JP2011106295A - 熱電気水素供給システム - Google Patents
熱電気水素供給システム Download PDFInfo
- Publication number
- JP2011106295A JP2011106295A JP2009259349A JP2009259349A JP2011106295A JP 2011106295 A JP2011106295 A JP 2011106295A JP 2009259349 A JP2009259349 A JP 2009259349A JP 2009259349 A JP2009259349 A JP 2009259349A JP 2011106295 A JP2011106295 A JP 2011106295A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- hydrogen
- steam
- lng
- supply system
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
- F25J3/0605—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the feed stream
- F25J3/0625—H2/CO mixtures, i.e. synthesis gas; Water gas or shifted synthesis gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0204—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the feed stream
- F25J3/0223—H2/CO mixtures, i.e. synthesis gas; Water gas or shifted synthesis gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0252—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of hydrogen
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0266—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of carbon dioxide
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0271—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of H2/CO mixtures, i.e. of synthesis gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
- F25J3/063—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream
- F25J3/0655—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream separation of hydrogen
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
- F25J3/063—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream
- F25J3/067—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream separation of carbon dioxide
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/62—Liquefied natural gas [LNG]; Natural gas liquids [NGL]; Liquefied petroleum gas [LPG]
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/04—Recovery of liquid products
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
- F25J2230/30—Compression of the feed stream
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2270/00—Refrigeration techniques used
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
- F25J2270/904—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration by liquid or gaseous cryogen in an open loop
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/14—Combined heat and power generation [CHP]
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Fuel Cell (AREA)
Abstract
【解決手段】LNGを気化した天然ガスを燃料とするCGSと、天然ガスの水蒸気改質による水素分離型水蒸気改質器と、水蒸気改質用加熱源である燃焼器とを有する熱、電気および水素を供給するシステムであって、(a)CGSからの排ガスと水素分離型水蒸気改質器からのオフガスを合流させ、(b)排ガス及びオフガスをその流れ方向でみて、順次、圧縮機、冷却熱交換器及び気液分離槽を含む二酸化炭素回収装置を備えてなり、(c)冷却熱交換器の冷熱としてLNGを使用し、(d)CGS及び水蒸気改質用加熱源である燃焼器には酸素富化空気を使用し、(e)CGSにて生成した水蒸気を水蒸気改質器で使用するようにしてなる、ことを特徴とする熱電気水素供給システム。
【選択図】図3
Description
(a)前記コジェネレーションシステムからの排ガスと前記水素分離型水蒸気改質器からのオフガスを合流させ、
(b)前記排ガス及びオフガスをその流れ方向でみて、順次、圧縮機、冷却熱交換器及び気液分離槽を含む二酸化炭素回収装置を備えてなり、
(c)前記冷却熱交換器の冷熱として前記LNGを使用し、
(d)前記コジェネレーションシステム及び前記水蒸気改質用加熱源である燃焼器には酸素富化空気を使用するようにしてなる、ことを特徴とする熱電気水素供給システムである。
(a)前記コジェネレーションシステムからの排ガスを前記ヒーターの熱源として使用した後、
(b)前記排ガスと前記水素分離型水蒸気改質器からのオフガスを合流させ、
(c)前記排ガス及びオフガスをその流れ方向でみて、順次、圧縮機、冷却熱交換器及び気液分離槽を含む二酸化炭素回収装置を備えてなり、
(d)前記冷却熱交換器の冷熱として前記LNGを使用し、
(e)前記コジェネレーションシステムには酸素富化空気を使用し、
(f)前記コジェネレーションシステムにて生成した水蒸気を前記水蒸気改質器で使用するようにしてなる、ことを特徴とする熱電気水素供給システムである。
(1)LNGターミナル、LNGサテライトにおいて、熱(温水、水蒸気)、電気、水素、二酸化炭素を高効率に供給することができる。
(2)LNGターミナル、LNGサテライトにおけるコジェネレーションシステムからの天然ガス由来の二酸化炭素の全量もしくは大部分を回収することができる。
(3)LNGの冷熱と水素分離型水蒸気改質器のオフガスとの効率的な熱交換によってLNG気化プロセスとCO2圧縮液化回収プロセスの効率向上を図ることができる。
(4)コジェネレーションシステムにおいてLNG気化器が省略でき、また水素分離型水蒸気改質器を用いた水素製造装置における脱硫器、都市ガス圧縮機、ボイラーを省略することができる。
図1〜2は従来技術を説明する図である。図1はLNGサテライトシステムを説明する図であり、図2は「水素分離型水蒸気改質器を用いた水素製造装置+二酸化炭素(CO2)回収装置」、すなわち水素分離型水蒸気改質器を用いた水素製造装置に二酸化炭素(CO2)回収装置を組み合わせたシステムを説明する図である。
図3は本発明(1)を説明する図である。
図4は本発明(2)を説明する図である。
2 導管
3 熱交換器
4 コジェネレーションシステム(CGS)
5 LNGタンク1からのボイルオフガス排出導管
6 パイプライン
11 都市ガス導管
12 都市ガス導管11からの分岐管
13 脱硫器
14 空気供給管
15 ボイラー
16 ボイラー15への水供給管
17 水素分離型水蒸気改質器
P1、P2 圧縮機
18 燃焼器
21 気液分離器
23 液化炭酸の導出管
31 LNGタンク
33 熱交換器
38 天然ガスを燃料とするコジェネレーションシステム(CGS)
39 空気供給管
40 酸素富化器
41 酸素富化空気の分岐管
44 水素分離型水蒸気改質器45への水蒸気供給管
45 水素分離型水蒸気改質器
46 燃焼器
49 気液分離器
52、53 気相分導出管
61 LNGタンク
62 LNG導管
63 熱交換器
64 天然ガス導管
65 パイプライン
67 天然ガスを燃料とするコジェネレーションシステム(CGS)
68 空気供給管
69 酸素富化器
70 温水、水蒸気等の導出管
71 水素分離型水蒸気改質器72への水蒸気供給管
72 水素分離型水蒸気改質器
73 水素分離型水蒸気改質器72の加熱部
75 オフガス導出管
76 合流ガス導管
77 気液分離器
78 液化炭酸の導出管
79、80 気相分導出管
Claims (5)
- LNGを気化した天然ガスを燃料とするコジェネレーションシステムと、前記天然ガスの水蒸気改質による水素分離型水蒸気改質器と、前記水蒸気改質用加熱源である燃焼器とを有する熱、電気および水素を供給するシステムであって、
(a)前記コジェネレーションシステムからの排ガスと前記水素分離型水蒸気改質器からのオフガスを合流させ、
(b)前記排ガス及びオフガスをその流れ方向でみて、順次、圧縮機、冷却熱交換器及び気液分離槽を含む二酸化炭素回収装置を備えてなり、
(c)前記冷却熱交換器の冷熱として前記LNGを使用し、
(d)前記コジェネレーションシステム及び前記水蒸気改質用加熱源である燃焼器には酸素富化空気を使用するようにしてなる、
ことを特徴とする熱電気水素供給システム。 - 請求項1に記載の熱電気水素供給システムにおいて、前記コジェネレーションシステムにて生成した水蒸気を前記水蒸気改質器での天然ガスの水蒸気改質用に使用するようにしてなることを特徴とする熱電気水素供給システム。
- LNGを気化した天然ガスを燃料とするコジェネレーションシステムと、前記天然ガスの水蒸気改質による水素分離型水蒸気改質器と、前記水蒸気改質用加熱源であるヒーターとを有する熱、電気および水素を供給するシステムであって、
(a)前記コジェネレーションシステムからの排ガスを前記ヒーターの熱源として使用した後、
(b)前記排ガスと前記水素分離型水蒸気改質器からのオフガスを合流させ、
(c)前記排ガス及びオフガスをその流れ方向でみて、順次、圧縮機、冷却熱交換器及び気液分離槽を含む二酸化炭素回収装置を備えてなり、
(d)前記冷却熱交換器の冷熱として前記LNGを使用し、
(e)前記コジェネレーションシステムには酸素富化空気を使用するようにしてなる、
ことを特徴とする熱電気水素供給システム。 - 請求項3に記載の熱電気水素供給システムにおいて、前記コジェネレーションシステムにて生成した水蒸気を前記水蒸気改質器での天然ガスの水蒸気改質用に使用するようにしてなることを特徴とする熱電気水素供給システム。
- 請求項1〜4のいずれか1項に記載の熱電気水素供給システムが、オンサイト方式の水素ステーションで設置する熱電気水素供給システムであることを特徴とする熱電気水素供給システム。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2009259349A JP5143812B2 (ja) | 2009-11-12 | 2009-11-12 | 熱電気水素供給システム |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2009259349A JP5143812B2 (ja) | 2009-11-12 | 2009-11-12 | 熱電気水素供給システム |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2011106295A true JP2011106295A (ja) | 2011-06-02 |
JP5143812B2 JP5143812B2 (ja) | 2013-02-13 |
Family
ID=44230050
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2009259349A Expired - Fee Related JP5143812B2 (ja) | 2009-11-12 | 2009-11-12 | 熱電気水素供給システム |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP5143812B2 (ja) |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4602477A (en) * | 1985-06-05 | 1986-07-29 | Air Products And Chemicals, Inc. | Membrane-aided distillation for carbon dioxide and hydrocarbon separation |
JPH04334729A (ja) * | 1991-05-08 | 1992-11-20 | Toyo Eng Corp | 発電方法 |
JP2000247604A (ja) * | 1999-02-25 | 2000-09-12 | Toshiba Corp | 水素製造装置及び方法 |
JP2002122030A (ja) * | 2000-10-16 | 2002-04-26 | Kobe Steel Ltd | 電力と水素の併産設備 |
JP2005226596A (ja) * | 2004-02-16 | 2005-08-25 | Jfe Engineering Kk | 発電機能併用水素製造方法及び装置 |
JP2009143744A (ja) * | 2007-12-12 | 2009-07-02 | Petroleum Energy Center | エネルギーステーション |
-
2009
- 2009-11-12 JP JP2009259349A patent/JP5143812B2/ja not_active Expired - Fee Related
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4602477A (en) * | 1985-06-05 | 1986-07-29 | Air Products And Chemicals, Inc. | Membrane-aided distillation for carbon dioxide and hydrocarbon separation |
JPH04334729A (ja) * | 1991-05-08 | 1992-11-20 | Toyo Eng Corp | 発電方法 |
JP2000247604A (ja) * | 1999-02-25 | 2000-09-12 | Toshiba Corp | 水素製造装置及び方法 |
JP2002122030A (ja) * | 2000-10-16 | 2002-04-26 | Kobe Steel Ltd | 電力と水素の併産設備 |
JP2005226596A (ja) * | 2004-02-16 | 2005-08-25 | Jfe Engineering Kk | 発電機能併用水素製造方法及び装置 |
JP2009143744A (ja) * | 2007-12-12 | 2009-07-02 | Petroleum Energy Center | エネルギーステーション |
Also Published As
Publication number | Publication date |
---|---|
JP5143812B2 (ja) | 2013-02-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7634915B2 (en) | Systems and methods for power generation and hydrogen production with carbon dioxide isolation | |
ES2963067T3 (es) | Craqueo de amoníaco | |
US11891950B2 (en) | Systems and methods for power production with integrated production of hydrogen | |
WO2022180740A1 (ja) | Lngを活用する炭酸ガス回収式水素製造システム | |
JP5280343B2 (ja) | 二酸化炭素分離回収装置を伴う水素分離型水素製造システム | |
US20090117024A1 (en) | Process for the Production of Hydrogen with Co-Production and Capture of Carbon Dioxide | |
JP2008163944A (ja) | 部分的co2回収式サイクルプラント用の改質システム | |
Ortiz et al. | Optimization of power and hydrogen production from glycerol by supercritical water reforming | |
JP2005532241A (ja) | 無/低排気エネルギー供給ステーション | |
Verda et al. | Thermodynamic and economic optimization of a MCFC-based hybrid system for the combined production of electricity and hydrogen | |
JP5280348B2 (ja) | ハイブリッド水素製造システム | |
JP5412232B2 (ja) | 二酸化炭素分離回収装置を伴う水素分離型水素製造システム | |
JP2010129286A (ja) | 発電システム | |
JP4744971B2 (ja) | 低質廃熱回収システム | |
RU2471080C2 (ru) | Способ эксплуатации энергетической установки с интегрированной газификацией, а также энергетическая установка | |
JP2004229374A (ja) | Mhd単独高効率発電方法およびシステム | |
JP4632532B2 (ja) | 水素製造方法およびシステム | |
Cioli et al. | Decarbonisation options for the Dutch industrial gases production | |
JP4791841B2 (ja) | 発電システム | |
JP5143812B2 (ja) | 熱電気水素供給システム | |
JP2004018343A (ja) | 炭化水素燃料からの電力と水素の併産方法とそのプラント及びその排熱回収型改質器 | |
KR20170136144A (ko) | 복합발전 시스템 | |
JP5148541B2 (ja) | 酸素燃焼技術を利用した水素分離型水素製造システム | |
JP7025310B2 (ja) | ガスタービン複合発電システム、ガスタービン複合発電方法 | |
JP2009043486A (ja) | 発電システム |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20120131 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20121026 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20121120 |
|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20121121 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20151130 Year of fee payment: 3 |
|
R150 | Certificate of patent or registration of utility model |
Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
LAPS | Cancellation because of no payment of annual fees |