Energy from Waste Gas & Reject Coal
Energy from Waste Gas & Reject Coal
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