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GB330872A - Improvements in and apparatus for carrying out endothermic catalytic gas reactions - Google Patents

Improvements in and apparatus for carrying out endothermic catalytic gas reactions

Info

Publication number
GB330872A
GB330872A GB37740/29A GB3774029A GB330872A GB 330872 A GB330872 A GB 330872A GB 37740/29 A GB37740/29 A GB 37740/29A GB 3774029 A GB3774029 A GB 3774029A GB 330872 A GB330872 A GB 330872A
Authority
GB
United Kingdom
Prior art keywords
catalytic gas
gas reactions
carrying
endothermic catalytic
reaction tube
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
GB37740/29A
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.)
IG Farbenindustrie AG
Original Assignee
IG Farbenindustrie AG
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 IG Farbenindustrie AG filed Critical IG Farbenindustrie AG
Publication of GB330872A publication Critical patent/GB330872A/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
    • 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
    • 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
    • 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
    • B01J2208/00212—Plates; Jackets; Cylinders

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)

Abstract

330,872. I. G. Farbenindustrie Akt.- Ges. Dec. 15, 1928, [Convention date]. Catalytic apparatus.-Apparatus for endothermic catalytic gas reactions comprises a reaction tube K fixed at one end only to the wall O of the heating chamber which surrounds it, and provided with an inner tube J extending to the bottom of the reaction tube for the removal of the reaction products. The free end of the reaction tube may extend through the opposite wall U of the heating chamber and be fitted with a removable closure K<1>.
GB37740/29A 1928-12-15 1929-12-09 Improvements in and apparatus for carrying out endothermic catalytic gas reactions Expired GB330872A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE330872X 1928-12-15

Publications (1)

Publication Number Publication Date
GB330872A true GB330872A (en) 1930-06-19

Family

ID=6193211

Family Applications (1)

Application Number Title Priority Date Filing Date
GB37740/29A Expired GB330872A (en) 1928-12-15 1929-12-09 Improvements in and apparatus for carrying out endothermic catalytic gas reactions

Country Status (1)

Country Link
GB (1) GB330872A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2654657A (en) * 1950-08-14 1953-10-06 Nat Cylinder Gas Co Tubular reactor with expansion compensator
US2660519A (en) * 1948-04-23 1953-11-24 Chemical Construction Corp Fluid heater
US2788266A (en) * 1951-10-13 1957-04-09 Stirnemann Ernst Catalytic reactor furnace
US3607128A (en) * 1970-04-02 1971-09-21 Uhde Gmbh Friedrich Axial flow reaction tower
US4690690A (en) * 1985-03-05 1987-09-01 Imperial Chemical Industries Plc Steam reforming hydrocarbons
US4750986A (en) * 1983-03-25 1988-06-14 Imperial Chemical Industries Plc Steam reforming
WO2001034287A1 (en) * 1999-11-09 2001-05-17 Mg Technologies Ag Method for catalytically dehydrating hydrocarbons in a tube reactor

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2660519A (en) * 1948-04-23 1953-11-24 Chemical Construction Corp Fluid heater
US2654657A (en) * 1950-08-14 1953-10-06 Nat Cylinder Gas Co Tubular reactor with expansion compensator
US2788266A (en) * 1951-10-13 1957-04-09 Stirnemann Ernst Catalytic reactor furnace
US3607128A (en) * 1970-04-02 1971-09-21 Uhde Gmbh Friedrich Axial flow reaction tower
US4750986A (en) * 1983-03-25 1988-06-14 Imperial Chemical Industries Plc Steam reforming
EP0298525A1 (en) * 1983-03-25 1989-01-11 Imperial Chemical Industries Plc Steam reforming
US4690690A (en) * 1985-03-05 1987-09-01 Imperial Chemical Industries Plc Steam reforming hydrocarbons
US4810472A (en) * 1985-03-05 1989-03-07 Imperial Chemical Industries Plc Apparatus for steam reforming hydrocarbons
WO2001034287A1 (en) * 1999-11-09 2001-05-17 Mg Technologies Ag Method for catalytically dehydrating hydrocarbons in a tube reactor

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