CL2016002619A1 - Reactor catalitico tubular isotermico. - Google Patents
Reactor catalitico tubular isotermico.Info
- Publication number
- CL2016002619A1 CL2016002619A1 CL2016002619A CL2016002619A CL2016002619A1 CL 2016002619 A1 CL2016002619 A1 CL 2016002619A1 CL 2016002619 A CL2016002619 A CL 2016002619A CL 2016002619 A CL2016002619 A CL 2016002619A CL 2016002619 A1 CL2016002619 A1 CL 2016002619A1
- Authority
- CL
- Chile
- Prior art keywords
- catalytic reactor
- catalytic
- tubular catalytic
- milk
- isothermal tubular
- Prior art date
Links
Classifications
-
- 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
- B01J8/0285—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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/006—Baffles
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular reactors
-
- 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
- B01J8/0207—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 horizontal
- B01J8/0221—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 horizontal in a cylindrical shaped bed
-
- 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
- C01C1/0441—Reactors with the catalyst arranged in tubes
-
- 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
-
- 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
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00132—Tubes
-
- 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
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
-
- 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
- C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Combustion & Propulsion (AREA)
- Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Analytical Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
REACTOR CATALITICO ISTOTERMICO QUE COMPRENDE UN LECHO CATALICO Y UN INTERCAMBAIDOR DE CALOR TUBULAR INMERSO EN DICHO LECHO CATALITICO, EN DONDE EL INTERCAMBIADOR ESTA FORMADO POR TUBOS RECTOS CONECTADOS A UN DISTRIBUIDO Y UN COLECTOR FORMADOS PREFERIBLEMENTE POR CUERPOS TOROIDALES QUE SOPORTAN DICHOS TUBOS, Y EN DONDE EL LECHO CATALÍTICO ES DEL TIPO ATRAVESADO POR FLUJO RADIAL ENTRANTE.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP14165317.0A EP2933016A1 (en) | 2014-04-18 | 2014-04-18 | Isothermal tubular catalytic reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
CL2016002619A1 true CL2016002619A1 (es) | 2017-01-20 |
Family
ID=50897342
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CL2016002619A CL2016002619A1 (es) | 2014-04-18 | 2016-10-14 | Reactor catalitico tubular isotermico. |
Country Status (10)
Country | Link |
---|---|
US (1) | US20170028373A1 (es) |
EP (2) | EP2933016A1 (es) |
CN (1) | CN106232222A (es) |
AU (1) | AU2015248803A1 (es) |
BR (1) | BR112016024253A2 (es) |
CA (1) | CA2939854A1 (es) |
CL (1) | CL2016002619A1 (es) |
MX (1) | MX2016013361A (es) |
RU (1) | RU2016145114A (es) |
WO (1) | WO2015158796A1 (es) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3124111A1 (en) | 2015-07-29 | 2017-02-01 | Casale SA | Tube isothermal catalytic reactor |
CN109173937B (zh) * | 2018-09-30 | 2021-06-11 | 中石化宁波工程有限公司 | 可变温甲醇合成反应系统 |
CN110898768A (zh) * | 2019-10-24 | 2020-03-24 | 中石化宁波工程有限公司 | 一种双等温系统变换炉 |
CN110876913A (zh) * | 2019-11-05 | 2020-03-13 | 中国石油化工股份有限公司 | 一种径向床等温变换反应装置 |
CN112050202B (zh) * | 2020-09-03 | 2023-04-28 | 福大紫金氢能科技股份有限公司 | 一种管式氨分解反应器 |
CN115414872B (zh) * | 2022-08-11 | 2023-11-03 | 安徽润衍科技有限公司 | 管式等温反应器及由1,2-环氧戊烷生产1,2-戊二醇的方法 |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5839572B2 (ja) * | 1979-04-03 | 1983-08-31 | 東洋エンジニアリング株式会社 | 反応器およびその使用法 |
EP0082609B1 (en) * | 1981-12-14 | 1987-01-14 | Imperial Chemical Industries Plc | Chemical reactor and process |
JPS59175442A (ja) * | 1983-03-23 | 1984-10-04 | Toyo Eng Corp | メタンを含むガスの製造法 |
CA1296023C (en) * | 1986-07-24 | 1992-02-18 | Maarten Johannes Van Der Burgt | Process for converting a gaseous feed into an at least partly liquidproduct |
US5366704A (en) | 1989-09-25 | 1994-11-22 | Uop | Radial flow reactor with double perforated scallops |
US5058664A (en) | 1990-07-13 | 1991-10-22 | Phillips Petroleum Company | Rodbaffle heat exchanger |
US5642778A (en) | 1996-04-09 | 1997-07-01 | Phillips Petroleum Company | Rod baffle heat exchangers |
DE202007006812U1 (de) * | 2007-05-11 | 2008-09-18 | Man Dwe Gmbh | Kühlrohrreaktor |
EP2246109A1 (en) * | 2009-04-29 | 2010-11-03 | Methanol Casale S.A. | Isothermal tube reactor |
CN102059078B (zh) * | 2010-11-19 | 2013-06-19 | 航天长征化学工程股份有限公司 | 一种等温径向变换反应器 |
CN203075925U (zh) * | 2013-01-09 | 2013-07-24 | 南京国昌化工科技有限公司 | 互供热双催化反应器 |
-
2014
- 2014-04-18 EP EP14165317.0A patent/EP2933016A1/en not_active Withdrawn
-
2015
- 2015-04-15 AU AU2015248803A patent/AU2015248803A1/en not_active Abandoned
- 2015-04-15 US US15/124,590 patent/US20170028373A1/en not_active Abandoned
- 2015-04-15 BR BR112016024253A patent/BR112016024253A2/pt not_active Application Discontinuation
- 2015-04-15 MX MX2016013361A patent/MX2016013361A/es unknown
- 2015-04-15 EP EP15719163.6A patent/EP3131668A1/en not_active Withdrawn
- 2015-04-15 CA CA2939854A patent/CA2939854A1/en not_active Abandoned
- 2015-04-15 RU RU2016145114A patent/RU2016145114A/ru unknown
- 2015-04-15 WO PCT/EP2015/058217 patent/WO2015158796A1/en active Application Filing
- 2015-04-15 CN CN201580020344.1A patent/CN106232222A/zh active Pending
-
2016
- 2016-10-14 CL CL2016002619A patent/CL2016002619A1/es unknown
Also Published As
Publication number | Publication date |
---|---|
CN106232222A (zh) | 2016-12-14 |
WO2015158796A1 (en) | 2015-10-22 |
EP3131668A1 (en) | 2017-02-22 |
EP2933016A1 (en) | 2015-10-21 |
AU2015248803A1 (en) | 2016-09-08 |
MX2016013361A (es) | 2017-02-09 |
BR112016024253A2 (pt) | 2017-08-15 |
RU2016145114A (ru) | 2018-05-21 |
US20170028373A1 (en) | 2017-02-02 |
CA2939854A1 (en) | 2015-10-22 |
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