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Industrial Scale Biomass & Waste Gasification
Gasification Technologies ConferenceOctober 3rd, 2006Washington D.C.
By: Benjamin D Phillips, President
Emery Energy Company
Support Organizations
U.S DOE U.S EPA
Idaho National Lab Brigham Young University
Financial
Technical
Discussion Summary
• Company Background• Past Technology Activities• Technology Description• Current Development Activities
– Thermal Applications (Nat. Gas Displacement)– Power Applications (I/C engines; Steam Turbine or
IGCC)– Other Applications (oxygen blown, syngas
production for liquid fuel synthesis or H2 production)
Relative Scales: Biomass vs. Coal
150 600+0 30075MWe (electric equivalents, but can be thermal or chemical applications)
Biomass& Waste Coal IGCC
Blended FuelsOr Industrial Scale Coal
Emery’s Initial Target Segment 5 – 70 MWeUsing Wood & MSW
Feedstocks
• Began technology development in mid-90’s under different entity name
• Initial testing of technology on MSW and other waste feedstocks, enable Emery to secure private & state funding
• With pilot plant operational experience, Emery secured U.S. DOE monies for further design development of a 70MWe Biomass IGCC
• Formally established Emery Energy Company in 2002• Currently commercializing initial modular gasifier
configurations for thermal and power applications
Company Background / History
70 MWe Biomass IGCC Design• ~70 MWe (net) IGCC
• ~1200 tpd Refuse Derived Fuel (base case); other cases evaluated: wood, coal, switchgrass and blends
• 2 Gasifier trains + 1 spare
• Oxygen-blown, pressurized gasifiers
• Annual availability of >90%
• Technical Participants: Idaho National Lab, BYU and GE Power Systems
This design project created the ‘stretch-goal’ for the technology for biomass feedstocks as well as the roadmap for technology progression and scaling activities
Emery’s Focus & Challenges
• Creation of a technology for multiple feed stocks, some that vary over the year.
• Producing an adequate quality of gas at a reasonable capital and operating price.
• Producing a technology that is robust, low maintenance, and not sophisticated to operate.
• Simple and cost-effective gas cleanup and conditioning.
• Capable of load swings & load following (turn down ratios).
25 TPD Pilot Plant
• Funding support from State Gov’t • 3rd Party Testing & Analyses• Robust, Simple Operation
Completed 2 TPD Test System
• 0 - 125 psig (ASME coded)• System used to test
various fuels and associated reaction kinetics: wood pellets, tire chips, RDF, coal
• Provides additional design data for scale up
• Fully Automated Control System and Gas Analyses equipment installed
U.S. EPA Funding
• Received Grant from U.S. EPA’s MSW Gasification Initiative in 2005 to develop novel tar/oil mitigation methods for MSW / RDF Gasification
• Purpose: to mitigate need or size of downstream tar cracking and condensable gases management systems
• Initial successful technology testing in 2005• Subsequent development & testing planned
Emery Gasification Technology
• Unique Gasifier, founded in fixed-bed technology while leveraging other Gasification Phenomena types
• Issued and pending U.S. & foreign patents • Ash Removal: Dry-Ash OR Slagging• Scalable / Modular (25 tpd >> 100 tpd >> 500 >>)
• Bio-Refining Enabling – Thermo chemical platform• Technology has merit for coal, at larger scales• Benefits:
– Greater Fuel Flexibility– Tar mitigation measures– Reduced # of unit operations compared to other fixed-bed and
fluidized bed processes resulting in CAPEX / OPEX reductions
Boiler
Gasifier
TarCracker
Cyc FilterRecip.
Engines
HX
Steam
FeedwaterHeater
ASH Catalyst ASH
Typical Fluidized Bed Schematic (non-Emery)
MWe
For a Combined Heat & Power Projectin the Northeastern U.S. for 200 tpd wood
Natural GasDisplacement
using producer gas
Boiler
Gasifier
TarCracker
Eliminated
Cyc FilterRecip.
Engines
HX
Steam
FeedwaterHeater
ASH
ASH
Proposed Emery System - Illustrative
+ Lower CAPEX/ OPEX
MWe
ASH
Aims to eliminate need for tar cracker and reduce size of other unit operationsto reduce capital and operating costs while increasing overall efficiency
Natural GasDisplacement
using producer gas
For a Combined Heat & Power Projectin the Northeastern U.S. for 200 tpd wood
Smaller Quench
Air-Blown Thermal / Steam / Power
FUEL PREP
GASIFIER
AIR / STEAM
DRY ASH OR SLAG
HOT CYCLONES
THERMAL OXIDIZERBURNER
HRSG / BOILER S.T. GENERATOR
FLUE GAS CLEANING
% STEAM
Technical Aspects of Gas Usage
1.Flame Characteristics• Swirl Number• Flame Speed Factor
2.Heating Value• Wobbe Number
3.Matching Overall Energy Delivery
4.Multi-Fuel Options
Air-Blown I-C Engine Power Schematic
GAS CLEANING / COOLING I-C ENGINES GENERATOR
% STEAM
FUEL PREP
GASIFIER
DRY ASH OR SLAG
HOT CYCLONES
AIR / STEAM
BY-PRODUCT UTILIZATION
Technical Aspects of Power Application
• Gas Cleaning• particulate removal • tar & oil removal • gaseous phase pollutants (H2S, etc. - as function of feedstock
composition)
• Gas Cooling• For engine input temperature limitations
• Gas Quality• ~140 - 200 btu’s/scf air-blown (depending on gas composition)• ~275 - 330 btu’s/scf 02-blown (depending on gas composition)
• I/C Engine de-rate (no de-rate on gas turbines)• ~40% de-rate on air-blown gas (depending on gas
composition) compared to Natural Gas • De-rate increases installed costs ($/kWe), but does not
impact overall fuel-to-electric efficiencies
GAS COOLING / CLEANING Gas Turbine GENERATOR
FUEL PREP
GASIFIER
DRY ASH OR SLAG
HOT CYCLONES
STEAM
O2-Blown IGCC Schematic
ASUNITROGEN
O2
Steam Turbine
GENERATOR
STEAM
STEAMBY-PRODUCT UTILIZATION
Conclusion
• Biomass is carbon-neutral• Can mitigate waste (industrial & municipal)
• Project scale opportunities that match distributed generation needs and fuels production
• Emerging growth and demand for reducing industrial fuel costs while meeting carbon-reduction goals
500500500
Planned Gasifier Scale Progression
1 225
100 100
500
Tons Per Day
Emery’sPilot Plants
Air-blownCommercialModules
O2-Blown & PressurizedOfferings
Multiple modules to match various project scales
Thank You
Contact Information
Emery Energy Company159 Pierpont Avenue
Salt Lake City, Utah 84101 USA