JP5248111B2 - 反応器 - Google Patents
反応器 Download PDFInfo
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- JP5248111B2 JP5248111B2 JP2007532943A JP2007532943A JP5248111B2 JP 5248111 B2 JP5248111 B2 JP 5248111B2 JP 2007532943 A JP2007532943 A JP 2007532943A JP 2007532943 A JP2007532943 A JP 2007532943A JP 5248111 B2 JP5248111 B2 JP 5248111B2
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- process fluid
- reactor
- catalyst
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- Expired - Fee Related
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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
- B01J8/0278—Feeding reactive fluids
-
- 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
- B01J8/0242—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 the fluid flow within the bed being predominantly vertical
-
- 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
- B01J8/04—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 the fluid passing successively through two or more beds
- B01J8/0446—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 the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
-
- 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
- B01J8/04—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 the fluid passing successively through two or more beds
- B01J8/0492—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
- C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
- C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
- C01B3/16—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using catalysts
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
- C01C1/0417—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst characterised by the synthesis reactor, e.g. arrangement of catalyst beds and heat exchangers in the reactor
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/152—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the reactor used
-
- 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
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00893—Feeding means for the reactants
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00002—Chemical plants
- B01J2219/00018—Construction aspects
- B01J2219/00024—Revamping, retrofitting or modernisation of existing plants
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- 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
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/0318—Processes
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T29/00—Metal working
- Y10T29/49—Method of mechanical manufacture
- Y10T29/49826—Assembling or joining
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- General Health & Medical Sciences (AREA)
- Health & Medical Sciences (AREA)
- Analytical Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
(i)プロセス流体を反応器の一つ以上の対向するポートに供給するステップと、
(ii)プロセス流体を反応器内に配置されている触媒又は収着剤の固定床を通って軸方向及び反対方向に通すステップと、
(iii)得られたプロセス流体を前記固定床内に配置された回収手段を通じて回収するステップと、そして
(iv)プロセス流体を前記回収手段(前記回収手段は前記反応器の一つ以上の既存対向ポートと流体連絡している)を通じて反応器から取り出すステップと
を含む方法も提供する。
Claims (17)
- ドーム形の両端部、及び前記ドーム形の両端部に配置された対向ポートを有するシェルを含む反応器を軸流配置から対向軸流配置に改造する方法であって、
(i)プロセス流体回収手段を前記シェルの中に、一つ以上の前記ポートと流体連絡させて設置すること、
(ii)前記反応器に、前記プロセス流体回収手段の周りの粒状触媒又は収着剤の床を提供すること、及び
(iii)前記反応器に供給されるプロセス流体が前記触媒又は収着剤の固定床を軸方向に及び反対方向に通り、そして前記プロセス流体回収手段によって回収されるように、前記対向ポートを通して前記反応器に流体を適応すること、
を含む方法。 - プロセス流体回収手段が、前記反応器内の前記床内の中央に配置される、請求項1に記載の方法。
- プロセス流体回収手段が、チャンバを規定する有孔部材と、前記チャンバと流体連絡している導管とを含み、前記導管は一つ以上の前記ポートに接続するように適応されている、請求項1又は請求項2に記載の方法。
- プロセス流体回収手段が有孔リングコレクタを含む、請求項3に記載の方法。
- プロセス流体回収手段がいくつかの部品で構成されるモジュール形式であり、該部品が反応器内でその場で一緒に接合されて該プロセス流体回収手段が形成される、請求項1〜4のいずれか1項に記載の方法。
- プロセス流体回収手段が、二つ以上の出口ポートと流体連絡するように設置される、請求項1〜5のいずれか1項に記載の方法。
- プロセス流体回収手段が、一つの出口ポートと流体連絡するように設置され、前記出口ポートは入口ポートと同心配置されている、請求項1〜5のいずれか1項に記載の方法。
- 出口ポートがベンチュリ手段を含む、請求項7に記載の方法。
- ドーム形の両端部、及び前記ドーム形の両端部に配置された対向ポートを有するシェルを含む、対向軸流用に改造された反応器であって、前記反応器はプロセス流体回収手段の周りに粒状触媒又は収着剤の床を有し、該プロセス流体回収手段は前記床内の中央に、一つ以上の前記ポートと流体連絡させて設置されており、前記反応器に供給されるプロセス流体が前記触媒又は収着剤の固定床を軸方向に及び反対方向に通り、そして前記回収手段によって回収され、そして前記ポートの一つ以上を通じて反応器から取り出される、前記反応器。
- 前記触媒又は収着剤の固定床が不活性材料の層を有する、請求項9に記載の反応器。
- 不活性粒子の層が前記プロセス流体回収手段の周りに提供されており、該不活性材料粒子は残りの床を構成する触媒又は収着剤粒子の粒径より大きい粒径を有し、回収手段の周辺のプロセス流体の透過性が向上される、請求項10に記載の反応器。
- 粒状触媒又は収着剤の床を通って延びるバイパス手段が備えられ、プロセス流体の一部が床の一端から他端に運搬される、請求項9〜11のいずれか1項に記載の反応器。
- i)プロセス流体を、請求項9〜12のいずれか1項に記載の反応器の対向ポートに供給するステップと、
ii)プロセス流体を反応器内に配置されている触媒粒子又は収着剤粒子の固定床を通って軸方向及び反対方向に通すステップと、
iii)得られたプロセス流体を、前記固定床内に配置された回収手段を通じて回収するステップと、
iv)プロセス流体を、前記反応器の一つ以上の前記対向ポートと流体連絡している前記回収手段を通じて容器から取り出すステップと
を含む方法。 - プロセス流体が、水素、一酸化炭素、二酸化炭素及び蒸気を含み、固定床が水性ガスシフト触媒を含む、請求項13に記載の方法。
- プロセス流体が水素、一酸化炭素及び二酸化炭素を含み、固定床がメタノール合成触媒を含む、請求項13に記載の方法。
- プロセス流体が水素及び窒素を含み、固定床がアンモニア合成触媒を含む、請求項13に記載の方法。
- プロセス流体が触媒毒を含有する炭化水素原料を含み、固定床が原料から前記毒を除去するのに有用な触媒又は収着剤を含む、請求項13に記載の方法。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0421198A GB0421198D0 (en) | 2004-09-24 | 2004-09-24 | Reaction vessel |
GB0421198.3 | 2005-09-02 | ||
PCT/GB2005/003397 WO2006032839A1 (en) | 2004-09-24 | 2005-09-02 | Reaction vessel |
Publications (3)
Publication Number | Publication Date |
---|---|
JP2008514399A JP2008514399A (ja) | 2008-05-08 |
JP2008514399A5 JP2008514399A5 (ja) | 2008-10-23 |
JP5248111B2 true JP5248111B2 (ja) | 2013-07-31 |
Family
ID=33397151
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2007532943A Expired - Fee Related JP5248111B2 (ja) | 2004-09-24 | 2005-09-02 | 反応器 |
Country Status (12)
Country | Link |
---|---|
US (3) | US8056205B2 (ja) |
EP (1) | EP1791630A1 (ja) |
JP (1) | JP5248111B2 (ja) |
CN (1) | CN101027121B (ja) |
BR (1) | BRPI0515873B1 (ja) |
CA (1) | CA2579209C (ja) |
EG (1) | EG24659A (ja) |
GB (1) | GB0421198D0 (ja) |
MY (1) | MY146647A (ja) |
RU (1) | RU2381057C2 (ja) |
UA (1) | UA88923C2 (ja) |
WO (1) | WO2006032839A1 (ja) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008297451A (ja) * | 2007-05-31 | 2008-12-11 | Japan Energy Corp | 多孔質脱硫剤及びこれを用いた脱硫方法 |
US8197785B2 (en) * | 2008-02-27 | 2012-06-12 | Kellogg Brown & Root Llc | Split flow contactor |
CN104492291B (zh) * | 2014-12-18 | 2023-04-25 | 重庆康乐制药有限公司 | 便于更换的乳化反应装置 |
FR3083716B1 (fr) * | 2018-07-10 | 2020-07-31 | Axens | Dispositif de distribution d’un fluide, apte a etre dispose dans un reacteur comprenant un lit catalytique fixe |
US11873227B2 (en) * | 2019-04-15 | 2024-01-16 | Regents Of The University Of Minnesota | Integrated apparatus for producing ammonia |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2861873A (en) * | 1955-12-07 | 1958-11-25 | Lummus Co | Apparatus for effecting catalytic exothermic reactions |
NL136765C (ja) * | 1965-10-20 | |||
GB1307845A (en) | 1969-05-28 | 1973-02-21 | Ici Ltd | Reactor |
DE2452428A1 (de) * | 1974-11-01 | 1976-05-13 | Mannesmann Ag | Doppelstromfilter |
US4075102A (en) * | 1976-05-13 | 1978-02-21 | Combustion Engineering, Inc. | Liquid processing media bed drain system |
US4033727A (en) | 1976-07-06 | 1977-07-05 | Phillips Petroleum Company | Separator ring in fixed bed radial flow catalytic reactor |
US4126539A (en) * | 1977-12-05 | 1978-11-21 | Mobil Oil Corporation | Method and arrangement of apparatus for hydrogenating hydrocarbons |
JPS5921859Y2 (ja) * | 1980-02-12 | 1984-06-29 | 三菱電機株式会社 | 充填塔 |
US4298589A (en) * | 1980-06-17 | 1981-11-03 | The M. W. Kellogg Company | Split axial flow converter in ammonia synthesis |
EP0075056A1 (en) | 1981-09-23 | 1983-03-30 | The M. W. Kellogg Company | Synthesis system and process for the production of ammonia |
GB8521650D0 (en) | 1985-08-30 | 1985-10-02 | Ici Plc | Catalyst |
JPH0783816B2 (ja) * | 1987-09-24 | 1995-09-13 | 日本酸素株式会社 | 吸着器 |
US5071449A (en) * | 1990-11-19 | 1991-12-10 | Air Products And Chemicals, Inc. | Gas separation by rapid pressure swing adsorption |
GB9107999D0 (en) * | 1991-04-16 | 1991-06-05 | Boc Group Plc | Improved apparatus for the separation of a gaseous mixture |
US5670116A (en) * | 1995-12-05 | 1997-09-23 | Exxon Research & Engineering Company | Hydroprocessing reactor with enhanced product selectivity |
GB9922940D0 (en) | 1999-09-29 | 1999-12-01 | Ici Plc | Catalytic reactor |
US7141640B2 (en) * | 2002-10-08 | 2006-11-28 | General Electric Company | Process for producing dihydroxy compounds using upflow reactor system |
JP3954953B2 (ja) * | 2002-10-24 | 2007-08-08 | 住友精化株式会社 | 吸着装置 |
-
2004
- 2004-09-24 GB GB0421198A patent/GB0421198D0/en not_active Ceased
-
2005
- 2005-09-02 CN CN2005800321603A patent/CN101027121B/zh not_active Expired - Fee Related
- 2005-09-02 UA UAA200704425A patent/UA88923C2/uk unknown
- 2005-09-02 CA CA2579209A patent/CA2579209C/en not_active Expired - Fee Related
- 2005-09-02 EP EP05777429A patent/EP1791630A1/en not_active Withdrawn
- 2005-09-02 WO PCT/GB2005/003397 patent/WO2006032839A1/en active Application Filing
- 2005-09-02 RU RU2007115400A patent/RU2381057C2/ru not_active IP Right Cessation
- 2005-09-02 BR BRPI0515873-7A patent/BRPI0515873B1/pt not_active IP Right Cessation
- 2005-09-02 US US11/663,895 patent/US8056205B2/en not_active Expired - Fee Related
- 2005-09-02 JP JP2007532943A patent/JP5248111B2/ja not_active Expired - Fee Related
- 2005-09-22 MY MYPI20054458A patent/MY146647A/en unknown
-
2007
- 2007-03-21 EG EGNA2007000302 patent/EG24659A/xx active
-
2011
- 2011-09-26 US US13/245,286 patent/US8852537B2/en not_active Expired - Fee Related
-
2014
- 2014-08-21 US US14/464,917 patent/US20140361222A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
RU2381057C2 (ru) | 2010-02-10 |
CN101027121A (zh) | 2007-08-29 |
EP1791630A1 (en) | 2007-06-06 |
US20120016041A1 (en) | 2012-01-19 |
CN101027121B (zh) | 2011-11-30 |
CA2579209C (en) | 2013-01-29 |
WO2006032839A1 (en) | 2006-03-30 |
RU2007115400A (ru) | 2008-10-27 |
CA2579209A1 (en) | 2006-03-30 |
US8852537B2 (en) | 2014-10-07 |
EG24659A (en) | 2010-04-07 |
UA88923C2 (uk) | 2009-12-10 |
GB0421198D0 (en) | 2004-10-27 |
BRPI0515873B1 (pt) | 2014-09-23 |
US20140361222A1 (en) | 2014-12-11 |
US8056205B2 (en) | 2011-11-15 |
US20080107584A1 (en) | 2008-05-08 |
JP2008514399A (ja) | 2008-05-08 |
MY146647A (en) | 2012-09-14 |
BRPI0515873A (pt) | 2008-08-12 |
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