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Launching of the second European Climate Change Programme (ECCP II) Stakeholder Conference Brussels 24th October 2005 Lars Strömberg Vattenfall AB Stockholm/Berlin © Vattenfall AB Who’s got the problem ? © Vattenfall AB 2 CO2 free power plant ECCP I - experiences © Vattenfall AB 3 Cost and Potential of options to reduce CO2 emissions Principal example Cost for carbon dioxide avoidance Solar [EUR/ton CO2] Wind 100 Hydro Biofuel Late change coal Reforestation CO2 sequestration Oil to gas 50 Coal to coal Coal to gas Potential [Percent] 0 0 20 40 60 80 The picture will look different when different time perspectives are adopted 2000-07-16 © Vattenfall AB Lars Strömberg Vattenfall AB 4 100 Reductions of CO2 – What ECCP 1 gave • The ECCP 1 work identified a number of measures which could to be taken. • Without agreement among all, it was concluded that almost 30 % reduction could be reached at a cost below 50 €/ton CO2 – – – – – © Vattenfall AB Change from coal to gas Introduce more efficient coal power technology Wind power Biofuels, especially in the heat sector More CHP 5 Cost and Potential of options to reduce CO2 emissions until 2010 Derived from ECCP Energy Supply Preliminary report. Cost for carbon dioxide avoidance Solar [EUR/ton CO2] 100 Wind Coal to Coal CHP Biomass heat CO2 sequestration Coal to gas 50 Biomass heat Potential [Percent] 0 0 20 40 60 Methane mines © Vattenfall AB 6 80 100 Reductions of CO2 – What we have learned (2) • Now, after 4 years we have learned a few things: – We will remain to be dependant on fossil fuels for a long time – Change from coal to gas has not happened • Due to high gas prices and lack of long time confidence – Building new efficient coal - yes • Several large plants have been built and at least seven large units under way. – Wind power has severe limitations • Cost lies about 70 – 90 €/MWh • When capacity (MWs) exceeds about 10 % in an area, the system cannot take any more, need for extra transmission and reserve power • 39 000 MW wind leads to that conventional power can only be reduced 2 500 MW according to one study © Vattenfall AB 7 Reductions of CO2 – What we have learned (3) – Biofuels are used, especially in the heat sector. • All district heat and CHP is using biofuel in Sweden today (140 TWh fuel) • To maintain competitiveness for bio fuels, it is necessary to keep CO2 tax in parallel with the trading system, at a level of 75 €/ton of CO2 • Biofuel usage has reached its limit in Sweden. 45 % of the fuel is imported from Russia, Baltic states and Canada ! – CHP is built wherever possible • Few opportunities left © Vattenfall AB 8 Reductions of CO2 – What we have learned (3) • Carbon Capture and Storage CCS has gained much recognition and development is going fast. – Many countries have recognized CCS as a powerful tool and have introduced it in their plans to fulfill their environmental goals • The USA, UK, Australia, France, Germany among many others – CCS does cost 20 – 25 €/ton CO2 • ECCP 1 assumed 50 €/ton of CO2 – Storage capacity exceeds the remaining fossil fuel reserves – Storage in geological formations is available all over the world, all over Europe, off-shore and on-shore – CCS will not be available in a large scale until 2015 –2020 • ECCP 1 assumed before 2010 – CCS can probably reach half of the mitigation necessary to reach our long term goals of 60 – 80 % of reduction until 2050 © Vattenfall AB 9 Emission Trading Emission Trading sets the commercial framework for new technology in Europe © Vattenfall AB 10 European CO2 trading system Sept. 2005 © Vattenfall AB 11 Allocations in the European trading system In total 12 000 units is included in the trading system. In the National allocation plans 2 100 Mton/year or 6300 Mtons for three years have been distributed. This is the roof set for emissions. The deficit is calculated to 180 Mton for 3 years. The power industry has a deficit of 360 Mton. Other sectors have an overallocation. Other Cement, Lime, Glass Oil and Gas Metals Pulp and Paper Public Power and Heat Total -100 -50 0 50 100 150 200 Mio. t CO2 © Vattenfall AB 12 250 300 350 400 Marginal cost vs. Reduction of CO2 emissions in EUR/ton CO2 Marginal vs. reduction CO2 emissions Euro/ton Source: ECOFYScost Economic evaluationof of sectorial reduction in objectives for CO2 climate change source: ECOFYS Economic Evaluation of sectorial Emission Reduction Objectives for Climate Change Marginal cost for reduction in Euro/ton CO2 300 250 The price in Sept 2005 is about 24 €/ton CO2 ??? 200 150 100 50 0 0 200 400 600 800 1000 1200 Emission reduction in mio ton CO2 © Vattenfall AB 13 1400 1600 Capture and storage of CO2 Capture and storage © Vattenfall AB 14 The CO2 free Power Plant principle • The principle of capture and storage of the CO2 under ground The CO2 can be captured either from the flue gases, or is the carbon captured from the fuel before the combustion process. The CO2 is cleaned and compressed. Then it is pumped as a liquid down into a porous rock formation for permanent storage. © Vattenfall AB 15 CO2 free power plant Storage and transport © Vattenfall AB 16 Storage of CO2 in a Saline Aquifer under the North Sea CO2-injection into the saline aquifer Utsira. (Source:STATOIL) The Sleipner field. Oil and gas production facilities. (Source: STATOIL ) © Vattenfall AB 17 Storage Capacity, saline aquifers There exists more storage capacity within Eorope (and in the world) than the remaining fossil fuels Source: Franz May, Peter Gerling, Paul Krull Bundesanstalt für Geowissenschaften und Rohstoffe, Hannover © Vattenfall AB 18 CO2 Transport and storage Schweinrich structure Two pipeline transport routes are possible Both routes can be designed to follow existing pipeline corridors >90% Structure can contain 1,4 billion ton of CO2, equivalent to about emissions from 6000 MW their whole lifetime Berlin © Vattenfall AB 19 Reservoir simulation – 40 year model Due to buoyancy, the CO2 strive against the top of the formation The CO2 spreads in the whole reservoir Conclusion: It is possible to inject 400 Mt CO2 Injection at flanks © Vattenfall AB 20 Geological structure modelling. Schweinrich © Vattenfall AB 10 years 200 years 500 years 2000 years 5000 years 10000 years 21 CO2 free power plant Capture © Vattenfall AB 22 Post-combustion capture This technology is already commercially available in large scale (500 MW). It is at present the most expensive © Vattenfall AB 23 Pre-combustion capture This technology needs development. Might be competitive. The gasifier exists in demo plants. The turbine is in the lab stage. Produces Hydrogen as an intermediary product © Vattenfall AB 24 O2/CO2 combustion is the preferred option at present At present the most competitive and preferred technology for coal. It needs development, pilot and demo plants to get design data © Vattenfall AB 25 © Vattenfall AB G HG PF G HG 20 0 IE PF 4 n A o G HG 20 ca 04 IE pt PF A ur p o e G st HG 20 c 20 om n b. M PF its 20 o c a ui 20 p 20 po ture 0 s 4 M PF tco its m u n i2 b M its 00 o ca . ui 4 O p tur 20 2/ e 2 C 0 IE M O PF A its 2 G u PF no HG i 2 0 c IE 2 a IG 0 A O p tur CC G 2/ e H C IE 2 G A IG 0 03 O2 G CC PF no H IE G I 20 ca G A pt 03 C G pr u re HG C 2 e IG 0 20 - co CC no mb . c 20 20 a ptu EN re p CA rec o P PF mb IE . O A O xy Lig xy G ni fu HG fu te e el IE 20 A wi l W FG G 0 th HG 4 D NG out IE 20 A W C F G 0 C G HG 4 D NG n o IE ca 20 A pt G 2 0 CC ur HG NG p o e st 2 C c 0 M o 2 C m its 0 b. ui NG n o c 20 C a pt M 04 N C p ur its o e G st ui co 20 CC no mb 04 ca . O 2/ pt C ur O e 2 NG CC IE A IE A COE [EUR/MWhe] Total generation cost of electricity with CO2 penalty 70 Hard Coal Lignite 26 Natural gas 60 50 40 CO2 penalty 30EUR/T CO2 penalty 20EUR/T 30 CO2 penalty 10EUR/T COE 20 10 0 Generation cost with and without CO2 capture 60 Hard Coal Lignite Natural gas 50 COE [EUR/MWh] 40 COE penalty 30 COE origninal 20 10 0 IEA GHG PF 2004 postcomb. © Vattenfall AB IEA GHG Mitsui 2004 Mitsui 2020 IEA GHG IEA GHG PF 2020 O2/CO2 PF O2/CO2 PF IGCC 2003 IGCC 2020 postcomb. pre-comb. pre-comb. Oxyfuel WFGD 27 Oxyfuel without WFGD IEA GHG IEA GHG Mitsui 2004 2004 NGCC 2020 NGCC O2/CO2 postcomb. postcomb. NGCC Electricity generation costs 60,0 Electricity production cost EUR/MWh 50,0 Fuel and consumables Fixed O&M + additional op costs Running O&M 40,0 30,0 Capital costs EUR/MWh 20,0 10,0 0,0 PF © Vattenfall AB CC PF oxyfuel 28 CC CO2 capt. Generation costs incl. CO2 costs (20 €/ton) 60,0 Electricity Production cost EUR/MWh 50,0 40,0 CO2 penalty Fuel and consumables Fixed O&M + additional op costs Running O&M 30,0 20,0 Capital costs EUR/MWh 10,0 0,0 PF © Vattenfall AB CC PF oxyfuel 29 CC CO2 capt. Avoidance costs of CO2 60,0 Avoidance costs 50,0 40,0 Avoidance cost €/ton CO2 CO2 penalty Fuel and consumables Fixed O&M + additional op costs Running O&M Capital costs EUR/MWh 30,0 20,0 10,0 0,0 PF with CO2 capture © Vattenfall AB Gas CC with CO2 capt 30 Cost and Potential of options to reduce CO2 emissions Principal example Cost for carbon dioxide avoidance New Picture 2005 including recent knowledge Solar [EUR/ton CO2] Wind 100 Biofuel El Hydro Savings New efficient coal Biofuel Heat Oil to gas CO2 Capture and Storage 50 Coal to gas Potential [Percent] 0 0 20 40 60 2000-07-16 © Vattenfall AB Lars Strömberg Vattenfall AB 31 80 100 Conclusions from analysis - Reduction of CO2 • Carbon capture and storage from Coal fired Power plants can be done at a cost close to 20 €/ton CO2 – Capture at about 15 €/ton of CO2 – Storage at lower than 2 €/ton CO2 – Transport depending on distance and volume, but 5 €/ton of CO2 for large plants on shore • More than enough storage capacity on shore and off shore is at hand in saline aquifers • Technology choice is not yet made. Oxyfuel is preferred technology in Vattenfall at present • The commercial choice stands between Gasfired CC without CCS, taking the penalty of CO2 emission, and Coal fired plants with CCS Lars Strömberg AB © VattenfallVattenfall AB Corporate Strategies 2003 07 05 32 Taking responsibilty • Lord Oxburgh, former chairman of Shell Transport and Trading: "CCS is absolutely essential if the world is serious about limiting greenhouse gas emissions“ • The new report from the Intergovernmental Panel on Climate Change (IPCC) concludes: “CCS could achieve more than half of the emissions reductions necessary to mitigate climate change up to 2100” Vattenfall agrees with this. We also believe CCS is needed to fulfill our climate goals © Vattenfall AB 33 CO2 free power plant Back up © Vattenfall AB 34 The Climate Change • The Climate Change problem is for real • EU ministers have agreed on, that we have to reduce the emissions to maintain a reasonable CO2 concentration in atmosphere – 15 – 30 % until 2030 – 60 – 80 % until 2050 • A radical solution is necessary. We cannot wait © Vattenfall AB 35 CO2 storage cost Storage at Schweinrich of 10 Mton CO2 per year over 40 years: Fictive cost calculations using tool developed in EU-funded GESTCO project: © Vattenfall AB 36 CO2 transport cost: Transport to Schweinrich from Schwarze Pumpe power plant: Distance 320 km 10 Mton CO2 per year over 40 years: 7,00 Opex 6,00 € per ton CO2 5,00 4,00 3,00 Capex 2,00 1,00 0,00 €/ton Left: 25 years, 7,5% © Vattenfall AB €/ton Right: 10 years, 10% 37 CO2 free power plant Pilot Plant © Vattenfall AB 38 Construction area © Vattenfall AB 39 Boxberg IV Why Oxy-fuel technology ? We work with all three (four) technologies, but: • • • © Vattenfall AB Oxyfuel technology is the technology giving lowest costs at present It is suitable for coal and have relatively little development work left We can build on our good experience with present PF technology 40 CO2 free power plant Analysis of some technology options © Vattenfall AB 41 CO2 Free Power Plant: Technology Choice The ultimate technology choice is not clear yet. Several technologies will probably be applied to different commercial situations. • Post combustion capture. – At present the most expensive option but commercially available in large size. – Can be applied to existing plants. – Needs no demo. Optimization of existing options needed. • Pre combustion capture. – The most complicated technology. IGCC demos have not been successful – Produces hydrogen as integrated intermediate fuel for the power process, from coal or gas. – Development need for the gas turbine run on hydrogen – Lab tests + pilot + demo • CO2/O2 (oxy-fuel) capture – The most preferred option at present – Technology straight forward and builds on the modern supercritical coal fired boilers – Tests in technical scale positive. Needs pilot plant and demo plant • Chemical Looping technology is the most interesting long term option. – Lab experiments very encouraging. © Vattenfall AB 42 Options for reduction of CO2 • Specific data for the plants Specific Investment costs €/kWe PF CC PF oxyfuel CC with capture 1000 550 1425 938 140 100 720 405 180 95 36,5 49 Additional investment mio € Power output MW 900 500 Energy penalty MW Efficiency % Lars Strömberg AB © VattenfallVattenfall AB Corporate Strategies 45 60 2003 07 05 43 Options for reduction of CO2 • Common data used for the four plants: Coal Price 50 $/ton ~ 5,7 €/MWh Gas price 13 €/MWh Depreciation time 25 years Interest rate © Vattenfall AB 10% 44 The Problem • Fossil fuels are needed – Analysis show that fossil fuels will remain as major energy source in 2030 ( 85 %) • The top priority is to introduce renewable energy sources in the energy system – All analysis show that renewable energy sources will play a large role, but not large enough and soon enough • In several countries nuclear power is decommissioned • No renewable energy source not known today can play a significant role in 25 years from now, i.e. 2030 • © Vattenfall AB Emissions from fossil fuels must be reduced 45 Schwarze Pumpe power plant © Vattenfall AB 46