JP2010516606A - C02捕獲ユニットと合体した発電所での加圧c02流の製造方法 - Google Patents
C02捕獲ユニットと合体した発電所での加圧c02流の製造方法 Download PDFInfo
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- B01D53/34—Chemical or biological purification of waste gases
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- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
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- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
- F01K23/10—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
- F01K23/10—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
- F01K23/106—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle with water evaporated or preheated at different pressures in exhaust boiler
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D2256/22—Carbon dioxide
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- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
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Abstract
【選択図】図1
Description
(a)ガスタービンを出る熱排気ガスを熱回収水蒸気発生器ユニットに導入して、第一量の水蒸気と、CO2含有煙道ガス流とを生成する工程、
(b)該煙道ガス流を吸収器中で吸収性液体と接触させて、CO2に富む吸収性液体及び精製煙道ガスとし、これによりCO2含有煙道ガス流からCO2を除去する工程、
(c)該CO2に富む吸収性液体を、再生器中、高温でストリッピングガスと接触させて、再生吸収性液体、及びCO2に富むガス流を得る工程、
(d)CO2圧縮機を使用して該CO2に富むガス流を加圧する工程、
を含み、該熱回収水蒸気発生器ユニットで生成した水蒸気の第一部分を該CO2圧縮機の駆動に使用することを特徴とする該方法を提供する。
熱回収水蒸気発生器ユニットは、熱排気ガスから熱を回収すると共に、この熱を水蒸気に変換するための手段を備えたユニットである。例えば熱回収水蒸気発生器ユニットは、層状に載せた複数の管を備えることができる。水をポンプ送りし、管中を循環させ、高温高圧下に保持できる。熱排気ガスは管を加熱して、水蒸気を生成するのに使用される。
好適な化学溶剤としてはアンモニア及びアミン化合物が挙げられる。
一実施態様では、吸収性液体は、モノエタノールアミン(MEA)、ジエタノールアミン(DEA)、ジグリコールアミン(DGA)、メチルジエタノールアミン(MDEA)及びトリエタノールアミン(TEA)の群から選ばれた1種以上のアミンを含む。MEAは、CO2を比較的高い割合(MEA 1容量当たりCO2容量)で吸収する能力を有するため、特に好ましいアミンである。したがって、MEAを含む吸収性液体は、低濃度、通常、3〜10容量%のCO2を有する煙道ガスからCO2を除去するのに好適である。
N,N,N’N’−テトラキス(ヒドロキシアルキル)−1,6−ヘキサンジアミンは、好ましくはN,N,N’N’−テトラキス(2−ヒドロキシエチル)−1,6−ヘキサンジアミン及び/又はN,N,N’N’−テトラキス(2−ヒドロキシプロピル)−1,6−ヘキサンジアミンである。
更に他の一実施態様では吸収性液体はN−エチルジエタノールアミン(EDEA)を含む。
特に好ましい実施態様では、吸収性液体はアンモニアを含む。
熱回収水蒸気発生器ユニットでの燃焼に好適な燃料としては、天然ガス及び合成ガスが挙げられる。
以下に本発明を添付の図1を参照して、単に例示により説明する。
2 熱回収水蒸気発生器ユニット
3 CO2捕獲ユニット
5 圧縮機
7 燃焼器
8 第一膨張器
9 発電機
13 第二膨張器
15 水蒸気タービン
16 発電機
18 アミン系吸収器
21 再生器
24 CO2圧縮機
25 シャフト
Claims (10)
- 熱回収水蒸気発生器ユニットと、吸収器及び再生器付きのCO2捕獲ユニットとに連結したガスタービンを少なくとも1つ備える、CO2捕獲ユニットと合体した発電所で加圧CO2流を製造する方法において、
(a)ガスタービンを出る熱排気ガスを熱回収水蒸気発生器ユニットに導入して、第一量の水蒸気と、CO2含有煙道ガス流とを生成する工程、
(b)該煙道ガス流を吸収器中で吸収性液体と接触させて、CO2に富む吸収性液体及び精製煙道ガスとし、これによりCO2含有煙道ガス流からCO2を除去する工程、
(c)該CO2に富む吸収性液体を、再生器中、高温でストリッピングガスと接触させて、再生吸収性液体、及びCO2に富むガス流を得る工程、
(d)CO2圧縮機を使用して該CO2に富むガス流を加圧する工程、
を含み、該熱回収水蒸気発生器ユニットで生成した水蒸気の第一部分を該CO2圧縮機の駆動に使用することを特徴とする該方法。 - 前記熱回収水蒸気発生器ユニットで生成した水蒸気の一部が、CO2圧縮機に連結した膨張器に案内される請求項1に記載の方法。
- 前記熱回収水蒸気発生器ユニットで生成した水蒸気の他の一部を、電力を発生する発電機に連結した水蒸気タービンに案内して、電力を発生させる請求項1又は2に記載の方法。
- 前記膨張器が低圧水蒸気を排出し、該低圧水蒸気が前記吸収性液体の再生に必要な熱の少なくとも一部を供給するのに使用される請求項2又は3に記載の方法。
- (e)第二量の水蒸気を生成するため、前記熱回収水蒸気発生器ユニット中で或る量の燃料を燃焼させる工程であって、該燃料の量は、前記吸収性液体の再生に必要な量の80%以上を供給するのに充分であるような量である該工程を更に含む請求項1〜4のいずれか1項に記載の方法。
- 前記高圧流が90〜125バール(絶対圧)、更に好ましくは100〜115バール(絶対圧)の範囲の圧力を有する、及び/又は前記低圧流が3〜8バール(絶対圧)、更に好ましくは4〜6バール(絶対圧)の範囲の圧力を有する請求項1〜5のいずれか1項に記載の方法。
- 前記CO2に富む加圧ガス流は、40〜300バール(絶対圧)、更に好ましくは50〜300バール(絶対圧)の範囲の圧力を有する請求項1〜6のいずれか1項に記載の方法。
- 前記吸収性液体が、アミン、好ましくはモノエタノールアミン(MEA)、ジエタノールアミン(DEA)、ジグリコールアミン、(DGA)、メチルジエタノールアミン(MDEA)、トリエタノールアミン(TEA)、N−エチルジエタノールアミン(EDEA)、N,N’−ジ(ヒドロキシアルキル)ピペラジン、N,N,N’,N’−テトラキス(ヒドロキシアルキル)−1,6−ヘキサンジアミン及びt−アルキルアミンスルホン酸化合物よりなる群から選ばれた1種以上のアミンである請求項1〜7のいずれか1項に記載の方法。
- 前記吸収性液体が物理溶剤、好ましくはポリエチレングリコールのジメチルエーテルを含む請求項1〜8のいずれか1項に記載の方法。
- 前記吸収性液体がアンモニアを含む請求項1〜7のいずれか1項に記載の方法。
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Application Number | Priority Date | Filing Date | Title |
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EP07101145 | 2007-01-25 | ||
PCT/EP2008/050734 WO2008090167A1 (en) | 2007-01-25 | 2008-01-23 | Process for producing a pressurised co2 stream in a power plant integrated with a co2 capture unit |
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JP2009546746A Withdrawn JP2010516606A (ja) | 2007-01-25 | 2008-01-23 | C02捕獲ユニットと合体した発電所での加圧c02流の製造方法 |
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US (1) | US8613794B2 (ja) |
EP (1) | EP2125164A1 (ja) |
JP (1) | JP2010516606A (ja) |
CN (1) | CN101622051A (ja) |
AU (1) | AU2008208881B2 (ja) |
CA (1) | CA2676078A1 (ja) |
WO (1) | WO2008090167A1 (ja) |
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2008
- 2008-01-23 WO PCT/EP2008/050734 patent/WO2008090167A1/en active Application Filing
- 2008-01-23 EP EP08708099A patent/EP2125164A1/en not_active Ceased
- 2008-01-23 CN CN200880006106A patent/CN101622051A/zh active Pending
- 2008-01-23 CA CA002676078A patent/CA2676078A1/en not_active Abandoned
- 2008-01-23 US US12/524,175 patent/US8613794B2/en not_active Expired - Fee Related
- 2008-01-23 AU AU2008208881A patent/AU2008208881B2/en not_active Ceased
- 2008-01-23 JP JP2009546746A patent/JP2010516606A/ja not_active Withdrawn
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011080464A (ja) * | 2009-10-05 | 2011-04-21 | General Electric Co <Ge> | 炭素隔離を含む方法及びシステム並びにエンジン |
JP2013533426A (ja) * | 2010-07-28 | 2013-08-22 | サーガス エーエス | 炭素捕捉を有するジェットエンジン |
JP2013540229A (ja) * | 2010-10-05 | 2013-10-31 | アルストム テクノロジー リミテッド | Co2捕捉を備えたコンバインドサイクル発電所及びこれを運転する方法 |
Also Published As
Publication number | Publication date |
---|---|
AU2008208881B2 (en) | 2011-06-09 |
EP2125164A1 (en) | 2009-12-02 |
US20100139484A1 (en) | 2010-06-10 |
CA2676078A1 (en) | 2008-07-31 |
AU2008208881A1 (en) | 2008-07-31 |
WO2008090167A1 (en) | 2008-07-31 |
CN101622051A (zh) | 2010-01-06 |
US8613794B2 (en) | 2013-12-24 |
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