GB1085613A - Process and apparatus for reacting gases, vapours or liquids - Google Patents

Process and apparatus for reacting gases, vapours or liquids

Info

Publication number
GB1085613A
GB1085613A GB4691863A GB4691863A GB1085613A GB 1085613 A GB1085613 A GB 1085613A GB 4691863 A GB4691863 A GB 4691863A GB 4691863 A GB4691863 A GB 4691863A GB 1085613 A GB1085613 A GB 1085613A
Authority
GB
United Kingdom
Prior art keywords
reactor
reactants
reaction
venturi
nozzles
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
GB4691863A
Inventor
Ronald Forfar Edge
Lionel Arthur Moignard
Bryan Reginald Parr
Brian Hoyle Thompson
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.)
Gas Council
Original Assignee
Gas Council
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 Gas Council filed Critical Gas Council
Priority to GB4691863A priority Critical patent/GB1085613A/en
Publication of GB1085613A publication Critical patent/GB1085613A/en
Expired legal-status Critical Current

Links

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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2415—Tubular reactors
    • B01J19/2435—Loop-type 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
    • B01J15/00—Chemical processes in general for reacting gaseous media with non-particulate solids, e.g. sheet material; Apparatus specially adapted therefor
    • B01J15/005—Chemical processes in general for reacting gaseous media with non-particulate solids, e.g. sheet material; Apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
    • 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
    • B01J16/00—Chemical processes in general for reacting liquids with non- particulate solids, e.g. sheet material; Apparatus specially adapted therefor
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
    • C01B3/16—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using catalysts
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/10—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with stationary catalyst bed

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Continuous catalytic reactions, e.g. the water gas shift reaction or the methanation reaction in an H2- and CO-containing gas, are carried out in a thermally insulated reactor which has an internal coaxial hollow cylinder, Figs. 1, 2 (not shown), or Venturi, Figs. 3 to 6 (not shown), and orifices or nozzles for continuous supply and withdrawal of reactants, the velocity of introduction of the reactants and the arrangement of the reactor parts being such as to ensure continuous circulation of a substantial body of the reactants and products in the reactor. The reactants may be preheated to control the reaction temperature, and the nozzles and the central cylinder or Venturi may be adjustable to control the reaction. The catalyst may be coated on the internal walls of the reactor, or may be supported on formers therein, and curved baffles may be included in the reactor to assist circulation. Two specific examples are described; one relates to the water gas shift reaction and the other to the catalytic methanation of a gas made by the catalytic gasefication of a light distillate.ALSO:Continuous catalytic reactions, e.g. the water gas shift reaction or the methanation reaction in a combustible gas mixture, are carried out in a thermally insulated reactor which has an internal coaxial hollow cylinder or venturi, and orifices or nozzles for continuous supply and withdrawal of reactants, the velocity of introduction of the reactants and the arrangement of the reactor parts being such as to ensure continuous circulation of a substantial body of the reactants and products in the reactor. The reactants may be preheated to control the reaction temperature, and the nozzles and the central cylinder or venturi may be adjustable to control the reaction. The catalyst may be coated on the internal walls of the reactor or may be supported on formers therein, and curved baffles may be included in the reactor to assist circulation.
GB4691863A 1963-11-27 1963-11-27 Process and apparatus for reacting gases, vapours or liquids Expired GB1085613A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB4691863A GB1085613A (en) 1963-11-27 1963-11-27 Process and apparatus for reacting gases, vapours or liquids

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB4691863A GB1085613A (en) 1963-11-27 1963-11-27 Process and apparatus for reacting gases, vapours or liquids

Publications (1)

Publication Number Publication Date
GB1085613A true GB1085613A (en) 1967-10-04

Family

ID=10443058

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4691863A Expired GB1085613A (en) 1963-11-27 1963-11-27 Process and apparatus for reacting gases, vapours or liquids

Country Status (1)

Country Link
GB (1) GB1085613A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0846653A1 (en) * 1996-12-05 1998-06-10 Ammonia Casale S.A. High efficiency catalytic carbon monoxide conversion process
NL2019236B1 (en) * 2017-07-12 2019-01-30 Green Vision Holding Bv DEVICE AND METHOD FOR CONVERTING CARBON MONOXIDE AND WATER IN CARBON DIOXIDE AND HYDROGEN ACCORDING TO AN LTS REACTION

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0846653A1 (en) * 1996-12-05 1998-06-10 Ammonia Casale S.A. High efficiency catalytic carbon monoxide conversion process
US5985231A (en) * 1996-12-05 1999-11-16 Ammonia Casale S.A. Catalytic carbon monoxide conversion with acceleration or gaseous feed
US6610259B1 (en) 1996-12-05 2003-08-26 Ammonia Casale S.A. High efficiency catalytic carbon monoxide conversion process
NL2019236B1 (en) * 2017-07-12 2019-01-30 Green Vision Holding Bv DEVICE AND METHOD FOR CONVERTING CARBON MONOXIDE AND WATER IN CARBON DIOXIDE AND HYDROGEN ACCORDING TO AN LTS REACTION

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