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Syngas Production and Conversion to Products - The Catalyst Group

Syngas Production and Conversion to Products - The Catalyst Group

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IV-B-39 UFP Program Development Plan .......................................................151IV-B-40 U-GAS-based Wu Jing Gas Plant No. 2, Shanghai, China................153IV-B-41 U-GAS ® Gasifier Schematic ..............................................................153IV-B-42 RENUGAS CHP Plant, Skive Denmark............................................156IV-B-43 KBR/Southern Company Transport Gasifier .....................................160V-C-1 Solid Fuel Gasification Experience...................................................190V-C-2 Underground Coal Gasification (UCG) ............................................200V-C-3 Cost of Fossil Fuels <strong>to</strong> the U.S. Electric Power Industry..................203VI-A-1 ConocoPhillips Technology Development in Gasification................208VI-B-1 Current (2006) Gasification Projects with Identified Feeds...............212VI-B-2 Changes in Market Share; Shell vs. GE .............................................213VI-B-3 Escalation of Plant Construction Costs ..............................................220VI-C-1 Schematic of a Polygeneration Facility..............................................230VI-C-2 <strong>Syngas</strong> <strong>Production</strong> from Coal – Gasification Routes <strong>to</strong> <strong>Products</strong>......233VI-C-3 Capital Cost of New Fossil Fuel Power Plants, Alberta, Canada ......236VI-C-4 Cost of Electricity (New Fossil Fuel Plants, Alberta, Canada)..........237VI-C-5 Scoping Economics: UCG for CTL (Coal-<strong>to</strong>-Liquids) <strong>and</strong> for ElectricPower Generation...............................................................................238VII-A-1 Effect of Scale on <strong>Syngas</strong> Investment Cost .......................................247VII-B-1 Simplified Process Flow Diagram of Integration ofHGDS & DSRP Processes .................................................................251VII-B-2 Process Schematic of Proposed Approach in Multi-Contaminant Control(MCC) ................................................................................................254VII-B-3 Eastman Plant Ammonia <strong>and</strong> Trace Metal Removal Skid.................254VII-B-4 RTI Ultra Gas Cleaning Process ........................................................255VII-B-5 Conceptual Basics of the UFP Technology........................................257VII-B-6 Conceptual Flowscheme of UFP Process...........................................258VII-B-7 Schematic Comparison of Gasification versus UFP ..........................259VII-B-8 UFP Process Flowscheme with highlighted features .........................259VII-B-9 Example of Integrated UFP Power Plant ...........................................260VII-C-1 Plant Construction Cost Escalation....................................................262VII-C-2 CPS IGCC Comparative Study ..........................................................264VII-C-3 Low Rank Coal Study – EPRI ...........................................................265<strong>The</strong> <strong>Catalyst</strong> <strong>Group</strong> 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

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