DD220232A5 - Stehender reaktor zur erzeugung von methanol - Google Patents
Stehender reaktor zur erzeugung von methanol Download PDFInfo
- Publication number
- DD220232A5 DD220232A5 DD84265063A DD26506384A DD220232A5 DD 220232 A5 DD220232 A5 DD 220232A5 DD 84265063 A DD84265063 A DD 84265063A DD 26506384 A DD26506384 A DD 26506384A DD 220232 A5 DD220232 A5 DD 220232A5
- Authority
- DD
- German Democratic Republic
- Prior art keywords
- reactor
- tubes
- item
- housing
- catalyst
- Prior art date
Links
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 239000003054 catalyst Substances 0.000 claims abstract description 54
- 238000004519 manufacturing process Methods 0.000 claims description 3
- IHPYMWDTONKSCO-UHFFFAOYSA-N 2,2'-piperazine-1,4-diylbisethanesulfonic acid Chemical compound OS(=O)(=O)CCN1CCN(CCS(O)(=O)=O)CC1 IHPYMWDTONKSCO-UHFFFAOYSA-N 0.000 abstract 2
- 239000007990 PIPES buffer Substances 0.000 abstract 1
- 238000010276 construction Methods 0.000 abstract 1
- 239000002689 soil Substances 0.000 abstract 1
- 239000013589 supplement Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 13
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000002826 coolant Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000004992 fission Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- B01J8/0496—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
- B01J8/02—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
- B01J8/0449—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 beds
- B01J8/0453—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 beds the beds being superimposed one above the other
-
- 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
- B01J2208/00115—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
- B01J2219/18—Details relating to the spatial orientation of the reactor
- B01J2219/185—Details relating to the spatial orientation of the reactor vertical
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19833332049 DE3332049A1 (de) | 1983-09-06 | 1983-09-06 | Stehender reaktor zur erzeugung von methanol |
| DE19833344423 DE3344423A1 (de) | 1983-12-08 | 1983-12-08 | Stehender reaktor zur erzeugung von methanol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DD220232A5 true DD220232A5 (de) | 1985-03-27 |
Family
ID=25813755
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DD84265063A DD220232A5 (de) | 1983-09-06 | 1984-07-09 | Stehender reaktor zur erzeugung von methanol |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US4632587A (fr) |
| EP (1) | EP0155341B1 (fr) |
| DD (1) | DD220232A5 (fr) |
| DE (1) | DE3469680D1 (fr) |
| SU (1) | SU1327782A3 (fr) |
| UA (1) | UA5987A1 (fr) |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4743432A (en) * | 1984-11-16 | 1988-05-10 | M.A.N. Maschinenfabrik Augsburg-Nurnberg | Vertical reactor for the generation of methanol |
| FR2584733B1 (fr) * | 1985-07-12 | 1987-11-13 | Inst Francais Du Petrole | Procede ameliore de vapocraquage d'hydrocarbures |
| DE3880877T2 (de) * | 1987-02-26 | 1993-09-23 | Ammonia Casale Sa | System zur verbesserung der reaktorausbeute fuer exotherme synthese, insbesondere fuer die ammoniakreaktion. |
| NL8902250A (nl) * | 1989-09-08 | 1991-04-02 | Veg Gasinstituut Nv | Werkwijze voor het uitvoeren van een chemische reactie en daarbij te gebruiken reactor. |
| DE19539622C1 (de) * | 1995-10-16 | 1997-06-05 | Bayer Ag | Rohrreaktor |
| US5989500A (en) * | 1997-07-02 | 1999-11-23 | Phillips Petroleum Company | Reactor heat exchange system |
| US7108835B2 (en) * | 2003-10-08 | 2006-09-19 | Rentech, Inc. | Fischer-tropsch slurry reactor cooling tube arrangement |
| MY140160A (en) * | 2004-01-28 | 2009-11-30 | Shell Int Research | Heat exchanger for carrying out an exothermic reaction |
| DE602005022833D1 (de) * | 2004-03-08 | 2010-09-23 | Shell Int Research | Filtersystem mit in ein gehäuse zurückziehbaren filtermitteln |
| DE202007006812U1 (de) | 2007-05-11 | 2008-09-18 | Man Dwe Gmbh | Kühlrohrreaktor |
| US8959769B2 (en) * | 2007-07-26 | 2015-02-24 | General Electric Company | Method and apparatus for heat recovery within a syngas cooler |
| CN102196857A (zh) * | 2008-08-21 | 2011-09-21 | 氟石科技公司 | 从放热的高温反应过程除去热量的装置和方法 |
| EP3839397A1 (fr) * | 2019-12-20 | 2021-06-23 | Fores Engineering Srl | Procédé et dispositif de refroidissement de gaz chauds |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1920800A (en) * | 1931-08-07 | 1933-08-01 | Griscom Russell Co | Heat exchanger |
| US2149300A (en) * | 1938-02-12 | 1939-03-07 | Houdry Process Corp | Distribution and temperature control in chemical reactions |
| US2261293A (en) * | 1938-07-16 | 1941-11-04 | Houdry Process Corp | Heat exchange apparatus |
| US2280081A (en) * | 1939-01-18 | 1942-04-21 | Houdry Process Corp | Catalytic converter |
| US2356700A (en) * | 1942-03-11 | 1944-08-22 | Standard Oil Dev Co | Treating hydrocarbon fluids |
| DE914131C (de) * | 1951-12-11 | 1954-06-28 | Metallgesellschaft Ag | Kontaktofen |
| US2862480A (en) * | 1954-09-10 | 1958-12-02 | Babcock & Wilcox Co | Synthesis gas reactor and heat exchanger |
| DE1501640A1 (de) * | 1966-05-03 | 1969-11-06 | Schmidt Sche Heissdampfgmbh | Waermeaustauscher,insbesondere zum Kuehlen frischer Spaltgase und/oder Synthesegase |
| DE2549398A1 (de) * | 1975-11-04 | 1977-05-05 | Linde Ag | Reaktor |
| DE2848014A1 (de) * | 1978-11-06 | 1980-05-08 | Linde Ag | Reaktor zur durchfuehrung exothermer katalytischer reaktionen |
| CA1172832A (fr) * | 1979-09-06 | 1984-08-21 | Hydrocarbon Research, Inc. | Reacteur a lits de catalyse jumeles a ecoulement ascendant |
| DE3007203A1 (de) * | 1980-02-26 | 1981-09-10 | Linde Ag, 6200 Wiesbaden | Reaktor |
| US4298589A (en) * | 1980-06-17 | 1981-11-03 | The M. W. Kellogg Company | Split axial flow converter in ammonia synthesis |
| DE3117077A1 (de) * | 1981-04-29 | 1982-11-18 | Linde Ag, 6200 Wiesbaden | Verfahren und vorrichtung zur entfernung unerwuenschter gasfoermiger bestandteile aus einem heissen abgas |
-
1984
- 1984-05-12 EP EP84105393A patent/EP0155341B1/fr not_active Expired
- 1984-05-12 DE DE8484105393T patent/DE3469680D1/de not_active Expired
- 1984-06-27 SU SU843753930A patent/SU1327782A3/ru active
- 1984-06-27 UA UA3753930A patent/UA5987A1/uk unknown
- 1984-07-09 DD DD84265063A patent/DD220232A5/de not_active IP Right Cessation
- 1984-08-06 US US06/637,759 patent/US4632587A/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| EP0155341A2 (fr) | 1985-09-25 |
| EP0155341B1 (fr) | 1988-03-09 |
| EP0155341A3 (en) | 1986-04-30 |
| SU1327782A3 (ru) | 1987-07-30 |
| DE3469680D1 (en) | 1988-04-14 |
| UA5987A1 (uk) | 1994-12-29 |
| US4632587A (en) | 1986-12-30 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PV | Patent disclaimer (addendum to changes before extension act) |