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Energy from Waste Gas & Reject Coal

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Western States <strong>Coal</strong> Mine<br />

Methane Recovery and Use<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

Workshop<br />

<strong>Energy</strong> <strong>from</strong> <strong>Waste</strong> <strong>Gas</strong> & <strong>Reject</strong><br />

<strong>Coal</strong><br />

John G. Whellock Ph.D.<br />

JWT JWTeechnolo<br />

JWT chnolo chnologgie ie iess


Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

CMM Recovery in USA<br />

US EPA Underground CMM Source Data 2000<br />

VAM<br />

66%<br />

27%<br />

7%<br />

Emissions avoided<br />

Drained CMMavailable<br />

JWTechnolog<br />

JWT JWTechnologies<br />

echnologies ies


Potential Sources of Mine <strong>Gas</strong><br />

• Ventilation Air Methane (VAM) with 0-2% 0 2%<br />

CH 4<br />

• Low Quality <strong>Gas</strong> <strong>from</strong> less than 5% up to<br />

27% CH 4, , which is too dangerous to flare<br />

• Gob <strong>Gas</strong> or <strong>Coal</strong>mine Methane-CMM Methane CMM ~ 30- 30<br />

90% CH 4—contaminated contaminated with O 2, , N 2 and<br />

CO 2<br />

• Flammability limits for methane 5-15% 5 15% CH 4<br />

in air<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWT JWTeechnolo<br />

JWT chnolo chnologgie ie iess


Issue in the Management of Mine<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

Methane<br />

• Safety considerations are paramount<br />

• Low quality gas is not flared but vented away <strong>from</strong><br />

operations<br />

• VAM has insufficient fuel value to support combustion—<br />

combustion<br />

reluctance to burn the methane just to defray emission— emission<br />

needs to make economic sense<br />

• CMM, if contaminated with air or carbon dioxide, is<br />

problematic for pipelining to market but technologies exist<br />

for its upgrading<br />

• Variability of the gas quality can create significant design<br />

constraints<br />

•<br />

JWT JWTeechnolo<br />

JWT chnolo chnologgie ie iess


Characteristics necessary for utilization<br />

• Safe operation<br />

of VAM as Ancillary Fuel<br />

• Efficient use with low additional energy requirements<br />

• Application of the recovered heat as power or alternative<br />

energy<br />

• Potential additional sources of heat with no virtual cost<br />

• Combined use of coal mine rejects, VAM and/or low quality<br />

gas provide new opportunities—application opportunities application of the TORBED*<br />

Reactor-- Reactor--toroidal<br />

toroidal fluidized bed reactor<br />

*TORBED is the register registered ed trademark of of Mortimer Techn Techno olog logy y Holdings Holdings<br />

Limited UK<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWT JWTeechnolo<br />

JWT chnolo chnologgie ie iess


Considerations for Use of Low Quality<br />

Methane approx. 2 to 30% CH 4<br />

• Range below explosive limits i.e. VAM with ca.<br />

0-2% 2% CH 4 can be used as combustion air source<br />

feeding the reactor<br />

• Explosive range is usually vented after being<br />

drained<br />

• Management of gas within the explosive limits<br />

range—5-15% range 15% CH 4<br />

• Above explosive range is usually vented or<br />

flared<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWT JWTeechnolo<br />

JWT chnolo chnologgie ie iess


The TORBED® Technology can be applied to<br />

utilization of Low Quality CH 4 as Fuel<br />

• The TORBED Expanded Bed Reactor can<br />

be configured to burn low quality CH 4<br />

(including that which is usually considered to<br />

be within the explosive limits)<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


TORBED process reactor technologies<br />

The TORBED Compact Bed Reactor (CBR)<br />

The process gas stream lifts a shallow compact bed<br />

imparting horizontal motion and subjecting the<br />

base layer of the bed to high impact gas velocities<br />

and thus higher heat and mass transfer rates.<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

Torftech<br />

JWT JWTeechnolo<br />

JWT chnolo chnologgie ie iess


TORBED process reactor technologies<br />

inner<br />

vortex<br />

bed bed<br />

blades<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

The TORBED<br />

Expanded Bed Reactor<br />

(EBR)<br />

Torftech<br />

The process gas flow is increased until it<br />

entrains all the bed particles in a rapidly<br />

spinning inner vortex.<br />

Particles separate by centrifugal force<br />

<strong>from</strong> the inner vortex to the outer wall<br />

before returning to the base of the reactor<br />

creating a diffuse toroidal bed.<br />

The base layer of the bed is subjected to<br />

high impact gas velocities and thus high<br />

heat and mass transfer rates.<br />

JWT JWTechnologies<br />

echnologies


TORBED process reactor technologies<br />

Torftech<br />

The toroidal motion of the bed in this 300mm<br />

diameter cold model is very clear<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


TORBED process reactor technologies<br />

Torftech<br />

The passage of gas through the fixed blades produces a<br />

diffuse bed with toroidal movement of the particles<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


TORBED process reactor technologies<br />

These EBRs are 6m in<br />

internal diameter Expanded<br />

Bed Reactors utilising<br />

alumina to scrub HF emitted<br />

<strong>from</strong> the smelting pots<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

The largest reactors are the<br />

20 gas scrubbers installed in<br />

two of the Comalco aluminium<br />

smelters in New Zealand and<br />

Tasmania.<br />

Torftech<br />

JWTechnologies


<strong>Coal</strong> Fines Problem or Opportunity?<br />

• In the eastern USA alone, there are in excess of 2 billion<br />

tons of coal fines, (EPRI ‘94), which might be reclaimed<br />

• Use of coal fines is a function of properties—GCV, properties GCV, sulfur,<br />

ash and size range for application<br />

• Some is currently blended and utilized in PC fired boilers<br />

• Some could be utilized in circulating fluid bed boilers<br />

• Limits can sometimes be ash softening temperature, sulfur<br />

level and ash management<br />

• We see the opportunity for utilization of this material for:<br />

• Co-processing Co processing with VAM or Low Quality <strong>Gas</strong><br />

• Steam or power raising at mine sites<br />

• Drying of main production coal<br />

• Fuel source for limestone calcination<br />

• Devolatilization and char production<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


Recent Testing of the TORBED<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

Technology in Poland<br />

• TORBED Reactor used to devolatilize wet waste coal fines<br />

(


Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


TORBED process reactor technologies<br />

Combustion of Biomass is shown here<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

Torftech<br />

JWTechnologies


Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


TORBED process reactor technologies<br />

• Very high heat/mass transfer rates per unit volume-<br />

superior to present technologies<br />

• Particles—especially Particles especially fines-- fines--are<br />

are processed efficiently due to<br />

high centrifugal force<br />

• Lower cost reactor with small footprint<br />

• Low pressure drop operation compared with other high<br />

efficiency solid-gas solid gas contactors enables reduced power for<br />

high volumetric flowrates<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

Torftech<br />

Special Characteristics of the TORBED Reactor<br />

JWTechnologies


TORBED Reactor used for Drying<br />

Applications<br />

• Low grade coal or rejects can be utilized in the<br />

TORBED reactor for drying applications<br />

• The reactor has low pressure drop and uses fuel<br />

efficiently-- efficiently--therefore<br />

therefore it can be applied as a<br />

combustor for heating another drying process— process<br />

e.g. rotary dryer<br />

• For fine coals or pulverized fuel a second<br />

TORBED can operate as a dryer. The design is<br />

tolerant to solids<br />

• The design has potential to remove inherent<br />

moisture under careful atmosphere control<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


TORBED Reactor used for Drying<br />

Applications<br />

FAN<br />

HIGH GRADE<br />

WET COAL<br />

27% H 2 0<br />

65 mtph<br />

6.4% Ash<br />

GCV 7800<br />

Btu/lb<br />

REJECT<br />

COAL<br />

FC 2 1%<br />

VM 3 3%<br />

H 2 O 23%<br />

ASH 23%<br />

3.8 mtph<br />

AIR<br />

2.5m. Dia<br />

TORBED<br />

DRYER<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

COAL PROCESSING FLOW DIAGRAM<br />

650 o C<br />

3.0m. Dia<br />

TORBED<br />

COMBUSTOR<br />

110 o C<br />

BAG<br />

FILTER<br />

FAN<br />

41,400<br />

Nm 3 /h<br />

FAN STACK<br />

DRIED PRODUCT<br />

49.4 mtph<br />

2.9% H 2 0, 10.4% Ash<br />

GCV 10300 Btu/lb<br />

JWTechnologies


TORBED Reactor used for Char Production<br />

and Power<br />

• <strong>Coal</strong> fines used to partially fire TORBED Reactor<br />

• Oxygen in reactor air is limited<br />

• Volatiles burned to low level producing char<br />

residual<br />

• Cyclone off majority of char<br />

• Complete combustion of fines and residual<br />

volatiles in afterburner/boiler for power production<br />

• Example shows 50 mtph of coal producing 35.8<br />

mtph of char and steam for approx. 20MW of<br />

power<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


TORBED Reactor used for Char Production<br />

and Power<br />

INT. REF.#1015<br />

AIR<br />

COAL<br />

FC 55.4%<br />

VM 22.6 %<br />

H 2 O 5.9%<br />

ASH 16.1%<br />

GCV 10580<br />

Btu/lb<br />

50,000 kg/h<br />

@ 20 o C<br />

116,178 kg/h<br />

@ 20 o C<br />

106,613 kg/h<br />

GAS + 3975<br />

kg/h CHAR<br />

@ 650 o C<br />

TORBED<br />

T3500<br />

650 o C<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

100 tph Steam<br />

CYCLONE<br />

TURBINE<br />

AFTERBURNER BOILER<br />

COAL<br />

PROCESSING<br />

FLOW DIAGRAM<br />

FC 69 .7%<br />

VM 10.0 %<br />

ASH 20.3%<br />

GCV 11170<br />

Btu/lb<br />

Condensate<br />

150 o C<br />

RECYCLE 96,363 kg/h @150 o C<br />

(5% OXYGEN)<br />

BAG FILTER<br />

226,685<br />

kg/h @ 150 o C<br />

(5% OXYGEN)<br />

FAN STACK<br />

ASH 81 kg/h<br />

CHAR 35,775 kg/h<br />

EXHAUST<br />

130,322 kg/h<br />

@ 150 o C<br />

JWTechnologies


Assumptions-TORBED Assumptions TORBED Reactor Producing Char & Power<br />

Power Generated<br />

<strong>Coal</strong> Feed<br />

Char Product<br />

Cost of Power<br />

Value of Char<br />

Labor Cost<br />

Cost of <strong>Coal</strong> Feed<br />

Plant Depreciation<br />

Maintenance Cost<br />

Annual Operation<br />

Capital Cost<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

MWh/h<br />

tonnes/h<br />

tonnes/h<br />

$/MWh<br />

$/tonne<br />

$/h<br />

$/tonne<br />

%<br />

% of TIC<br />

hours<br />

20<br />

50<br />

35.8<br />

50<br />

29<br />

25<br />

10<br />

10<br />

3<br />

8000<br />

$30 Million<br />

JWTechnologies


TORBED Reactor Pro Forma Economics<br />

Power Sales—20 Sales 20 MWe<br />

@ $50/MWh<br />

Char Product Sales— Sales<br />

286,400 tpa @ $29/t<br />

Operating Costs<br />

Net Estimated Revenue<br />

Return on Investment<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

$ 8,000,000 per year<br />

$ 8,305,600 per year<br />

$ 8,900,000 per year<br />

$ 7,405,600 per year<br />

~25%<br />

JWTechnologies


TORBED Reactor used with VAM & Low<br />

Quality <strong>Gas</strong> for Calcination of Lime<br />

• VAM used as air supply<br />

• Low quality gas injected into reactor above<br />

blades<br />

• Ground limestone processed at 800 oC • <strong>Coal</strong> fines may be used to compensate for<br />

variability in low quality gas feed<br />

• Example flowsheet follows..<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


TORBED Reactor CMM and Lime<br />

Calcination<br />

WATER<br />

CRUSHED<br />

LIME<br />

LOW<br />

QUALITY<br />

GAS<br />

VAM<br />

HEAT<br />

EXCHANGER<br />

OR WASTE<br />

HEAT BOILER<br />

TORBED<br />

COMBUSTOR<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

LIME CALCINATION<br />

PROCESS<br />

FLOW DIAGRAM<br />

STEAM TURBINE<br />

BAG<br />

FILTER<br />

POWER FOR SALE<br />

FAN STACK<br />

POWDERED LIME FOR SALE<br />

JWTechnologies


TORBED Reactor can be used to burn<br />

VAM in Combination with Low Quality CH 4<br />

• An Example: Combust 8% CH 4, , using VAM (0.5%<br />

CH 4) ) as combustion air/ lean fuel and circulate an<br />

inert alumina bed (Al 2O3 )<br />

• Alumina bed becomes a circulating heated mass<br />

which helps maintain the temperature in the<br />

reactor and diffuses the 8% CH 4 so that<br />

combustion is stable (non-explosive)<br />

(non explosive)<br />

• All methane is consumed and resulting heat<br />

energy can be used to generate electricity and run<br />

a heat pump to cool mine intake air<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

JWTechnologies


Example Low Quality CMM TORBED<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

Demo<br />

• 3.5 m diameter TORBED Operating<br />

temperature: 800 oC • VAM Feed to: 0.5% CH 4@ @ 18.6 m 3 /s<br />

• CMM Feed to TORBED: 8%CH 4@ @ 10.0 m 3 /s<br />

• <strong>Energy</strong> converted to Power = 5.70 MW<br />

• Available for Chiller Circuit = 6.87 MW<br />

• Total Power + Heat = 12.57 MW<br />

JWTechnologies


Low Quality CMM and VAM Utilization<br />

LOW<br />

QUALITY<br />

GAS<br />

10 am 3 /sec<br />

8%CH 4<br />

FAN<br />

VAM 18.6<br />

am 3 /sec<br />

0.5% CH 4<br />

Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

Process Flow Diagram<br />

800 O C<br />

TORBED<br />

REACTOR<br />

BOILER<br />

TURBO-<br />

GENERATOR<br />

INDUCTED<br />

AIR<br />

GROSS THERMAL INPUT<br />

FROM METHANE 33 MW.<br />

NET CO2 REDUCTION<br />

337,000 TONNES/YEAR<br />

~<br />

5.7 MWe<br />

HEAT<br />

EXCHANGER<br />

250 O C 70 O C<br />

CHILLER<br />

6.9 MW<br />

FAN<br />

FAN<br />

SUFFICIENT FOR ~73<br />

am 3/ sec AIR COOLED<br />

FROM 90 % RH and 35 O C<br />

TO 60 % RH and 18 O C<br />

STACK<br />

TO MINE<br />

JWTechnologies


Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

<strong>Energy</strong> Converted<br />

• <strong>Energy</strong> converted to Power = 5.70 MW<br />

• Available for Chiller = 6.87 MW<br />

• Can chill air <strong>from</strong> ambient of 35 oC C to 18o 18 C @ 50 m3 m /s<br />

• Relative humidity is reduced <strong>from</strong> 100% to 90%<br />

• Total Power + Heat = 12.57 MW<br />

• (Ambient conditions make a difference in performance. For<br />

example, if the total cooling duty is 4.5 MW, 3.5MW is used in<br />

removing the humidity <strong>from</strong> the intake air, only 1 MW is used for fo<br />

cooling the de-humidified de humidified air. Therefore, without high moisture<br />

content, condensation heat load would be reduced and more<br />

ventilation air could be cooled through the same temperature<br />

range.)<br />

• Cost for complete plant is estimated at $800,000 to<br />

$1,000,000 per MW installed<br />

JWTechnologies


Emission Reduction<br />

Credits Revenue<br />

@ $5.00/t CO 2e Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

Pro Forma Economics<br />

Value of Power Displaced<br />

@ $50/MWh<br />

Value of Heating/Cooling<br />

@ $5.00 GJ/h<br />

Total Estimated Annual<br />

Revenue<br />

$1,506,426 per year<br />

$2,495,752 per year<br />

$1,082,978 per year<br />

$5,085,156<br />

JWTechnologies


Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

Conclusions<br />

• Significant deposits of waste coal exist that could be<br />

exploited. <strong>Waste</strong> gas in three low quality forms could<br />

be utilized at coal mines<br />

• To date a number of issues have inhibited the<br />

successful exploitation of these resources at mine-<br />

sites<br />

• Technology is available that permits separate or co­- co<br />

processing of these materials for generation of power<br />

or for heating/cooling for mine applications<br />

• The TORBED reactor enables efficient solids<br />

processing & combustion of reject coal fines or<br />

wastes. Flame dissipation can assure safe release of<br />

the fuel value of low quality gas<br />

JWTechnologies


Western States <strong>Coal</strong> Mine Methane Recovery and Use Workshop<br />

John G. Whellock Ph.D.<br />

JohnW@JWTechnologies.com<br />

(303) 773-2995 773 2995<br />

Thank you<br />

JWTechnologies

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