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Pratt & Whitney RocketdyneCP5-8-1
Freiberg May 8-12, 2007/kms
PWR Compact Gasifier Dry Feed System Development
Kenneth M. Sprouse & David R. Matthews Pratt & Whitney Rocketdyne, Inc. (PWR)
Greg F. Weber University of North Dakota
Energy & Environmental Research Center (EERC)
Presented at the 2nd International Freiberg Conference on IGCC and XtL Technologies
8th – 12th May, 2007
Pratt & Whitney RocketdyneCP5-8-2
Freiberg May 8-12, 2007/kms
Acknowledgement
This presentation was prepared with the support of the U.S. Department of Energy (DOE),
under Award No. DE-FC26-04NT42237.
However, any opinions, findings, conclusions, or recommendations expressed herein are those of the author(s)
and do not necessarily reflect the views of the DOE.
Acknowledgement
Pratt & Whitney RocketdyneCP5-8-3
Freiberg May 8-12, 2007/kms
PROGRAM OBJECTIVES Two Phase Effort
• Phase 1• Scale-up of the PWR 100-ton/day (1,500 psia) feed
system -- U.S. Patent 4,191,500 (1980) – to commercial sizes above 1,200-tons/day
• Demonstrate uniform “two-tier” coal injector flow splitting with 18 elements – previous uniform splitting demonstrated “single tiers” with 3 and 6 elements
• Phase 2• Develop high pressure (1,200 psia) dry solids extrusion
pump at nominal 400-tons/day flow rate• Test pump and feed system continuously for 1,000 hours
Pratt & Whitney RocketdyneCP5-8-4
Freiberg May 8-12, 2007/kms
PWR COMPACT GASIFIER SYSTEM Dry Compact Gasifier with Rapid Start & Shutdown Capability
COAL SILO
DRY SOLIDS PUMP
HIGH PRESSURE DISCHARGE TANK
COMPACT GASIFIER(with Rapid Quench)
CYCLONE SEPARATOR
CANDLE FILTERS
Pratt & Whitney RocketdyneCP5-8-5
Freiberg May 8-12, 2007/kms
GASIFIER THERMODYNAMICS Significant Efficiency Advantages with Dry Feed Gasifiers -- CEA 1994
CARBONACEOUS SOLID
KENTUCKY 9/14 HVABASSAY (AS REC'D)
PROXIMATE ANALYSISWT% MOISTURE 2.00WT% ASH 10.46WT% VOLATILES 38.17WT% FIXED CARBON 49.37
ULTIMATE ANALYSISWT% MOISTURE 2.00WT% CARBON 68.81WT% HYDROGEN 4.92WT% NITROGEN 1.49WT% SULFUR 4.14WT% ASH 10.48WT% OXYGEN 8.16
HHV (BTU/LBM) 12,360SOLID DENSITY (LBM/FT3) 93.60BULK DENSITY (LBM/FT3) 38.78
INPUT CONDITIONS
GASIFIER PRESSURE (PSIA) 1,000STEAM TEMPERATURE (°F) 700
Pratt & Whitney RocketdyneCP5-8-6
Freiberg May 8-12, 2007/kms
• PWR Kinetic Models Developed Under DOE and IR&D Funding Since 1977
• See, e.g., AIChE Journal, 26, 964 (1980) & Comb. Flame, 43, 265 (1981)
• Both 1-D and Multi-Dimensional Capability – modified FLUENT codes
• Correlation with Rocketdyne Hot-Fire Data From 1970-80’s
• PWR Kinetic Models Developed Under DOE and IR&D Funding Since 1977
• See, e.g., AIChE Journal, 26, 964 (1980) & Comb. Flame, 43, 265 (1981)
• Both 1-D and Multi-Dimensional Capability – modified FLUENT codes
• Correlation with Rocketdyne Hot-Fire Data From 1970-80’s
GASIFIER KINETICS High Flame Temperatures Produce Compact Size
Pratt & Whitney RocketdyneCP5-8-7
Freiberg May 8-12, 2007/kms
ROCKET ENGINE TECHNOLOGY Ultra-Dense Phase Feeding and Rapid-Mix Injectors Key
6-ELEMENT INJECTOR LAX THERMODYNAMICS LABORATORY SETUP
1-TO-6 SPLITTER
GASIFIER
SONIC NOZZLE
WATER QUENCH
Compact Gasifier Testing From 1978 (24 tons/day and 100 psia)Compact Gasifier Testing From 1978 (24 tons/day and 100 psia)
Pratt & Whitney RocketdyneCP5-8-8
Freiberg May 8-12, 2007/kms
Ultra-Dense Phase Dry Feed System Simple Dry Bingham Fluid Flow System for Rapid-Mix Capability
COAL PUMP
HIGH PRESSURE(1,200-PSIA)
DISCHARGE TANK
MULTI-ELEMENTINJECTOR
ATMOSPHERICPRESSURE
STORAGE SILO
REGULATOR
TRANSPORT GAS INLET
METERING VENTURI
DRY PULVERIZED COAL INLET
Pratt & Whitney RocketdyneCP5-8-9
Freiberg May 8-12, 2007/kms
BATCH MODE TEST FACILITY -- 1980 Flow Splitting Demonstrated to Non-Uniformities of 1% RSD
COLD FLOW TEST SCHEMATIC
SANTA SUSANA BOWL FACILITY
1-TO-3 SPLITTER
3/8” TUBES
3/4” TUBE • High Pressure• to 1,500 psia
• Coal Flow Rates• to 100 tons/day
• Multi-Element Flow Splitters
• High Pressure• to 1,500 psia
• Coal Flow Rates• to 100 tons/day
• Multi-Element Flow Splitters
Pratt & Whitney RocketdyneCP5-8-10
Freiberg May 8-12, 2007/kms
CONTINUOUS FLOW TEST FACILITY Component Life Demonstration at Near Commercial Scale
SOLIDS PUMP
1,300-PSIAHIGH PRESSURE
DISCHARGE TANK700-GAL
MULTI-ELEMENTINJECTOR
(PWR)
1,000-GALATMOSPHERIC
PRESSURE STORAGE SILO
CYCLONESEPARATOR
BAGHOUSE
GN2/AIR RECYCLE COMPRESSOR
1,500-PSIA(1,000-GAL)
GN2/AIR STORAGE TANK
TO STACK
REGULATOR
REGULATOR
MAKE-UPGN2
METERING VENTURI
CASCADE NOZZLE
• High Pressure• to 1,000 psia
• Coal Flow Rates• 400 tons/day
• Multi-Element Injectors
• High Pressure• to 1,000 psia
• Coal Flow Rates• 400 tons/day
• Multi-Element Injectors
Pratt & Whitney RocketdyneCP5-8-11
Freiberg May 8-12, 2007/kms
EERC FLOW FACILITY First Phase Construction Nearly Complete
Facility Construction – February 2007 (Floors 1 thru 5)
Cascade Nozzle & Cyclone (6th Floor)
HPDT Exit Piping Assembly
Pratt & Whitney RocketdyneCP5-8-12
Freiberg May 8-12, 2007/kms
MULTI-ELEMENT INJECTORS Testing Starts May 2007 with 1x6 Multi-Element Injector
Flow Checkout of Ramsey- Granucor Velocity Sensors
(ThermoElectron Corp.)
1x18 Multi-Element Coal Injector Assembly (1,200 tons/day rating)
High Pressure Injector Chamber
(1,000 psia -- 6.9 MPa)
Pratt & Whitney RocketdyneCP5-8-13
Freiberg May 8-12, 2007/kms
HIGH EFFICIENCY DRY SOLIDS PUMP Phase 2 Effort for Continuous Operation at 400-tons/day
( )( )ε−ρ
−=
1s
atmPdPisenW
( ) ( )
⎥⎥⎥
⎦
⎤
⎢⎢⎢
⎣
⎡
−γ
−γ
⎟⎟⎠
⎞⎜⎜⎝
⎛γ
⎟⎟⎠
⎞⎜⎜⎝
⎛−ε+−γη
=η
1n
1
atmPdP
n
dPatmP
111clh
• Minimum Work Required For Pumping a Pulverized Solid• ~ 6 kJ/lbm at 1,200 psia discharge pressure
• Mechanical Efficiency for a Single Pair of Cycling Lock Hoppers• ~ 25% at 1,200 psia discharge pressure
• Program Goal to Develop a 1,200 psia Discharge 400-tons/day Dry Solids Extrusion Pump At Mechanical Efficiencies Above 50% Without Blowback
• Stamet Inc. testing with Posimetric®
pump encouraging• CFD performance model -- AIChE Journal, 29, 1000 (1983) – nearing
completion
Pratt & Whitney RocketdyneCP5-8-14
Freiberg May 8-12, 2007/kms
DRY SOLIDS EXTRUSION PUMP 400-Tons/Day Tractor Mill (Phase 2)
EXTRUSION PUMP
DRY GRANULAR SOLIDS INLET
ELECTRIC DRIVE MOTORS
REDUCTION GEAR BOXES
BREAKER MILL
DRY GRANULAR SOLIDS OUTLET
• Development Schedule – Completion Dates
• CFD Performance Model Programming
• July 2007• Preliminary Design
• September 2007• Detail Design
• March 2008• Fabrication
• January 2009• Testing
• December 2009
• Development Schedule – Completion Dates
• CFD Performance Model Programming
• July 2007• Preliminary Design
• September 2007• Detail Design
• March 2008• Fabrication
• January 2009• Testing
• December 2009