Coal Gasification Technology for Coal-Fired Power Plants

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Coal Gasification Technology for Coal-Fired Power Plants McIlvaine Hot Topic Hour By CastleLight Energy Corp. Keith Moore President See: www.castle-light.com December 12, 2013 DISCLAMER Information herein is best estimates of the presenters and subject to change. No guarantees or warrantees implied or given.

Objective: CastleLight Energy Corp. Re-engineer coal-fired power plants to reduce operating cost, and generate very competitive electricity with very low emissions. Approach: Apply coal beneficiation and coal-gasification processes to existing coal-fired power plants 2

Conventional Coal-Fired Power Plant with Back-End Emission Controls SO 2 = FGD+ Limestone; NO x = SCR + Ammonia; SO 3 = Trona?, Hg = Activated Carbon? 3

Coal-Fired Power Plant Re-Engineered with Hybrid of Coal-Gasification SO 2 & NO x Controls Right in the Combustion Step. 4

Typical Pulverized Coal-Fired Power Plant 500 MW w/5 Mills Direct Fired Pulverized Coal Boiler Steam Out Raw Coal Bunker Boiler Economizer Ambient Combustion Air Flue Gas To Stack Furnace Hot Inert Flue Gas FD Fan ID Fan Sweep Air w/ Pulverized Coal Burners Air Heater Coal Feeder Cool Flue Inert Gas Emissions Control Mill Fan Coal Mill Hot Primary Air Hot Secondary Air Boiler Feedwater Hot Combustion Air Waste Products FIG. 1 TYPICAL PULVERIZED COAL-FIRED POWER PLANT Copyright 2013 Castle Light Energy Corp 5

Re-Engineered Power Plant Indirect Fired with Coal-Beneficiation Modifications 6

Re-Engineered Power Plant Coal-Beneficiation Modifications Add Coal-Beneficiation Modules One for each coal mill 1. Re-route coal mill sweep gas: Use the hot inert (low O 2 ) boiler exhaust vs. hot air Improve safety - eliminate mill fires & puffs Dry the coal (from >20% to <10% moisture) 2. Separate the powdered coal from sweep gas with bag house: Direct wet sweep gas to boiler stack Process powdered coal to extract volatile hydrocarbon oil 3. Separate carbon particles from oil vapor with cyclone: Meter coal carbon with limestone added to furnace Condense and collect oil from each mill <<<< Sell the oil and pay for the coal! >>>> 7

Coal Beneficiation Process Powder River Basin (PRB) Low Rank Coals Coal Characteristics - PRB : - Low in Btu ~ 8300 Btu/Lb. - High in Moisture 20 30% - High in Ash 10 15% - High in Mercury 130 to 150 ppb Coal Beneficiation Target - PRB Coals : - Increase Btu ~ 10,000 Btu/Lb. (+20%) - Reduce Moisture 10 12% (- 50%) - Reduce Ash 7 10%% (- 50%) - Compliance Mercury ~36 ppb (- 75%) EPA CAMR Compliance Mercury (Hg) : - Existing Plants = 4.0 lb./trillion Btu or ~ 36 Parts / Billion Oil Production Example: 500 MW Electric Generation: Fires 12,000 T/day PRB; cost =$360,000/day; Oil Product: ~ 5000 barrel/day crude oil @ $72/BBL = $360,000/day income Coal By Product: 10,000 T/day high quality coal-fuel for power plant May show as a Carbon-Neutral Process (No CO 2 increase!) An Oil Well in the Coal Pile 8

The Clean Combustion System (CCS) Hybrid of Coal-Gasification & Combustion Schematic CCS Gasification Chamber replaces coal burners & wind box Existing Boiler Furnace. 9

CCS Process Steps SO 2 & NO x emissions control right in the combustion step An entrained-flow gasification of powdered coal; Creates a hot, fuel-rich gas, and frees the sulfur from the coal, Limestone - provides calcium, captures the sulfur in the coal, Forms calcium sulfide (CaS) - a solid particle, High temperatures melt the coal ash (alumina & silica) and encapsulate the CaS; forms liquid slag drains as bottom ash, At these conditions, nitrogen is molecular N 2 (NO x < 50 ppm), Clean hot gases CO, H 2 and N 2 enter boiler & cool, Staged over-fire air completes combustion to CO 2 & H 2 O in boiler (<2300 o F, where NO x formation is frozen). 10

Re-Engineered Power Plant Indirect Fired with Coal-Beneficiation & Coal-Gasification Modifications Raw Coal Bunker Mill ID Fan Sweep Gases To Bag House Boiler Steam Out Boiler PC Coal / Gas Separator Sweep Gas w/ Pulverized Coal Economizer Ambient Combustion Air Pulverized Coal Feeder Surge Bin Over-Fire Combustion Air Furnace Hot Inert Flue Gas FD Fan ASH Water / Ash / Mercury / Oil Extraction Module OIL Water Coal Feeder Coal Mill Pulverized Coal & Sweep Gas from Power Plant Coal Mill CCS Coal Gasification Chamber (SO2 & NOx Control) CLEAN HOT FUEL-RICH GASES Over-Fire Combustion Air Air Heater Flue Gas Exhaust & Particulate to Baghouse Boiler Feedwater Hot (Inert) Primary Air Bottom Ash Disposal Hot Combustion Air Copyright 2013 Castle Light Energy Corp 11

Opposed-Wall Fired Boiler 500 MW 24 Wall-Fired PC Burners WITH CCS, NO SCR REQUIRED Copyright 2013 Castle Light Energy Corp 12

CCS Re-Engineered Wall-Fired Boiler Replace Burners with 24 new CCS Burners & 6 GC s 13

CCS-Tangential Boiler Retrofit 100 to 300 MW 14

CCS-Cyclone Industrial Steam Supply Design Capacity (MCR): 165,300 lb./h Steam (74 T M /h ) Features: Smallest Boiler Foot print per MW T Largest Steam Output per Ton of Steel Internal SO 2 & NO x Emissions Control Near Zero SO 3 emissions High Combustion Efficiency (Reduced CO 2 Near Zero LOI) Fires most all coal types PC Coal-fired w/limestone added Slag Screen Fly Ash Removal Wet bottom slagging operation Clean Furnace Walls Bottom Ash / Fly Ash is saleable No waste water disposal Affordable & Rapid Delivery 15

Re-Engineered Power Plant with CCS & Coal Beneficiation Processes Stack Emissions Estimate* firing PRB coals (1.2 lb. SO 2 /mm Btu Coal) SO 2 = < 0.2 lb./mmbtu (< 105 ppm) ~80% SO 2 reduction NO x = < 0.10 lb./mmbtu (< 75 ppm) CO = < 300 ppm LOI = < 1% (high efficiency combustion) SO 3 = < 0.1 ppm (condensable particulate) Mercury = < 40 ppb Particulate = < 0.03 lb./mmbtu (bag house) Boiler Efficiency = 2 10% increase * Preliminary estimates of performance, measured after bag house no guarantees 16

Rockwell International 25 x 10 6 Btu/hr (1 ton/hr) Test Facility (1990) 17

LNS-CAP Facility ESSO Site, Cold Lake, Alberta Canada 50 mmbtu/hr 3T/hr PRB Coal 18

LNS-CAP Top of LNS Burner 19

LNS-CAP Gasification Chamber Inspection 20

LNS-CAP Slag to Water Trough 21

Boiler Radiant Section View Forward to Burner 22

Demonstrated Emissions SO 2-0.2 lb./mmbtu & NO x - 0.15 lb./mmbtu ESSO LNS-CAP Facility, Cold Lake, Alberta, Canada 23

CCS-Stoker Project Objective: - Reduce operating cost by half (switch to low-cost high-sulfur Illinois coal 2.5 lb. SO 2 /mmbtu) - Construction Permit w/ waiver NSPS, PSD; no NSR - Emissions Warrantee: <0.9 lb. SO 2 /mmbtu, <0.25 lb. NO x /mmbtu Project Initiated: Oct 2005, Commissioning: Jan 2007 CEC Scope : Process Design & Engineering; - Supply all equipment, hardware, electrical, instrumentation / controls - Provide Commercial Warrantee & License Client Scope: Site Construction Management; - Equipment Installation, as directed by CLPRC - Commissioning & Start-up Project Support: In part, by the Illinois Department of Commerce and Economic Opportunity through the Illinois Clean Coal Institute and the Office of Coal Development. 24

Coal-Fired Stoker Boiler (typical) CCS Retrofit Modifications Remove: Stoker Feeders, Ash Hopper, Brick over stoker grate Control Panel New Equipment: CCS Burner, Gasification Chamber, Combustion Air Heater Boiler Instruments, Coal Mill, Bag house, FD fan, BM & Combustion Sys, HMI & PLC Controls New MCC Operators (one/shift): Was all manual operation; Now with HMI - from cold start to automatic full load operation in 5 hrs. 25

CCS-Stoker Retrofit 30 MW (Thermal) - 125 mmbtu/hr 5 T/hr Coal 26

CCS-Stoker Gasification Chamber 27

CCS-Stoker Gasification Chamber Installation McBurney Corp designed and supplied the GC Connected to the boiler drums for natural circulation water cooling Shop fabricated membrane wall studded and refractory lined. 28

Stoker Boiler Furnace Deposits Typical Examples Wall Ash Deposits Exit Fouling Deposits 29

Operation Observations CCS-Stoker Furnace Ash Deposits CCS Walls CCS Ceiling 30

CCS-Stoker Operation @ MCR Steam Overboard 31

CCS-Stoker Retrofit Performance Preliminary Results Full Load Operation Item Stoker Base Line Test Preliminary CCS Performance % Change from Base Line SO 2 Stack Emissions (lb/mmbtu) 1.80 0.72 NOx Stack Emissions (lb/mmbtu) 0.50 0.14 (88 ppm) Boiler Efficiency 77.0 86.9-67.0 % - 72.0 % + 12.8 % CO 2 Emissions - Ton/yr GW credits (% Reduction) Project Cost Recovery (from firing lower cost coal) 94,019 73,720 20,300T/y (- 21.6 %) ~ 3 years 32

CCS Features Improved Operability, Availability & Reliability All equipment off-the-shelf & familiar to the operators - Safe, stable burner operation, - Same startup, shutdown and turndown as the PC plant Bottom Ash (slag) removed before furnace - low particulate/ash load; clean furnace, less soot blowing Sulfur removed from furnace gases - near-zero SO 3 : - Allows for lower furnace exit temperatures - Minimize water-wall wastage & corrosion, - Can use hot boiler exhaust for pulverizer sweep air: - Dry the coal reject moisture - Improves coal pulverizer safety from fire & puffs (low O 2 ) Improved Boiler Efficiency (2 to +10%) - Reduce CO 2 emissions - High combustion efficiency (LOI < 1%) Limestone is only chemical required No waste water for disposal 33

CCS Summary (Key Strategic Issues) From Fundamental Combustion Theory to Commercial Operation Fire lower cost coals - reduce plant operating cost Meets EPA s new stringent regulations for SO 2 & NO x Allow power plant upgrade with waiver of NSPS & PSD - No NSR Low Retrofit Cost; maintains older, smaller plants competitive Improve plants capacity factor & dispatch Fits within plant & boiler site footprint Ash products have value (sell bottom ash & fly ash) No hazardous or toxic chemicals required It s ADVANCED COAL GASIFICATION TECHNOLOGY! 34

Strategic Business Opportunity? Acquire Abandoned Coal-fired Power Plants Re engineer and Update PC Electric Generation Plant with CCS; - Provides SO 2 & NO x emissions control, - Waiver of NSPS, PSD, & no NSR Integrate a CBM on each coal Mill Improved power plant performance - improves boiler heat rate/efficiency - less fuel fired Very competitive dispatch; - paid for fuel = low cost electricity Meet EPA CAMR goals (+90% mercury reduction) Can show carbon neutral process = No CO 2 increase! 35

CastleLight Energy Corp. Re Engineering Programs Please Contact CastleLight Energy Corp. Phone: 805-551-0983 Keith Moore - President E-mail: keith@castle-light.com See Web Site: www.castle-light.com For Technical Presentations / Plant Surveys and Reports: Re-Engineering Coal-Fired Power Plants for Low Emissions and Competitive Electricity Dispatch Operating Experience of a Coal-Fired Boiler Retrofit with an Advanced Hybrid of Coal Gasification For SO 2 & NO X Emissions Control and Reduced Operating Cost Proposal: - Re-Engineering Coal-Fired Power Plants with the Clean Combustion System 36