GB758538A - Method and apparatus for temperature control of catalytic chemical reactions - Google Patents
Method and apparatus for temperature control of catalytic chemical reactionsInfo
- Publication number
- GB758538A GB758538A GB1767/54A GB176754A GB758538A GB 758538 A GB758538 A GB 758538A GB 1767/54 A GB1767/54 A GB 1767/54A GB 176754 A GB176754 A GB 176754A GB 758538 A GB758538 A GB 758538A
- Authority
- GB
- United Kingdom
- Prior art keywords
- temperature
- cooling medium
- coolant
- controlled
- reactants
- 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
Classifications
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/001—Controlling catalytic processes
-
- 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
- C07C29/1512—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 reaction conditions
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F27/00—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
-
- 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
- B01J2208/00026—Controlling or regulating the heat exchange system
- B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
- B01J2208/00044—Temperature measurement
- B01J2208/00061—Temperature measurement of the reactants
-
- 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
- B01J2208/00026—Controlling or regulating the heat exchange system
- B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
- B01J2208/00088—Flow rate measurement
-
- 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
- B01J2208/00477—Controlling the temperature by thermal insulation means
- B01J2208/00495—Controlling the temperature by thermal insulation means using insulating materials or refractories
Abstract
In a method for carrying out exothermic catalytic reactions with homogeneous flowing fluid reactants, e.g. the oxidation of naphthalene to phthalic anhydride or ethylene to ethylene oxide, the reacting temperature is maintained at predetermined values by indirect cooling with co-current flowing coolant characterized in that the temperature of admission of the cooling medium and the throughput of cooling medium are controlled independently and, preferably, automatically. Preferably the temperature of the coolant is controlled by relating it to the inlet temperature of the reaction zone and the quantity of coolant controlled in relation to the outlet temperature. The cooling medium may be recycled; or may be cooled or portionally cooled before recycling; or the reactants may be used as cooling medium.ALSO:In a method for carrying out exothermic catalytic reactions with homogeneous flowing fluid reactants, the reacting temperature is maintained at predetermined values by indirect cooling with co-current flowing coolant characterized in that the temperature of admission of the cooling medium and the throughput of cooling medium are controlled independently and, preferably, automatically. Preferably the temperature of the coolant is controlled by relating it to the inlet temperature of the reaction zone and the quantity of coolant controlled in relation to the outlet temperature. The cooling medium may be recycled; or may be cooled or portionally cooled before recycling; or the reactants may be used as cooling medium. This method is useful for the oxidation of naphthalene to phthallic anhydride or ethylene to ethylene oxide and allows reaction tubes of wider diameter and lengths of 20-50 feet and longer, instead of the usual 6 feet.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE758538X | 1953-01-21 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB758538A true GB758538A (en) | 1956-10-03 |
Family
ID=20326641
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1767/54A Expired GB758538A (en) | 1953-01-21 | 1954-01-20 | Method and apparatus for temperature control of catalytic chemical reactions |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1077192B (en) |
GB (1) | GB758538A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1304159A1 (en) * | 2001-10-19 | 2003-04-23 | Methanol Casale S.A. | Method and reactor for carrying out chemical reactions in pseudo-isothermal conditions |
EP1594604A1 (en) * | 2003-02-17 | 2005-11-16 | Methanol Casale S.A. | Method for carrying out chemical reactions in pseudo-isothermal conditions |
US7799171B2 (en) | 2004-07-01 | 2010-09-21 | Metso Paper, Inc. | Reeling method and system as well as an measuring apparatus |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FI75100C (en) * | 1986-03-03 | 1988-05-09 | Rm Metal Consulting Ky | Catalyst bed for exothermic reactions between gases or liquids. |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE564042C (en) * | 1927-10-23 | 1932-11-25 | Selden Co | Process and apparatus for carrying out exothermic catalytic reactions |
CH145140A (en) * | 1929-01-18 | 1931-02-15 | Degussa | Process for regulating the temperature in flowing mixtures. |
DE855241C (en) * | 1942-09-25 | 1952-11-10 | Ruhrchemie Ag | Process for temperature control of exothermic reactions with the help of a heat transferring liquid medium |
DE853441C (en) * | 1945-03-29 | 1952-10-23 | Standard Oil Dev Co | Reaction chamber for controlling the temperature of exothermic and endothermic reactions |
-
1953
- 1953-03-16 DE DEG11221A patent/DE1077192B/en active Pending
-
1954
- 1954-01-20 GB GB1767/54A patent/GB758538A/en not_active Expired
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1304159A1 (en) * | 2001-10-19 | 2003-04-23 | Methanol Casale S.A. | Method and reactor for carrying out chemical reactions in pseudo-isothermal conditions |
WO2003035242A1 (en) * | 2001-10-19 | 2003-05-01 | Methanol Casale S.A. | Method and reactor for carrying out chemical reactions in pseudo-isothermal conditions |
CN100351009C (en) * | 2001-10-19 | 2007-11-28 | 卡萨尔甲醇公司 | Method for carrying out chemical reactions in pseudo-isothermal conditions |
EP1594604A1 (en) * | 2003-02-17 | 2005-11-16 | Methanol Casale S.A. | Method for carrying out chemical reactions in pseudo-isothermal conditions |
EP1594604B1 (en) * | 2003-02-17 | 2009-06-03 | Methanol Casale S.A. | Method and reactor for carrying out chemical reactions in pseudo-isothermal conditions |
US7727482B2 (en) | 2003-02-17 | 2010-06-01 | Methanol Casale S.A. | Method for carrying out chemical reactions in pseudo-isothermal conditions |
US7799171B2 (en) | 2004-07-01 | 2010-09-21 | Metso Paper, Inc. | Reeling method and system as well as an measuring apparatus |
Also Published As
Publication number | Publication date |
---|---|
DE1077192B (en) | 1960-03-10 |
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