FR1396218A - Appareil pour la production de réactions chimiques en phase gazeuse en présence de catalyseurs - Google Patents

Appareil pour la production de réactions chimiques en phase gazeuse en présence de catalyseurs

Info

Publication number
FR1396218A
FR1396218A FR975931A FR975931A FR1396218A FR 1396218 A FR1396218 A FR 1396218A FR 975931 A FR975931 A FR 975931A FR 975931 A FR975931 A FR 975931A FR 1396218 A FR1396218 A FR 1396218A
Authority
FR
France
Prior art keywords
catalysts
production
gas phase
chemical reactions
reactions
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
Application number
FR975931A
Other languages
English (en)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chemical Processes of Ohio Inc
Original Assignee
Chemical Processes of Ohio Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Chemical Processes of Ohio Inc filed Critical Chemical Processes of Ohio Inc
Application granted granted Critical
Publication of FR1396218A publication Critical patent/FR1396218A/fr
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C01C1/0423—Cold wall 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
    • B01J8/0005—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
    • B01J8/0446—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
    • B01J8/02—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
    • 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
    • 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
    • C07C29/153—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 catalyst used
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08C—TREATMENT OR CHEMICAL MODIFICATION OF RUBBERS
    • C08C19/00—Chemical modification of rubber
    • C08C19/28—Reaction with compounds containing carbon-to-carbon unsaturated bonds
    • 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
    • B01J2208/00194—Tubes
    • 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)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
FR975931A 1963-06-17 1964-05-26 Appareil pour la production de réactions chimiques en phase gazeuse en présence de catalyseurs Expired FR1396218A (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US288226A US3254967A (en) 1963-06-17 1963-06-17 Multiple bed catalyst apparatus having close temperature control

Publications (1)

Publication Number Publication Date
FR1396218A true FR1396218A (fr) 1965-04-16

Family

ID=23106277

Family Applications (1)

Application Number Title Priority Date Filing Date
FR975931A Expired FR1396218A (fr) 1963-06-17 1964-05-26 Appareil pour la production de réactions chimiques en phase gazeuse en présence de catalyseurs

Country Status (9)

Country Link
US (1) US3254967A (fr)
BE (1) BE648734A (fr)
CH (1) CH448033A (fr)
DE (1) DE1261116B (fr)
ES (1) ES300421A1 (fr)
FR (1) FR1396218A (fr)
GB (1) GB1079643A (fr)
NL (1) NL6405888A (fr)
SE (1) SE301633B (fr)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3366461A (en) * 1964-05-11 1968-01-30 Chemical Construction Corp Apparatus for exothermic catalytic reactions
US3442626A (en) * 1965-01-08 1969-05-06 Girdler Corp Ammonia converter
NL136765C (fr) * 1965-10-20
US3480407A (en) * 1967-02-02 1969-11-25 Vulcan Cincinnati Inc Multiple zone apparatus for the processing of fluids having interzone fluid mixing and redistribution features
US3888896A (en) * 1973-05-29 1975-06-10 Chem Systems Methanol production
GB1484366A (en) * 1974-07-02 1977-09-01 Ici Ltd Methanol
US4127389A (en) * 1977-04-04 1978-11-28 Pullman Incorporated Exchanger reactor
US4264566A (en) * 1978-10-06 1981-04-28 Phillips Petroleum Company Temperature control for an ammonia synthesis reactor
US4226795A (en) * 1979-05-04 1980-10-07 E. I. Du Pont De Nemours And Company Purge gas in methanol synthesis
US4423022A (en) * 1979-05-22 1983-12-27 The Lummus Company Processes for carrying out catalytic exothermic and endothermic high-pressure gas reactions
DE3068184D1 (en) * 1980-07-08 1984-07-19 Riedel Kalte- Und Klimatechnik Gmbh & Co, Kg Evaporator for liquid and/or gaseous media, especially for refrigeration plants and heat pumps
DE3065830D1 (en) * 1980-08-28 1984-01-12 Theodore Oscar Wentworth Process for the synthesis of methanol from hydrogen and the oxides of carbon using catalysts
JPH09509611A (ja) * 1994-03-01 1997-09-30 メサノール カサーレ ソシエテ アノニーム 異なる温度のガス流用の、特に不均一系の発熱合成反応器用の混合装置
EP2116296B1 (fr) * 2008-04-30 2010-08-25 Ammonia Casale S.A. Dispositif de chauffage de démarrage pour réacteurs d'ammoniac
ITUB20150576A1 (it) * 2015-04-24 2016-10-24 Hexsol Italy Srl Scambiatore di calore a fascio tubiero e struttura perfezionata
DE102016107124A1 (de) * 2016-04-18 2017-10-19 Thyssenkrupp Ag NH3 Synthesekonfiguration für Großanlagen
CN109850918A (zh) * 2018-12-17 2019-06-07 福州大学化肥催化剂国家工程研究中心 一种合成氨反应器及工艺

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1949122A (en) * 1929-07-05 1934-02-27 Calco Chemical Co Inc Apparatus for use in the catalytic oxidation of gases
US1959898A (en) * 1929-08-14 1934-05-22 Kathe Brode Production of phthalic anhydride
US2046816A (en) * 1930-04-29 1936-07-07 Gen Chemical Corp Converter
BE389974A (fr) * 1931-07-24
US2512586A (en) * 1945-09-04 1950-06-20 Commercial Solvents Corp Process and apparatus for carrying out exothermic chemical reactions
US2632692A (en) * 1949-01-18 1953-03-24 Hydrocarbon Research Inc Multiple bed catalyst apparatus
DE892743C (de) * 1951-12-09 1953-10-08 Basf Ag Vorrichtung zur Durchfuehrung von katalytischen Gasreaktionen, insbesondere unter Druck
US3002816A (en) * 1958-07-23 1961-10-03 Kellogg M W Co Method of effecting exothermic catalytic reactions
US3164446A (en) * 1960-09-08 1965-01-05 Metallgesellschaft Ag Mixing device for multiple bed reactor

Also Published As

Publication number Publication date
GB1079643A (en) 1967-08-16
US3254967A (en) 1966-06-07
BE648734A (fr) 1964-12-02
CH448033A (de) 1967-12-15
DE1261116B (de) 1968-02-15
ES300421A1 (es) 1964-11-16
NL6405888A (fr) 1964-12-18
SE301633B (fr) 1968-06-17

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