Siemens Gas Turbine H 2 Combustion Technology for Low Carbon IGCC

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1 Siemens Gas Turbine H 2 Combustion Technology for Low Carbon IGCC Presented at:, Phillip Brown: Program Manger, SGT6-5000F IGCC Joe Fadok: Program Manager, Siemens/DOE Advanced Hydrogen Turbine Program Pedy Chan: Program Engineer, Siemens/DOE Advanced Hydrogen Turbine Program Siemens Power Generation, Inc. - Orlando FL, USA

2 Overview 1. Introduction to Siemens Gas Turbines 2. Siemens Syngas Operating Experience 3. Combustion System Development for the SGT6-5000F 4. Siemens / DOE Advanced Hydrogen Turbine Development 5. Conclusions Page 2

3 1. Introduction to Siemens Gas Turbines - Gas Turbines for IGCC Applications 60 Hz Applications 50 Hz Applications E Class E Class F Class F Class Advanced H 2 Turbine Applications Include: Coal, Petcoke, or Residual Oil Based IGCC Other Low-BTU or Med-BTU Applications Greenfield IGCC or Repowered NGCC Page 3

4 1. Introduction to Siemens Gas Turbines - The SGT6-5000F (formerly known as W501F) Compressor 16 Stage Compressor High Efficiency Combustor 16 Basket Low Emission Turbine 4 Stage Turbine 3 Stages Air Cooled 190+ Operating Units >3.5 Million Operating Hours 94% Fleet Availability (Sept 2007) Page 4

5 2. Siemens Syngas Operating Experience - Nuon Power Buggenum (Netherlands) IGCC Plant SHELL gasification 253 MW, SGT5-2000E Start-up in 1993 on NG, 1994/95 on SG > 97,000 Total operating hours (2007) Page 5

6 2. Siemens Syngas Operating Experience - ELCOGAS Puertollano (Spain) IGCC Plant PRENFLO gasification 300 MW, V94.3 Start-up in 1996 on NG, 1997/98 on SG > 73,000 Total operating hours (2007) Page 6

7 2. Siemens Syngas Operating Experience - Syngas Experience at Modern IGCC Plants Customer/Plant (Location) Hörde Steelworks (Dortmund, Germany) Electrical Output (net) Gas Turbine Main Features IGCC Start-up Blast-furnace-gas-fired, gas turbine as 1960/ 8 MW VM5 Handan Iron & Steel compressor drive 2000 (Handan, P.R. China) U. S. Steel Corp. (Chicago, USA) 20 MW CW201 Blast-furnace-gas-fired gas turbine 1960 STEAG/Kellermann First CC plant in the world with integrated 163 MW V93 (Lünen,Germany) LURGI coal gasification (hard coal) 1972 DOW Chemical 208 MW 1) CC plant with integrated DOW coal 2 x W501D5 (Plaquemine, USA) gasification 1987 Nuon Power Buggenum CC plant with integrated SHELL coal 253 MW V94.2 (Buggenum, Netherlands) gasification (hard coal and biomass blend) 1995 HRL CC plant with integrated drying gasification 10 MW Typhoon (Morwell, Australia) process (lignite) 1996 Sydkraft First CC plant in the world with integrated 6MW Typhoon (Värnamo, Sweden) biomass gasification 1996 ELCOGAS CC plant with integrated PRENFLO coal 300 MW V94.3 (Puertollano, Spain) gasification (coal and petroleum coke blend) 1997 ISAB Energy CC plant with integrated TEXACO heavy-oil 521 MW 2 x V94.2K (Priolo Gargallo, Italy) gasification (asphalt) 1999 ELETTRA GLT (Servola, Italy) 180 MW V94.2K CC plant with steel-making recovery gas 2000 ARBRE (Eggborough, UK) 8 MW Typhoon CC plant with integrated biomass gasification 2002 EniPower CC plant with integrated SHELL heavy-oil 250 MW V94.2K (Sannazzaro, Italy) gasification ) 160 MW from syngas and 48 MW from natural gas Large Modern IGCC Plants 450,000+ Operating Hours Page 7

8 3. Combustion System Development for the SGT6-5000F - IGCC Hardware Description Nozzle & Basket Diffusion flame nozzle based on the design that successfully operated at the SGT6-3000E (formerly known as the W501D5) Dow Chemical Plaquemine site. Dual fuel design: Natural gas as startup & backup fuel, H 2 / Syngas as main fuel. Dilution is premixed into the fuel. Combustor basket is an improved Siemens diffusion flame basket design. The transition segment and downstream turbine hardware is the standard design, no change is necessary for IGCC. Page 8

9 3. Combustion System Development for the SGT6-5000F - Constituents Tested Range of diluted H 2 / Syngas compositions tested: vol% min Syngas max min H 2 max H 2 11% 22% 30% 73% CO 21% 34% 0% 46% CO 2 1% 11% 0% 14% CH 4 0% 4% 0% 5% N 2 5% 41% 0% 60% H 2 O 0% 57% 0% 57% SGT6-5000F supports operation at all levels of carbon capture Page 9

10 3. Combustion System Development for the SGT6-5000F - Test Objectives Nozzle & Basket To Demonstrate: Operability on NG from ignition to 100% load Operability on H 2 / Syngas from 30% to 100% load Fuel transfers from NG to H 2 / Syngas between 30% to 90% load and vice versa NG and H 2 / Syngas co-firing between 30% and 100% load Emissions Targets: On H 2 / Syngas 15 ppm NOx from 50% to 100% load 10 ppm CO from 70% to 100% load On NG 25 ppm NOx from 70% to 100% load 10 ppm CO from 70% to 100% load Page 10

11 3. Combustion System Development for the SGT6-5000F - Combustion Testing Combustion Test Rig High pressure High temperature Engine conditions are simulated Fuel flexible: SG / H 2 / NG Combustion Test Gases H 2 O, N 2 Diluents available H 2, CO, CO 2, NG available for testing Test Rig H 2 /CO N 2 NG Fuel Supply Page 11

12 3. Combustion System Development for the SGT6-5000F - Combustion Test Results SGT6-5000F test results show that emissions targets and all operability targets have been meet. Page 12

13 4. Siemens / DOE Advanced Hydrogen Turbine - Program Background Siemens was awarded a contract for Phases 1 and 2 of a 10-year program to develop an advanced GT for IGCC applications. DOE Advanced Power Systems goal is to conduct R&D for CO 2 sequestration ready coal-based power systems. Phase 1 Technologies identification, R&D Implementation Plan, conceptual designs Phase 2 Development and Validation of Component Technologies Phase 3 (Not yet awarded) GT-IGCC plant construction, validation / demonstration Completed Page 13

14 4. Siemens / DOE Advanced Hydrogen Turbine - Development Timeline Intermediate SGT6-5000F H2+Syngas FutureGen Technology Infusion SGT6-IGCC H2+Syngas 2010 Goal DOE Turbine 2010 Goal: 2-3% pt improvement in CC efficiency 20-30% reduction of CC capital cost 2 ppm NOx on Syngas FutureGen & DOE 2012 Goal: Showcase of near zero emissions coal-based power plant Demonstrate Carbon Sequestration Capability Long-term Phase 1 Conceptual Design Advanced GT H2+Syngas Phase 2 Development and Validation of Component Technologies DOE Turbine 2015 Goal : Demonstrate Carbon Sequestration ability => High H 2 fuel 3-5% pt improvement in CC efficiency 2 ppm NOx on H 2 fuel Phase 1 Phase 2 Phase 3 (Not in current award) With the 2-step approach, DOE intermediate and long-term goals are addressed. Technology infusion from the Advanced GT to FutureGen & 2010 GT will be realized. Page 14

15 5. Conclusions Siemens has extensive gas turbine operational experience with fuels for IGCC spanning several decades. The combustion development program for the SGT6-5000F engine is based on a proven IGCC combustor and fully rig tested to ensure all emissions and operational requirements can be meet with syngas and high hydrogen syngas fuels. Siemens in partnership with the DOE Advanced Hydrogen Turbine project is working on advanced hydrogen combustion technologies producing lower emissions while at the same time operating at higher gas turbine efficiencies for IGCC projects with carbon capture. Page 15

16 Thank You Page 16

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