COGEN Europe 15th Annual Conference 2009 The future of large cogeneration plants in Europe Stéphane Grée Air Liquide
Renaissance Hotel, Brussels – April 22nd, 2009
Agenda
Development of Cogeneration in Air Liquide Group Air Liquide references in the Chemical Industry Cogeneration Projects Opportunities Ways to Create Value Steam Turbine Generator to expand “fatal” steam Basin : Botlek (R’dam-NL) Basin : Bayport (TX-USA) Fire non conventional fuels in gas turbine Make flexible and “independent” the power and steam production Fresh air retrofit of existing plants Pergen (R’dam-NL) Conclusion : The future of large cogeneration plants in Europe
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Development of Cogeneration in Air Liquide Group Expanded offer to AL core business clients Efficiency improvement in a sustainable way Tailor made cogeneration plant to satisfy the needs Scale effect aggregating several clients in a basin AL investment allows customers to focus on their core business
Natural Gas
Natural gas
H2
H2 / CO
CO
Energy Providers
Cogen
steam
AL Industrial Clients
air gases
Electricity
ASU
Electricity
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Air Liquide references in the Chemical Industry
HUNTSMAN 1997 ENECAL LYONDELL/HUNTSMAN 1995 EUROGEN SHELL 2008 PERGEN RHODIA 1999 COGENAL Belle Etoile Utilités
DOW 1999 Saskatchewan
SHELL 1999 Scotford
LYONDELL/EQUISTAR... 1985 Bayou
HUNTSMAN 1993 Port Neches
BASF 1999 Geismar
SOLVAY 1998 SOLAL
INEOS/NAPHTACHIMIE 2000 LAVERA ENERGIES LAVERA UTILITES LYONDELL 1999 FIGENAL
SHELL 2001 Geismar
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Cogeneration Projects Opportunities
New Investment
New requirement / Debottlenecking Replacement of obsolete equipment
Low Efficiency – High Cost of Production
Steam let down / Steam vent Large boilers operating at low steam loads Obsolete technologies with poor efficiency Flaring of excess process gases High cost of grid power
Emission Compliance
Implementation of new environmental regulations CO2 emission reduction target Subsidies mechanism
Poor Reliability or Flexibility
Weak Grid supply Base load power production associated to a stable steam demand
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Ways to Create Value
Implement Steam Turbine Generator
Replace steam static let down Design with higher steam pressure/temperature than the needs Expand “fatal” steam (e.g. from Steam Methane Reformer)
Combine steam hosts to create a larger steam network
Scale and efficiency effect Stranded assets available at one site to serve another customer (shared back-up)
Comply with new emissions regulations
Gasification of waste liquid fuels and syngas cogeneration Fire non conventional fuels in gas turbine or duct burner Natural gas cogeneration to replace Heavy Fuel Oil Boilers
Flexibilize steam and power production
Follow power market and steam demand by changing cogeneration plant load Make as much as possible independent the production of steam and power
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Steam Turbine Generator to expand “fatal” steam
Co-production of electricity in a SMR plant :
Design with higher steam temperature Implement back-pressure steam turbine down to LP steam export Implement condensing steam turbine to expand further steam not taken by steam client
Better valorization of “fatal” steam :
Avoid static let down Avoid steam vent
CO2 saving :
Case 100% LP steam export 6.2 gCO2/Nm3H2 Case 50% LP steam export 29.2 gCO2/Nm3H2
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Basin : Botlek (R’dam-NL)
Multi-products plant located in the center of the Port of Rotterdam Possible extension of steam network to other customers Difficulty due to crowded pipe ways and safety of steam transportation on public area
Power: 3 x GE 6B Gas Turbines, 40 MWe each Steam: 3 x HRSGs 135t/h 75barg capacity 1 condensate treatment unit 2 demineralized water units Customers: serving 2 steam&power clients, 1 power grid off-taker in the basin Steam (HP, MP), more than 1.6km P/L Electricity Industrial gases : Syngas, H2, CO Connected to the AL northern Europe H2 pipeline
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Basin : Bayport (TX-USA)
Power: 4 x GE 7E Gas Turbines, 62 MWe each Steam: 4 x HRSGs, 3 x boilers 2.7 mmlb/h 800 psig capacity Treated Water: 15 million GPD Demin Water : 4.8 million GPD Customers: serving 35 in the basin Steam (HP, LP), more than 3 miles P/L Industrial gases O2, N2, H2 Demin water Industrial water Electricity
Cogeneration plant commissioned in 1985 Gas turbines approach end of life time
Huge refurbishment costs ? Replacement ?
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Fire non conventional fuels in gas turbine
IGCC like : Convert refinery liquid waste fuels into synthetic gas for producing steam and power in a cogeneration instead of conventional power plant Fire Refinery Fuel Gas in DLN gas turbine
Refinery fuel gas contains H2 and olefins which have been hardly allowed in DLN gas turbine so far A new generation of DLN gas turbine is or will soon be able to burn such fuel Advantages :
• Get rid of waste fuel gases instead of flaring • To get steam and power with excess non costly fuels • Low emissions
• • NOx kept in the same order of magnitude than with natural gas fuel CO2 emissions similar to natural gas : CO2 from olefins combustion is balanced by H2
Natural gas cogeneration to replace Heavy Fuel Oil Boilers
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Make flexible and “independent” the power and steam production The industrial cogeneration which mainly sells electricity to the grid must adapt its production to the power market volatility Steam consumption While producing stable steam flow 700 And vice versa
650 Steam flow (t/h) 600 550 500 450 400 350 janv.-07 févr.-07 avr.-07 mai-07 juil.-07 sept.-07 oct.-07 déc.-07
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Make flexible and “independent” the power and steam production
Cogeneration plant operation
Operation time :
• Peak/offpeak :
• Ideal match with power market • Need of auxiliary steam production
• Week/weekend :
• Good match with power market but offpeak night time to be compensated • Need of auxiliary steam production during weekend
• Winter :
• Play with power load to match with power market • Need of auxiliary steam production during summer
• Year :
• Play with power load to match with power market • Need of auxiliary steam production during summer
Power load :
• Start/stop :
• Gas turbine : increased maintenance costs, reduced lifetime • HRSG : reduced lifetime, continuous steam supply requires auxiliary boiler • To compensate start-up costs
• Partial to base load
• Increased NOx emissions, reduced efficiency
• Base load
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Fresh air retrofit of existing plants
Existing cogeneration plants can be retrofitted to fresh air firing and flue gas recirculation :
Allows continue making steam while gas turbine is stopped or has decreased load for following power market
Fresh air retrofit + flue gas recirculation
GT outlet GT outlet Air Liquide, the world leader in gases for industry, health and the environment 13
Pergen (R’dam-NL) : Innovative concept, high efficiency
Power: 2 x GE 9E Gas Turbines, 130 MWe each Steam: 4 x split boilers, 800 t/h 85 barg capacity Back-pressure turbines : 55 MWe capacity Demin Water Unit : 1400 m3/h capacity Steam customer : Steam (HP, MP, LP) : 520 t/h Electricity : 30 MWe Demin water : 800 m3/h Compressed air, hot water Waste heat recovery Grid customer : 250 MWe
86% net efficiency
Start-up 2008
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Pergen (R’dam-NL) : Flexibility, reliability Flexible concept
Fresh air and flying take over (FTO) Gas turbines runs between 60 and 100%load to match power market needs Flue gas recirculation :
• Reduction of NOx emissions in Fresh air mode • Keep steam capacity at gas turbine part load
4 HRSG’s : steam reliability
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Pergen (R’dam-NL) : Low emissions
The emission situation in the Netherlands led to the “emission reduction plan”, which engaged industrial actors into emissionreduction measures
Current Equivalent Situation
High Sulphur Residues fired Boilers of 560tph HP steam Equivalent Dutch fossil fuelled power plant of 243MWe 275 t/y 982 t/y 1066 kt/y Total
Pergen
Total
SO2 NO2 CO2
8226 t/y 2745 t/y 1413 kt/y
8501 t/y 3727 t/y 2479 kt/y
0 t/y 852 t/y 1561 kt/y
NO2 concentration, source: ESA
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CONCLUSION : The future of large cogeneration plants in Europe
New and Existing Cogeneration plants must be characterized by :
High Flexibility High Efficiency Low Emissions
If necessary, existing cogeneration plants must be retrofitted to cope with above mentioned characteristics They should receive at least the same CO2 allocations than equivalent production plant :
Industrial fired boilers Combined cycle power plant
Current economic crisis is an opportunity for the development of cogeneration in Europe :
Reduced investment costs Reduced equipment fabrication time Requirement for energy savings for a better competitiveness vs developing countries
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COGEN Europe 15th Annual Conference 2009
THANK YOU FOR YOUR ATTENTION
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