GB626664A - An improved reaction chamber for the temperature control of endothermic and exothermic chemical reactions - Google Patents

An improved reaction chamber for the temperature control of endothermic and exothermic chemical reactions

Info

Publication number
GB626664A
GB626664A GB2806546A GB2806546A GB626664A GB 626664 A GB626664 A GB 626664A GB 2806546 A GB2806546 A GB 2806546A GB 2806546 A GB2806546 A GB 2806546A GB 626664 A GB626664 A GB 626664A
Authority
GB
United Kingdom
Prior art keywords
heat
bundles
exchange
endothermic
catalyst
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
GB2806546A
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.)
Standard Oil Development Co
Original Assignee
Standard Oil Development Co
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 Standard Oil Development Co filed Critical Standard Oil Development Co
Priority to GB2806546A priority Critical patent/GB626664A/en
Publication of GB626664A publication Critical patent/GB626664A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836Heating and cooling the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/245Spouted-bed technique
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/005Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for only one medium being tubes having bent portions or being assembled from bent tubes or being tubes having a toroidal configuration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00115Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00141Coils

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

A reaction chamber for controlling endothermic or exothermic reactions particularly with fluidised catalysts is provided with a plurality of vertical heat-exchange bundles disposed within the chamber, each of the bundles comprising an upper and lower headers <PICT:0626664/III/1> <PICT:0626664/III/2> interconnected by a plurality of tubular elements, and having individually controlled means for introducing thereto or removing therefrom heat-exchange medium. In Fig. 1 a reaction chamber 1 containing a fluidised catalyst bed on grid 6 has hexagonal or square cross-section tubular heat-exchange bundles 5, each of which has individual valved feed and discharge lines 7, 8 to permit isolation of a particular bundle, while monorails 10 and opening 11 are provided in the free space above the catalyst bed for removal and replacement of a bundle. If the reaction is endothermic the heat-exchange medium may be introduced through line 8 and removed by line 7 or vice versa in exothermic reactions. Fig. 4 shows a construction in which the outlet line 8 passes through the lower header 14 to render removal easier. The bundles should be so arranged that no portion of the catalyst space is more than 4 ft. from one, and the tubes of the bundles should be so spaced as not to restrict catalyst flow, e.g. not closer than 0.4 inch nor occupying more than 65 per cent of the cross-sectional area of reactor. One or more tubes, preferably near the centre of a bundle may be larger than the others to facilitate an internal circulation by heat siphon. The heat transfer medium may be vaporising or non-vaporizing fluids such as water, diphenyl, gas oils, or low melting alloys. The reaction vessel may have a central tube with heat-exchange bundles in or around it, the fluidised catalyst being circulated up through the tube and down in the annular space or vice versa.
GB2806546A 1946-09-18 1946-09-18 An improved reaction chamber for the temperature control of endothermic and exothermic chemical reactions Expired GB626664A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2806546A GB626664A (en) 1946-09-18 1946-09-18 An improved reaction chamber for the temperature control of endothermic and exothermic chemical reactions

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2806546A GB626664A (en) 1946-09-18 1946-09-18 An improved reaction chamber for the temperature control of endothermic and exothermic chemical reactions

Publications (1)

Publication Number Publication Date
GB626664A true GB626664A (en) 1949-07-19

Family

ID=10269707

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2806546A Expired GB626664A (en) 1946-09-18 1946-09-18 An improved reaction chamber for the temperature control of endothermic and exothermic chemical reactions

Country Status (1)

Country Link
GB (1) GB626664A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117109180A (en) * 2023-10-24 2023-11-24 耐尔能源装备有限公司 Heat conduction oil heater

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117109180A (en) * 2023-10-24 2023-11-24 耐尔能源装备有限公司 Heat conduction oil heater
CN117109180B (en) * 2023-10-24 2024-01-02 耐尔能源装备有限公司 Heat conduction oil heater

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