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Figure 29: Block Diagram for pre-combustion carbon capture IGCC Plant .................... 53 Figure 30: Adsorption ....................................................................................................... 55 Figure 31: Polymeric Membranes..................................................................................... 56 Figure 32: Ion Transport Membrane................................................................................. 57 Figure 33: Cryogenic Separation ...................................................................................... 58 Figure 34: Entrained Flow Gasifier Figure 35: Moving Bed Gasifier............. 60 Figure 36: Equivalence Ratio vs. Equilibrium Mole Fraction .......................................... 62 Figure 37: Equivalence Ratio vs. Equilibrium Mole Fraction .......................................... 63 Figure 38: Initial Mole Fraction vs. Equilibrium Mole Fraction ...................................... 64 Figure 39:Initial Mole Fraction vs. Equilibrium Mole Fraction ....................................... 64 Figure 40: Initial Mole Fraction of water vs. KJ/mole of Synthesis gas .......................... 65 Figure 41: GE Reactor ...................................................................................................... 66 Figure 42: Physical Solvent AGR Process Flow .............................................................. 70 Figure 43: Upstream AGR Placement Temperature Profile ............................................. 71 Figure 44: Down Stream AGR Placement Temperature Profile ...................................... 71 Figure 45: Composition of synthesis gas through WGS and AGR .................................. 73 Figure 46: Effects of variable dilution methods and inlet temperatures on flame temperature (Chiesa & Lozza, 2005) ................................................................................ 75 Figure 47: Calculated nitrogen requirement for a given inlet temperature....................... 77 Figure 48: Nitrogen Oxide (NOx) formation at various effluent temperatures for a defined gas turbine......................................................................................................................... 78 Figure 49: Heat Recovery Operations from Combined Cycle Processes ......................... 78 Figure 50: Steam and NOx produced from the gas turbine, while varying excess oxygen provided ............................................................................................................................ 79 Figure 51: Nitrogen Oxide Comparison. .......................................................................... 84 Figure 52: Sulfur Dioxide Comparison............................................................................. 85 Figure 53: Particulate Matter Comparison........................................................................ 85 Figure 54: Carbon Dioxide Comparison........................................................................... 86 Figure 55: Price & Volume of Sulfur Dioxide Traded ..................................................... 93 Figure 56: Class VI Wells Figure 57: Class II Wells....................................... 96 Figure 58: Fraction costs of the EGS field development and binary power plant (GETEM results)............................................................................................................................. 107 Figure 59: Determining Break Even Point for Double Flash Plants 41MW ................. 110 Figure 60: Determining Break Even Point for Double Flash Plants 84MW ................ 111 Figure 61: Determining Break Even Point for Double Flash Plants 125MW .............. 112 Figure 62: NPV of EGS and IGCC Combined Systems................................................. 120 xiPDF Image | GREAT NECK WATER POLLUTION CONTROL DISTRICT NASSAU COUNTY, NEW YORK MICROTURBINE INSTALLATION FEASIBILITY STUDY
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