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1MEGTEC Confidential
The Power of VAMThe Power of VAM - technology application update
For Methane to Markets
in Cagliari 29 April 2008
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The Power of VAM - technology application update
UUPPDDAATTEE HHEEAADD LLIINNEESS
• Update on VVAAMM ttoo EElleeccttrriicciittyy at WestVAMP, Australia
• Update on VVAAMM AAbbaatteemmeenntt at CONSOL, USA • Update on VVAAMM ttoo TThheerrmmaall EEnneerrggyy • Next steps
• VAM reduction potentials
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WestVAMP by April 2008 - in full operation since over 1 year
• 250 000 Nm3/h (150 000 scfm) of ventilation air with • 0.9% CH4 concentration (VAM + drainage gas) generating • High pressure, superheated steam (60 bar, 460oC)driving a • Conventional 6 MWe power plant steam turbine
Fuel contains ~ 99% air
Fuel contains ~ 99% air
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WestVAMP by April 2008 - in full operation since over 1 year
Reported to in first year of operation have generated 220 000 t CO2e from reducing VAM emissions and an additional 30 000 t CO2e from replacing energy (with more CO2 efficient energy source)
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WestVAMP by April 2008 - in full operation since over 1 year
Officially opened on 14 September 2007 by the Premier of NSW.
The Project is partly Government funded by the AGO (Australian Greenhouse Office)
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Honorable awards
- for WestVAMP
• Aug 2007; Highly Commended in Excellence Awards 2007 of NSW Minerals Council • Sept 2007; WestVAMP received the Excellence in Energy Award 2007 by the Australian Institute of Energy
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Windsor mine, West Liberty site, West Virginia
CONSOL Energy, USA
� Simulating various concentrations of VAM by injecting high concentration (35-50%) Abandoned Mine Gas into …
� 50 000 m3/h (30 000 scfm) of fresh air
� Unmanned operation since May 2007
� Rebuilt in April 2008 for improved availability, presently being re-started
The Project is partly Government funded by the US EPA and the US DOE
FC
CH4 CH4
VOCSIDIZER™
CMM
35 – 50 %
CH4
0.1 – 1.2
US VAM Project at CONSOL Energy, USA
% CH4
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VAM to Thermal Energy - for District Heating / cooling
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THREE OPTIONAL VAM VOCSIDIZER CONCEPTS
A
VAM Abatement Only
B
VAM to Thermal Energy
VAM Power Plant (VAM to Electrical Energy)
~
VOCSIDIZER™
Steam drum Deaerator
FW tank
TurbineGenerator
Condenser
FW treatment plant
Air cooler C
VAM to Energy
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Next steps
• Based on experience in VAM application now prepared to roll out installations on broad basis
• Mostly Abatement or VAM to Thermal Energy • Large number of prospects mainly in China, but also in Australia, Europe and in the Americas
• Plan to start production in China within a year
• When ready to release info on progress, will do so via M2M.
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The formula will be:[Cleaning Efficiency] x [Hours of availability] x [Volume flow of ventilation air] x [VAM concentration] x [(CH4 weight) x Global Warming factor (CO2 weight)]
which comes to:0.97 x [8760x0.97] x [Flow of ventilation air] x [VAM concentration] x [ 0.71 x ( 21 2.75)]
Calculations of CERs
For calculation of amount to CERs, consider; - Vocsidizer cleaning efficiency and availability - conversion rate of CH4 into CO2e.
–
–
The formula will be: [Cleaning Efficiency] x [Hours of availability] x [Volume flow of ventilation air] x [VAM concentration] x [(CH4 weight) x Global Warming factor – (CO2 weight)]
which comes to: 0.97 x [8760x0.97] x [Flow of ventilation air] x [VAM concentration] x [ 0.71 x ( 21 – 2.75)]
Examples:
250 000 Nm3/h @ 0.9 % VAM comes to 240 000 tonnes of CO2e
125 000 Nm3/h @ 0,9 % VAM comes to 120 000 t CO2e
125 000 Nm3/h @ 0,3 % VAM comes to 40 000 t CO2e
120 80 40 125 000
640
320
160
0.6
320
160
80
0.3
960 1 000 000
480 500 000
240 250 000
0.9
Thousand tons of CO2e per year
IN ADDITION at energy recovery : If carbon based energy is replaced, the effect on Global Warming is ~20% better.
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The aim of all efforts to reduce GHG emissions
is now to bbrreeaakk tthhee ttrreenndd
ooff iinnccrreeaassiinngg gglloobbaall wwaarrmmiinngg,
which is melting the ice of the Arctic.
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The aim of all effortsto reduce GHG emissions
is now to break the trendbreak the trend
of of increasingincreasing global global warmingwarming,
which is melting the ice of the Arctic.