JPS6467246A - Reactor - Google Patents

Reactor

Info

Publication number
JPS6467246A
JPS6467246A JP22505487A JP22505487A JPS6467246A JP S6467246 A JPS6467246 A JP S6467246A JP 22505487 A JP22505487 A JP 22505487A JP 22505487 A JP22505487 A JP 22505487A JP S6467246 A JPS6467246 A JP S6467246A
Authority
JP
Japan
Prior art keywords
inner tube
catalyst layer
high temperature
temperature gas
introducing side
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.)
Pending
Application number
JP22505487A
Other languages
Japanese (ja)
Inventor
Kenji Kataoka
Toshihiko Hirabayashi
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP22505487A priority Critical patent/JPS6467246A/en
Publication of JPS6467246A publication Critical patent/JPS6467246A/en
Pending legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
    • F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

PURPOSE:To utilize sensible heat of high temperature gas passing through inside an inner tube by disposing an endothermic section on the high temperature gas introducing side of the inner tube and an exothermic section of the raw material gas introducing side of a catalyst layer and providing a plurality of heat pipes in which operating liquid is enclosed. CONSTITUTION:A catalyst layer 7 having a double tube structure consisting of an outer tube 2 and an inner tube 6 and filled with catalyst 3 in an annular space formed between the outer tube 2 and the inner tube 6 is formed, and raw material gas introduced into the outer tube 2 and passing through the catalyst layer 7 is discharged out through the inside of the inner tube 6. An endothermic section 10a is provided on the high temperature gas introducing side of the inner tube 6 in a plurality of heat pipes 10 in which operating liquid (example: cesium) is enclosed, while an exothermic section 10b is provided on the raw gas introducing side of the catalyst layer 7. As a result, sensible heat of high temperature gas passed through the catalyst layer is not thrown away uselessly, but can be utilized effectively.
JP22505487A 1987-09-08 1987-09-08 Reactor Pending JPS6467246A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22505487A JPS6467246A (en) 1987-09-08 1987-09-08 Reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22505487A JPS6467246A (en) 1987-09-08 1987-09-08 Reactor

Publications (1)

Publication Number Publication Date
JPS6467246A true JPS6467246A (en) 1989-03-13

Family

ID=16823318

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22505487A Pending JPS6467246A (en) 1987-09-08 1987-09-08 Reactor

Country Status (1)

Country Link
JP (1) JPS6467246A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003057358A1 (en) * 2002-01-12 2003-07-17 Saudi Basic Industries Corporation Heat exchange tubular reactor with a heat pipe

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003057358A1 (en) * 2002-01-12 2003-07-17 Saudi Basic Industries Corporation Heat exchange tubular reactor with a heat pipe

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