MA51536A1 - Reacteur de conversion de reactions reduites a l'equilibre - Google Patents
Reacteur de conversion de reactions reduites a l'equilibreInfo
- Publication number
- MA51536A1 MA51536A1 MA51536A MA51536A MA51536A1 MA 51536 A1 MA51536 A1 MA 51536A1 MA 51536 A MA51536 A MA 51536A MA 51536 A MA51536 A MA 51536A MA 51536 A1 MA51536 A1 MA 51536A1
- Authority
- MA
- Morocco
- Prior art keywords
- zone
- tube
- conversion reactor
- reaction conversion
- equilibrium
- 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
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
- B01J8/009—Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
-
- 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
- B01J19/2475—Membrane 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
-
- 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
-
- 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
- B01J2208/00008—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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
L’invention concerne un réacteur de conversion de réactions réduites à l’équilibre comprenant un boîtier de réacteur (4) réalisé sous forme de tube - dans lequel est agencée une première zone (8) servant au passage d’un moyen d’absorption (6) liquide qui s’étend dans la direction longitudinale du tube (10) et - dans lequel une deuxième zone (12) s’étendant également dans la direction longitudinale du tube (10) pour l’accueil d’un matériau de catalyseur (14) étant agencé. L’invention se caractérise - en ce que la première zone (8) et la deuxième zone (12) sont séparées par une zone séparatrice (16) perméable aux gaz, - en ce que la zone séparatrice (16) comporte une structure autoporteuse (26) mécanique et - en ce que le rapport d’aspect du boîtier de réacteur (4) tubulaire le long de la zone de réaction (28) est supérieur à 6.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP18168501.7A EP3556460A1 (fr) | 2018-04-20 | 2018-04-20 | Réacteur de mise en uvre de réactions à équilibre réduit |
PCT/EP2019/059882 WO2019201974A1 (fr) | 2018-04-20 | 2019-04-17 | Réacteur de conversion de réactions réduites à l'équilibre |
Publications (2)
Publication Number | Publication Date |
---|---|
MA51536A1 true MA51536A1 (fr) | 2021-04-30 |
MA51536B1 MA51536B1 (fr) | 2022-11-30 |
Family
ID=62046680
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MA51536A MA51536B1 (fr) | 2018-04-20 | 2019-04-17 | Reacteur de conversion de reactions reduites a l'equilibre |
Country Status (6)
Country | Link |
---|---|
US (1) | US20210154634A1 (fr) |
EP (2) | EP3556460A1 (fr) |
CN (1) | CN112004594A (fr) |
CL (1) | CL2020002702A1 (fr) |
MA (1) | MA51536B1 (fr) |
WO (1) | WO2019201974A1 (fr) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU2021332773A1 (en) * | 2020-08-31 | 2023-04-13 | Sumitomo Chemical Company, Limited | Chemical reaction method, chemical reaction apparatus and production method |
CN113041970B (zh) * | 2021-03-17 | 2021-11-26 | 南京理工大学 | 一种内置扰流结构催化膜式反应器 |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS585691B2 (ja) * | 1978-09-27 | 1983-02-01 | 理化学研究所 | 多段交換反応塔 |
JP2001342155A (ja) * | 2000-06-01 | 2001-12-11 | Nkk Corp | スラリー床反応器 |
US20070264190A1 (en) * | 2006-05-09 | 2007-11-15 | Qinglin Zhang | Fixed-bed reactors and catalytic processes |
KR101573085B1 (ko) * | 2007-05-18 | 2015-11-30 | 셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이 | 반응기 시스템, 흡수재 및 공급물을 반응시키는 방법 |
GB201000156D0 (en) * | 2010-01-07 | 2010-02-24 | Gas2 Ltd | Isothermal reactor for partial oxidisation of methane |
GB201107072D0 (en) * | 2011-04-27 | 2011-06-08 | Davy Process Techn Ltd | Process |
CN102584526B (zh) * | 2011-12-28 | 2014-09-10 | 上海碧科清洁能源技术有限公司 | 一种由合成气制备甲醇的膜接触器方法以及用于该方法的膜反应器 |
DE102016204717A1 (de) * | 2016-03-22 | 2017-09-28 | Siemens Aktiengesellschaft | Reaktor zur Durchführung von gleichgewichtslimitierten Reaktionen |
DE102016210224A1 (de) | 2016-06-09 | 2017-12-14 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Reaktor und Verfahren zur Umsetzung von gleichgewichtslimitierten Reaktionen |
JP7049075B2 (ja) * | 2016-07-04 | 2022-04-06 | 公益財団法人地球環境産業技術研究機構 | メタノール製造方法およびメタノール製造装置 |
-
2018
- 2018-04-20 EP EP18168501.7A patent/EP3556460A1/fr not_active Withdrawn
-
2019
- 2019-04-17 US US17/047,862 patent/US20210154634A1/en not_active Abandoned
- 2019-04-17 MA MA51536A patent/MA51536B1/fr unknown
- 2019-04-17 WO PCT/EP2019/059882 patent/WO2019201974A1/fr unknown
- 2019-04-17 CN CN201980026995.XA patent/CN112004594A/zh active Pending
- 2019-04-17 EP EP19720485.2A patent/EP3784381A1/fr not_active Withdrawn
-
2020
- 2020-10-19 CL CL2020002702A patent/CL2020002702A1/es unknown
Also Published As
Publication number | Publication date |
---|---|
CL2020002702A1 (es) | 2021-04-05 |
MA51536B1 (fr) | 2022-11-30 |
US20210154634A1 (en) | 2021-05-27 |
WO2019201974A1 (fr) | 2019-10-24 |
EP3556460A1 (fr) | 2019-10-23 |
CN112004594A (zh) | 2020-11-27 |
EP3784381A1 (fr) | 2021-03-03 |
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