Syngas Production and Conversion to Products - The Catalyst Group

III-B-4 AGHR + Secondary Reformer .............................................................49IV-A-1 NOx emission Buggenum IGCC..........................................................56IV-A-2 Sox, NOx and dust emissions from coal fired plants ...........................57IV-A-3 Gasification integrated in Shell Pernis refinery ...................................57IV-A- 4 GE Energy coal gasification process with water quench .....................59IV-A- 5 GE Energy Coal gasification process with effluent cooler ..................60IV-A- 6 Effect of water slurry type feed on efficiency of gasifier ....................61IV-A- 7 Shell Coal Gasification Process ..........................................................62IV-A- 8 The Sasol-Lurgi Gasification system ...................................................66IV-A-9 The E-Gas Gasifier system...................................................................68IV-A-10 Siemens SFG reactor for coal application............................................69IV-A-11 BGL Gasifier........................................................................................71IV-A-12 KBR Transport Gasifier .......................................................................72IV-A-13 Configuring the PHTW gasifier ...........................................................73IV-A-14 Values of Liquid Hydrocarbons ...........................................................79IV-A-15 GE Reactor with water quench and with boiler. ..................................80IV-A-16 GE Soot water processing ...................................................................81IV-A-17 Shell Gasification Process, SGP...........................................................83IV-A-18 Lurgi MPG Process with Water Quench..............................................85IV-B-1IV-B-2IV-B-3IV-B-4IV-B-5IV-B-6IV-B-7IV-B-8Hydrogen flux through ≈15 µm-thick cement membrane on aporous substrate at 500 and 900°C using 100% H 2 at ambientpressure as the feed gas. .......................................................................90Time dependence of hydrogen flux ≈0.20 mm-thick cermetmembrane at 900°C with feed gas of ≈400 ppm H 2 S/73%H 2 /balance He.......................................................................................91Schematic of H 2 Transport Across Membrane.....................................94Tubular HTM Configuration................................................................94Simplified Flowsheet of CO-Shift / HTM Process StagedIntegration ............................................................................................95SEM Image of PBI-coated Pall AccuSep Tube used for moduledevelopment .........................................................................................97PBI-coated Pall AccuSep Tube with ~67cm2 of activemembrane area .....................................................................................98Schematic of molecular sieving separation via micro-porous membranes............................................................................................................100The Catalyst Group Resources, Inc., P.O. Box 680, Spring House, PA 19477, Phone: (215) 628-4447,Fax: (215) 628-2267, E-mail: tcg@catalystgrp.com, Website: www.catalystgrp.com