UA80203C2 - Chemical reactor, method for conducting catalytic chemical reactions - Google Patents
Chemical reactor, method for conducting catalytic chemical reactions Download PDFInfo
- Publication number
- UA80203C2 UA80203C2 UAA200511846A UAA200511846A UA80203C2 UA 80203 C2 UA80203 C2 UA 80203C2 UA A200511846 A UAA200511846 A UA A200511846A UA A200511846 A UAA200511846 A UA A200511846A UA 80203 C2 UA80203 C2 UA 80203C2
- Authority
- UA
- Ukraine
- Prior art keywords
- heat exchangers
- reactor
- catalyst
- fact
- reactor according
- Prior art date
Links
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 49
- 239000000126 substance Substances 0.000 title claims abstract description 14
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 4
- 238000000034 method Methods 0.000 title claims description 6
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 5
- 239000003054 catalyst Substances 0.000 claims description 55
- 239000012530 fluid Substances 0.000 claims description 19
- 239000003153 chemical reaction reagent Substances 0.000 claims description 17
- 239000002826 coolant Substances 0.000 claims description 17
- 239000000376 reactant Substances 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 150000003839 salts Chemical class 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 239000007795 chemical reaction product Substances 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 230000001154 acute effect Effects 0.000 description 1
- 230000004323 axial length Effects 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
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
- B01J8/04—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
- B01J8/0403—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 fluid flow within the beds being predominantly horizontal
- B01J8/0423—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 fluid flow within the beds being predominantly horizontal through two or more otherwise shaped beds
- B01J8/0426—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 fluid flow within the beds being predominantly horizontal through two or more otherwise shaped beds the beds being superimposed one above the other
- B01J8/043—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 fluid flow within the beds being predominantly horizontal through two or more otherwise shaped beds the beds being superimposed one above the other in combination with one cylindrical annular 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/248—Reactors comprising multiple separated flow channels
-
- 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
- B01J8/0461—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 in two or more cylindrical annular shaped beds
- B01J8/0469—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 in two or more cylindrical annular shaped beds the beds being superimposed one above the other
-
- 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
-
- 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
- B01J8/0496—Heating or cooling the reactor
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0006—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the plate-like or laminated conduits being enclosed within a pressure vessel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0012—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the apparatus having an annular form
- F28D9/0018—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the apparatus having an annular form without any annular circulation of the heat exchange media
-
- 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
- B01J2208/0015—Plates; 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
- B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
-
- 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
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00761—Discharging
-
- 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
- B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
- B01J2208/021—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles comprising a plurality of beds with flow of reactants in parallel
- B01J2208/022—Plate-type reactors filled with granular catalyst
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fluid Mechanics (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP03011209A EP1477220A1 (en) | 2003-05-16 | 2003-05-16 | Chemical reactor |
| PCT/EP2004/004422 WO2004101135A1 (en) | 2003-05-16 | 2004-04-27 | Chemical reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| UA80203C2 true UA80203C2 (en) | 2007-08-27 |
Family
ID=33016914
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| UAA200511846A UA80203C2 (en) | 2003-05-16 | 2004-04-27 | Chemical reactor, method for conducting catalytic chemical reactions |
Country Status (13)
| Country | Link |
|---|---|
| US (2) | US7807115B2 (pt) |
| EP (2) | EP1477220A1 (pt) |
| CN (1) | CN1791459B (pt) |
| AR (1) | AR044285A1 (pt) |
| AU (1) | AU2004238016B2 (pt) |
| BR (1) | BRPI0410368B1 (pt) |
| CA (1) | CA2525876C (pt) |
| CL (1) | CL2004000986A1 (pt) |
| MX (1) | MXPA05012330A (pt) |
| MY (1) | MY142840A (pt) |
| RU (1) | RU2346734C2 (pt) |
| UA (1) | UA80203C2 (pt) |
| WO (1) | WO2004101135A1 (pt) |
Families Citing this family (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1442786A1 (en) * | 2003-01-29 | 2004-08-04 | Methanol Casale S.A. | Pseudo isothermal radial reactor |
| DE10361517A1 (de) * | 2003-12-23 | 2005-07-28 | Basf Ag | Verfahren zur Herstellung von Formaldehyd |
| MX2007001173A (es) | 2004-01-15 | 2007-09-25 | Methanol Casale Sa | Reactor catalitico de lecho fijo. |
| EP1707259B1 (en) * | 2005-04-01 | 2018-06-06 | Casale Sa | Process for the heterogeneous synthesis of chemical compounds |
| EP2292326A1 (en) | 2009-09-02 | 2011-03-09 | Methanol Casale S.A. | Vertical isothermal shell-and-tube reactor |
| US8759600B2 (en) | 2010-06-28 | 2014-06-24 | Uop Llc | Reduced fluidization of solid particles in radial flow fluid/solid contacting |
| FR3009862B1 (fr) * | 2013-08-26 | 2015-09-11 | Commissariat Energie Atomique | Echangeur de chaleur entre deux fluides, utilisation de l'echangeur avec du metal liquide et du gaz, application a un reacteur nucleaire a neutrons rapides refroidi avec du metal liquide |
| EP3115338A1 (en) * | 2015-07-07 | 2017-01-11 | Casale SA | A method for revamping an ammonia converter |
| WO2017165753A1 (en) | 2016-03-24 | 2017-09-28 | Tetra, Technologies, Inc. | Improving the temperature stability of polyols and sugar alcohols in brines |
| US11136486B2 (en) | 2016-03-24 | 2021-10-05 | Tetra Technologies, Inc. | High density, low TCT monovalent brines and uses thereof |
| GB2564063B (en) | 2016-03-24 | 2022-04-06 | Tetra Tech | High density, low TCT divalent brines and uses thereof |
| EP3497057B1 (de) * | 2016-08-09 | 2020-09-30 | thyssenkrupp Industrial Solutions AG | Verfahren zur herstellung von ammoniak sowie ammoniaksynthesekonverter |
| US11453817B2 (en) | 2017-10-24 | 2022-09-27 | Tetra Technologies, Inc. | Stabilization of iodide-containing brines and brine mixtures |
| US11021645B2 (en) | 2017-10-24 | 2021-06-01 | Tetra Technologies, Inc | Stabilization and reduction of TCT of divalent iodide-containing brines |
| US10851278B2 (en) | 2017-10-24 | 2020-12-01 | Tetra Technologies, Inc. | Stabilization and reduction of TCT of brines containing monovalent iodides |
| AR113649A1 (es) | 2017-12-20 | 2020-05-27 | Haldor Topsoe As | Convertidor de flujo axial enfriado |
| CN109908843B (zh) * | 2019-04-23 | 2019-12-31 | 宁波巨化新材料有限公司 | 丙醛加氢反应器 |
| EP4286043A1 (en) * | 2022-05-31 | 2023-12-06 | Walter Tosto S.p.A. | Catalytic reactor with heat exchange unit |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3796547A (en) * | 1969-11-26 | 1974-03-12 | Texaco Inc | Heat exchange apparatus for catalytic system |
| AT367722B (de) * | 1977-01-31 | 1982-07-26 | Robert Dipl Ing Dr Tec Schober | Vorrichtung zur durchfuehrung eines verfahrens zur erhoehung des ammoniakaufbaues bei der katalytischen ammoniaksynthese |
| EP1060788A1 (en) * | 1999-06-15 | 2000-12-20 | Methanol Casale S.A. | Isothermal catalytic reactor for exothermic or endothermic heterogeneous reactions |
| JP2001038195A (ja) * | 1999-06-28 | 2001-02-13 | Basf Ag | 熱交換板を備えた反応器 |
| EP1153653A1 (en) * | 2000-05-11 | 2001-11-14 | Methanol Casale S.A. | Reactor for exothermic or endothermic heterogeneous reactions |
| EP1221339A1 (en) * | 2001-01-05 | 2002-07-10 | Methanol Casale S.A. | Catalytic reactor with heat exchanger for exothermic and endothermic heterogeneous chemical reactions |
| US20030039601A1 (en) | 2001-08-10 | 2003-02-27 | Halvorson Thomas Gilbert | Oxygen ion transport membrane apparatus and process for use in syngas production |
| EP1306126A1 (en) * | 2001-10-19 | 2003-05-02 | Methanol Casale S.A. | Heat exchange unit for isothermal chemical reactors |
-
2003
- 2003-05-16 EP EP03011209A patent/EP1477220A1/en not_active Withdrawn
-
2004
- 2004-04-27 CA CA2525876A patent/CA2525876C/en not_active Expired - Lifetime
- 2004-04-27 RU RU2005139156/12A patent/RU2346734C2/ru active
- 2004-04-27 BR BRPI0410368-8B1A patent/BRPI0410368B1/pt active IP Right Grant
- 2004-04-27 EP EP04729618A patent/EP1626802A1/en not_active Withdrawn
- 2004-04-27 UA UAA200511846A patent/UA80203C2/uk unknown
- 2004-04-27 WO PCT/EP2004/004422 patent/WO2004101135A1/en active Application Filing
- 2004-04-27 CN CN200480013475.9A patent/CN1791459B/zh not_active Expired - Lifetime
- 2004-04-27 MX MXPA05012330A patent/MXPA05012330A/es active IP Right Grant
- 2004-04-27 US US10/557,008 patent/US7807115B2/en active Active
- 2004-04-27 AU AU2004238016A patent/AU2004238016B2/en not_active Expired
- 2004-05-06 MY MYPI20041683A patent/MY142840A/en unknown
- 2004-05-07 CL CL200400986A patent/CL2004000986A1/es unknown
- 2004-05-10 AR ARP040101586A patent/AR044285A1/es active IP Right Grant
-
2009
- 2009-12-30 US US12/649,615 patent/US8071059B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| US20070274880A1 (en) | 2007-11-29 |
| MXPA05012330A (es) | 2006-01-30 |
| US20100129283A1 (en) | 2010-05-27 |
| CA2525876C (en) | 2012-01-17 |
| RU2005139156A (ru) | 2006-06-10 |
| EP1477220A1 (en) | 2004-11-17 |
| BRPI0410368A (pt) | 2006-05-30 |
| CL2004000986A1 (es) | 2005-03-11 |
| RU2346734C2 (ru) | 2009-02-20 |
| US8071059B2 (en) | 2011-12-06 |
| CN1791459B (zh) | 2010-10-06 |
| US7807115B2 (en) | 2010-10-05 |
| WO2004101135A1 (en) | 2004-11-25 |
| EP1626802A1 (en) | 2006-02-22 |
| CA2525876A1 (en) | 2004-11-25 |
| AR044285A1 (es) | 2005-09-07 |
| BRPI0410368B1 (pt) | 2013-10-01 |
| AU2004238016B2 (en) | 2009-10-29 |
| MY142840A (en) | 2011-01-14 |
| CN1791459A (zh) | 2006-06-21 |
| AU2004238016A1 (en) | 2004-11-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2361657C2 (ru) | Реактор с неподвижным слоем катализатора | |
| RU2265480C2 (ru) | Реактор для проведения экзотермических или эндотермических гетерогенных реакций и способ его изготовления | |
| UA80203C2 (en) | Chemical reactor, method for conducting catalytic chemical reactions | |
| RU2279307C2 (ru) | Псевдоизотермический каталитический реактор и блочный теплообменник для проведения экзотермических и эндотермических химических реакций | |
| RU2435639C2 (ru) | Изотермический реактор | |
| RU2298432C2 (ru) | Теплообменник для изотермических химических реакторов | |
| US7314603B2 (en) | Heterogeneous catalytic reactor with a modular catalytic cartridge | |
| EP1464384B1 (en) | Horizontal chemical reactor, in particular for methanol synthesis | |
| RU2217230C2 (ru) | Способ модификации гетерогенного экзотермического реактора синтеза, реактор синтеза и способ осуществления гетерогенных экзотермических реакций синтеза | |
| RU2377062C2 (ru) | Реактор для гетерогенного синтеза химических соединений | |
| RU2310641C2 (ru) | Способ и установка для гетерогенного синтеза метанола или аммиака | |
| AU712231B2 (en) | Process and reactor for heterogeneous exothermic synthesis of formaldehyde | |
| RU2340391C2 (ru) | Псевдоизотермический радиальный реактор | |
| CN217410715U (zh) | 一种列管式加氢反应器 | |
| RU2371243C1 (ru) | Каталитический реактор | |
| WO1995024961A1 (en) | Horizontal reactor for heterogeneous exothermic synthesis, in particular for methanol synthesis | |
| SU1058487A3 (ru) | Реактор дл проведени гетерогенного катализа реакций газообразных реагентов под давлением | |
| CN114272872A (zh) | 筒式反应器 |