pressure 50 mbar Cooling water temperature 15 oC Heat exchanger ∆Tmin. 10 oC HX pressure drop (∆P) 2 - 5 % 3. Results and discussions Evaluated IGCC power plant cases with CCS were modelled and simulated using ChemCAD.	cache/cet-5718.pdf	txt/cet-5718.txt