GB1276457A - Improvements in or relating to the temperature regulation of high pressure synthesis reactions - Google Patents
Improvements in or relating to the temperature regulation of high pressure synthesis reactionsInfo
- Publication number
- GB1276457A GB1276457A GB01495/70A GB1149570A GB1276457A GB 1276457 A GB1276457 A GB 1276457A GB 01495/70 A GB01495/70 A GB 01495/70A GB 1149570 A GB1149570 A GB 1149570A GB 1276457 A GB1276457 A GB 1276457A
- Authority
- GB
- United Kingdom
- Prior art keywords
- relating
- high pressure
- temperature regulation
- synthesis reactions
- pressure synthesis
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000003786 synthesis reaction Methods 0.000 title abstract 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract 4
- 230000015572 biosynthetic process Effects 0.000 abstract 3
- 229910021529 ammonia Inorganic materials 0.000 abstract 2
- 230000003197 catalytic effect Effects 0.000 abstract 2
- 239000007789 gas Substances 0.000 abstract 2
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
- B01J8/0446—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
-
- 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
- B01J8/0005—Catalytic processes under superatmospheric pressure
-
- 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
-
- 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
-
- 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
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
1276457 Temperature control of catalytic ammonia synthesis OSTERREICHISCHE STICKSTOFFWERKE AG 10 March 1970 [18 March 1969] 11495/70 Heading B1X Temperature control of catalytic ammonia synthesis is achieved by introducing fresh cold synthesis gas into the reacting hot gases substantially at right angles to the general direction of flow of the at a velocity of at least 0.5 m/sec.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT264169A AT289847B (en) | 1969-03-18 | 1969-03-18 | Method and device for the sole or additional temperature control of high-pressure synthesis reactors, preferably for ammonia synthesis, by feeding in cold gas |
DE19691914247 DE1914247A1 (en) | 1969-03-18 | 1969-03-20 | Method and device for the sole or additional temperature control of high pressure synthesis reactors by supplying cold gas |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1276457A true GB1276457A (en) | 1972-06-01 |
Family
ID=25598851
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB01495/70A Expired GB1276457A (en) | 1969-03-18 | 1970-03-10 | Improvements in or relating to the temperature regulation of high pressure synthesis reactions |
Country Status (6)
Country | Link |
---|---|
AT (1) | AT289847B (en) |
BE (1) | BE747512A (en) |
DE (1) | DE1914247A1 (en) |
FR (1) | FR2037869A5 (en) |
GB (1) | GB1276457A (en) |
NL (1) | NL7003312A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014056935A1 (en) | 2012-10-10 | 2014-04-17 | Shell Internationale Research Maatschappij B.V. | Multiple-bed downflow reactor comprising a mixing device, use of said reactor, as well as mixing method |
CN104781002B (en) * | 2012-10-10 | 2016-11-30 | 国际壳牌研究有限公司 | Multi-compartment bed downflow reactor, the using method of described reactor and mixed method including mixing arrangement |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0063864B1 (en) * | 1981-04-23 | 1986-05-14 | Imperial Chemical Industries Plc | Fluid injection apparatus |
JPS60225632A (en) * | 1984-04-23 | 1985-11-09 | Mitsubishi Heavy Ind Ltd | Reactor |
ES2030467T3 (en) * | 1987-07-03 | 1992-11-01 | Ammonia Casale S.A. | IMPROVED PROCESS FOR HETEROGENOUS SYNTHESIS AND RELATED REACTORS. |
DE3829214A1 (en) * | 1988-08-29 | 1990-03-08 | Uhde Gmbh | REACTOR FOR CARRYING OUT CATALYTIC GAS REACTIONS WITH A NUMBER OF COLD GAS SUPPLIES |
DE3829215A1 (en) * | 1988-08-29 | 1990-03-08 | Uhde Gmbh | REACTOR FOR CARRYING OUT CATALYTIC GAS REACTIONS WITH A PRESSURE-RESISTANT SHEATH AND ONE BALL BOTTOM ON THE FRONT OUTER EDGE |
-
1969
- 1969-03-18 AT AT264169A patent/AT289847B/en not_active IP Right Cessation
- 1969-03-20 DE DE19691914247 patent/DE1914247A1/en active Pending
-
1970
- 1970-03-09 NL NL7003312A patent/NL7003312A/xx unknown
- 1970-03-10 FR FR7008485A patent/FR2037869A5/fr not_active Expired
- 1970-03-10 GB GB01495/70A patent/GB1276457A/en not_active Expired
- 1970-03-17 BE BE747512D patent/BE747512A/en unknown
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014056935A1 (en) | 2012-10-10 | 2014-04-17 | Shell Internationale Research Maatschappij B.V. | Multiple-bed downflow reactor comprising a mixing device, use of said reactor, as well as mixing method |
KR20150067330A (en) * | 2012-10-10 | 2015-06-17 | 쉘 인터내셔날 리써취 마트샤피지 비.브이. | Multiple-bed downflow reactor comprising a mixing device, use of said reactor, as well as mixing method |
CN104781002A (en) * | 2012-10-10 | 2015-07-15 | 国际壳牌研究有限公司 | Multiple-bed downflow reactor comprising a mixing device, use of said reactor, as well as mixing method |
CN104781002B (en) * | 2012-10-10 | 2016-11-30 | 国际壳牌研究有限公司 | Multi-compartment bed downflow reactor, the using method of described reactor and mixed method including mixing arrangement |
US10076736B2 (en) | 2012-10-10 | 2018-09-18 | Shell Oil Company | Multiple-bed downflow reactor comprising a mixing device, use of said reactor, as well as mixing method |
KR102135558B1 (en) | 2012-10-10 | 2020-07-21 | 쉘 인터내셔날 리써취 마트샤피지 비.브이. | Multiple-bed downflow reactor comprising a mixing device, use of said reactor, as well as mixing method |
Also Published As
Publication number | Publication date |
---|---|
BE747512A (en) | 1970-09-17 |
NL7003312A (en) | 1970-09-22 |
AT289847B (en) | 1971-05-10 |
FR2037869A5 (en) | 1970-12-31 |
DE1914247A1 (en) | 1970-10-08 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PLNP | Patent lapsed through nonpayment of renewal fees |