JP4477432B2 - 改質器 - Google Patents
改質器 Download PDFInfo
- Publication number
- JP4477432B2 JP4477432B2 JP2004191299A JP2004191299A JP4477432B2 JP 4477432 B2 JP4477432 B2 JP 4477432B2 JP 2004191299 A JP2004191299 A JP 2004191299A JP 2004191299 A JP2004191299 A JP 2004191299A JP 4477432 B2 JP4477432 B2 JP 4477432B2
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- Prior art keywords
- reformer
- tube
- gas
- floating head
- reaction
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-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
- B01J8/067—Heating or cooling the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
- B01J8/065—Feeding reactive fluids
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/384—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/0229—Double end plates; Single end plates with hollow spaces
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/0236—Header boxes; End plates floating elements
- F28F9/0241—Header boxes; End plates floating elements floating end plates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00176—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles outside the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00203—Coils
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00212—Plates; Jackets; Cylinders
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00212—Plates; Jackets; Cylinders
- B01J2208/00221—Plates; Jackets; Cylinders comprising baffles for guiding the flow of the heat exchange medium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/08—Methods of heating or cooling
- C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Description
容器と、容器内に配された、改質触媒を収容するための領域を有する反応管とを有し、
容器が固定管板によって仕切られて仕切室が設けられ、
反応管の一端が固定管板に接続されて反応管内部が仕切室と連通し、
反応管の他端が伸縮継ぎ手を介して遊動頭に接続されて反応管内部が遊動頭内部と連通し、
仕切室には改質ガス出口が設けられ、
遊動頭は容器に設けられた原料ガス入口に可動式管継ぎ手を介して接続され、
容器の固定管板と遊動頭との間に、反応管を加熱するための加熱用ガスの入口と出口が設けられ、
加熱用ガスの入口が遊動頭よりも固定管板に近い位置に設けられ、加熱用ガスの出口が固定管板よりも遊動頭に近い位置に設けられ、
固定管板には固定管板を冷却するための冷却手段が設けられ
たことを特徴とする改質器が提供される。
1a 胴
1b 固定管板側鏡板
1c 遊動頭側鏡板
2 原料ガス入り口
3 改質ガス出口
4 加熱用ガス入り口
5 加熱用ガス出口
11 反応管
11a 反応管の触媒層が形成される部分
11b 反応管下部
12 改質触媒
21 固定管板
22 仕切室
23 冷却手段
31 遊動頭
31a 遊動管板
32 可動式管継ぎ手
33 伸縮継ぎ手
34 滑り継ぎ手
35 グランドパッキン
41 冷却水入り口
42a 水冷ジャケット(胴部)
42b 水冷ジャケット(固定管板側鏡板部)
43 冷却水出口
51 断熱材
52 緩衝部材
53 ベーパーベルト
54 ディストリビュータ
55 スプリングハンガー
56 バッフル
61 スペーサー
62 さや管
Claims (6)
- 原料ガスを改質して改質ガスを得るための改質器において、
容器と、容器内に配された、改質触媒を収容するための領域を有する反応管とを有し、
容器が固定管板によって仕切られて仕切室が設けられ、
反応管の一端が固定管板に接続されて反応管内部が仕切室と連通し、
反応管の他端が伸縮継ぎ手を介して遊動頭に接続されて反応管内部が遊動頭内部と連通し、
仕切室には改質ガス出口が設けられ、
遊動頭は容器に設けられた原料ガス入口に可動式管継ぎ手を介して接続され、
容器の固定管板と遊動頭との間に、反応管を加熱するための加熱用ガスの入口と出口が設けられ、
加熱用ガスの入口が遊動頭よりも固定管板に近い位置に設けられ、加熱用ガスの出口が固定管板よりも遊動頭に近い位置に設けられ、
固定管板には固定管板を冷却するための冷却手段が設けられ
たことを特徴とする改質器。 - 前記遊動頭が、容器に固定されたスプリングハンガーによって支持された請求項1記載の改質器。
- 前記反応管が緩衝部材を介して固定管板に接続された請求項1または2記載の改質器。
- 前記反応管の改質触媒を収容する領域が形成される部分の外径より小さい外径を有する反応管部分が、該領域より固定管板側に存在する請求項1〜3の何れか一項記載の改質器。
- 前記反応管を複数有し、反応管と反応管の隙間に伝熱促進手段を有する請求項1〜4の何れか一項記載の改質器。
- 冷却手段が水冷手段である請求項1〜5の何れか一項記載の改質器。
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2004191299A JP4477432B2 (ja) | 2004-06-29 | 2004-06-29 | 改質器 |
US11/168,309 US7517373B2 (en) | 2004-06-29 | 2005-06-29 | Reformer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2004191299A JP4477432B2 (ja) | 2004-06-29 | 2004-06-29 | 改質器 |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2006008480A JP2006008480A (ja) | 2006-01-12 |
JP4477432B2 true JP4477432B2 (ja) | 2010-06-09 |
Family
ID=35505971
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2004191299A Active JP4477432B2 (ja) | 2004-06-29 | 2004-06-29 | 改質器 |
Country Status (2)
Country | Link |
---|---|
US (1) | US7517373B2 (ja) |
JP (1) | JP4477432B2 (ja) |
Families Citing this family (32)
Publication number | Priority date | Publication date | Assignee | Title |
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ES2416331T3 (es) * | 2004-10-26 | 2013-07-31 | Haldor Topsoe A/S | Reactor y procedimiento para llevar a cabo reacciones catalíticas endotérmicas o exotérmicas |
FR2883773B1 (fr) * | 2005-04-01 | 2007-05-11 | Alstom Sa | Dispositif de combustion produisant de l'hydrogene avec reutilisation de co2 capte |
JP5224651B2 (ja) * | 2006-03-31 | 2013-07-03 | Jx日鉱日石エネルギー株式会社 | 固体酸化物形燃料電池 |
WO2007116045A1 (en) * | 2006-04-12 | 2007-10-18 | Shell Internationale Research Maatschappij B.V. | Apparatus and process for cooling hot gas |
DE102006022898B3 (de) * | 2006-05-15 | 2007-09-27 | Uhde Gmbh | Sammelleitung für Röhrenspaltöfen |
US20080016768A1 (en) | 2006-07-18 | 2008-01-24 | Togna Keith A | Chemically-modified mixed fuels, methods of production and used thereof |
FR2914395B1 (fr) * | 2007-03-30 | 2009-11-20 | Inst Francais Du Petrole | Nouveau reacteur echangeur compact utilisant un bruleur poreux |
US20090042071A1 (en) * | 2007-08-07 | 2009-02-12 | Fischer Bernhard A | Multi-tube fuel reformer with augmented heat transfer |
KR100971743B1 (ko) | 2007-12-27 | 2010-07-21 | 삼성에스디아이 주식회사 | 연료 전지 시스템 및 연료 전지 시스템용 개질기 |
US8752615B2 (en) * | 2008-01-08 | 2014-06-17 | General Electric Company | Methods and systems for controlling temperature in a vessel |
JP4638537B2 (ja) * | 2008-11-28 | 2011-02-23 | 三菱重工業株式会社 | 燃料集合体の衝撃吸収装置及び燃料集合体収納容器 |
JP5355062B2 (ja) * | 2008-12-15 | 2013-11-27 | 東洋エンジニアリング株式会社 | メタノール及びアンモニアの併産方法 |
CN102085467B (zh) * | 2009-12-03 | 2013-04-03 | 杭州林达化工技术工程有限公司 | 一种固定床催化反应器 |
WO2011088982A1 (en) | 2010-01-19 | 2011-07-28 | Haldor Topsøe A/S | Process and apparatus for reforming hydrocarbons |
WO2011088981A1 (en) * | 2010-01-19 | 2011-07-28 | Haldor Topsøe A/S | Process for reforming hydrocarbons |
US8747765B2 (en) | 2010-04-19 | 2014-06-10 | Exxonmobil Chemical Patents Inc. | Apparatus and methods for utilizing heat exchanger tubes |
US20150300738A1 (en) * | 2010-05-26 | 2015-10-22 | Astec, Inc. | Apparatus and method for tube dryer |
WO2013004254A1 (en) * | 2011-07-01 | 2013-01-10 | Haldor Topsøe A/S | Heat exchange reactor |
WO2013044444A1 (zh) * | 2011-09-27 | 2013-04-04 | 中国科学院宁波材料技术与工程研究所 | 一种催化重整制氢方法与催化装置 |
KR101422630B1 (ko) * | 2011-12-30 | 2014-07-23 | 두산중공업 주식회사 | 열교환형 선개질기 |
EP2812278B1 (en) * | 2012-02-06 | 2023-04-19 | Helbio Societé Anonyme Hydrogen and Energy Production Systems | Heat integrated reformer with catalytic combustion for hydrogen production |
CA2876374C (en) | 2012-06-14 | 2020-09-01 | Nuvera Fuel Cells, Inc. | Steam reformers for the production of hydrogen reformate and uses thereof |
US9688927B2 (en) * | 2012-09-13 | 2017-06-27 | General Electric Company | System for accommodating differential thermal expansion in syngas cooler |
FR3020968B1 (fr) * | 2014-05-16 | 2016-05-13 | Ifp Energies Now | Reacteur a lit radial multitubulaire |
US9958211B2 (en) | 2015-03-12 | 2018-05-01 | Bayotech, Inc. | Nested-flow heat exchangers and chemical reactors |
CN109477663A (zh) | 2015-07-13 | 2019-03-15 | 富尔顿集团有限公司 | 高效率流体加热系统排放歧管 |
GB2557109A (en) * | 2015-07-24 | 2018-06-13 | Fulton Group N A Inc | Compliant heating system comprising a metallic expansion joint |
FR3052367B1 (fr) * | 2016-06-08 | 2018-06-15 | IFP Energies Nouvelles | Reacteur catalytique radial multitubulaire |
CN109282678B (zh) * | 2018-09-20 | 2020-06-26 | 浙江明一化工机械有限公司 | 一种提高化工生产中热交换效率的方法 |
IT201900008280A1 (it) * | 2019-06-06 | 2020-12-06 | Amec Foster Wheeler Italiana S R L | Reattore, in particolare reattore di reforming con vapore, e suo uso in un processo di reforming con vapore |
CN110595231A (zh) * | 2019-09-04 | 2019-12-20 | 山西亚乐士环保技术股份有限公司 | 浮管式换热器 |
CN114111377A (zh) * | 2021-11-25 | 2022-03-01 | 北京动力机械研究所 | 一种可协调变形换热器结构设计方法 |
Family Cites Families (11)
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US2145877A (en) * | 1935-08-07 | 1939-02-07 | Houdry Process Corp | Apparatus for thermal control of contact masses |
US4337170A (en) | 1980-01-23 | 1982-06-29 | Union Carbide Corporation | Catalytic steam reforming of hydrocarbons |
US4650651A (en) * | 1983-06-09 | 1987-03-17 | Union Carbide Corporation | Integrated process and apparatus for the primary and secondary catalytic steam reforming of hydrocarbons |
US4919844A (en) | 1984-08-16 | 1990-04-24 | Air Products And Chemicals, Inc. | Enhanced heat transfer reformer and method |
EP0194067B2 (en) | 1985-03-05 | 1994-05-11 | Imperial Chemical Industries Plc | Steam reforming hydrocarbons |
AU6120486A (en) * | 1985-06-27 | 1987-01-30 | Stone & Webster Engineering Corporation | Production of synthesis gas using convective reforming |
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DK167864B1 (da) * | 1990-02-02 | 1993-12-27 | Topsoe Haldor As | Fremgangsmaade og reaktorsystem til reforming af carbonhydrider under varmeveksling |
US5567398A (en) | 1990-04-03 | 1996-10-22 | The Standard Oil Company | Endothermic reaction apparatus and method |
DE4221837C1 (en) | 1992-07-03 | 1993-08-19 | Uhde Gmbh, 4600 Dortmund, De | Shrouded catalytic reformer tube - with partially enclosed gas mixing zone, for prodn. of synthesis gas |
JP3442167B2 (ja) | 1993-12-28 | 2003-09-02 | 千代田化工建設株式会社 | 改質器における伝熱方法 |
-
2004
- 2004-06-29 JP JP2004191299A patent/JP4477432B2/ja active Active
-
2005
- 2005-06-29 US US11/168,309 patent/US7517373B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
US7517373B2 (en) | 2009-04-14 |
JP2006008480A (ja) | 2006-01-12 |
US20050287053A1 (en) | 2005-12-29 |
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