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GB790166A - Improvements in or relating to processes and apparatus for effecting a rapid change in temperature of gaseous fluid or for rapidly vaporising liquid fluid - Google Patents

Improvements in or relating to processes and apparatus for effecting a rapid change in temperature of gaseous fluid or for rapidly vaporising liquid fluid

Info

Publication number
GB790166A
GB790166A GB2914/56A GB291456A GB790166A GB 790166 A GB790166 A GB 790166A GB 2914/56 A GB2914/56 A GB 2914/56A GB 291456 A GB291456 A GB 291456A GB 790166 A GB790166 A GB 790166A
Authority
GB
United Kingdom
Prior art keywords
fluid
screen
vessel
temperature
solid
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
GB2914/56A
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.)
Baiaafsche Petroleum Mij Nv De
Bataafsche Petroleum Maatschappij NV
Original Assignee
Baiaafsche Petroleum Mij Nv De
Bataafsche Petroleum Maatschappij NV
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 Baiaafsche Petroleum Mij Nv De, Bataafsche Petroleum Maatschappij NV filed Critical Baiaafsche Petroleum Mij Nv De
Publication of GB790166A publication Critical patent/GB790166A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00Other direct-contact heat-exchange apparatus
    • F28C3/10Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material
    • F28C3/12Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid
    • F28C3/16Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid the particulate material forming a bed, e.g. fluidised, on vibratory sieves

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Allyl chloride is formed by the reaction of propene with chlorine at about 500 DEG C., using a process in which a rapid change in temperature of a gaseous fluid is effected by passing the fluid through a screen of free-falling solid particles of size less than 2 mm., which screen is formed by flow of particles from a homogeneously fluidized bed, the temperature of which is considerably different from that of the fluid (see Group III).ALSO:<PICT:0790166/III/1> A rapid change in temperature of a gaseous fluid is effected, or a liquid fluid is rapidly vaporized, by passing the fluid through a screen of free-falling solid particles of size less than 2 mm., which screen is formed by flow of particles from a homogeneously fluidized bed, the temperature of which is considerably different from that of the fluid. The solids fall through a straight or circular slot at the top of a vessel to form a flat or cylindrical screen; a collecting device for the solid is provided at the foot of the vessel and an inlet for the fluid leads into one of the spaces into which the vessel is divided by the screen. The process may be used for the rapid heating of reactants, for the cooling of reaction products, or for controlling the temperature of endothermic or exothermic reactions. Liquid or gaseous hydrocarbons may be cracked by contact with solids which are either inert, e.g. sand, or catalytic; the reaction products may be cooled by introducing a quenching medium into the outlet from the vessel or by passing the products through a second screen of cooled solids. When reactants are to be heated separately, two screens of hot particles may be used, one for each reactant. As shown, hot particles flow from fluidized bed in vessel 5 through slot 15 to form screen 16, being collected in a fluidized bed in vessel 6. The fluid to be treated is supplied through nozzle 17 and passes through screen 16 to outlet 13 and cyclone 35. Solid collects in vessel 38 and is withdrawn at 39 for heating, regenerating if necessary, and return to vessel 5. Heating and regeneration may be carried out by a process according to the invention, the solid being treated as a falling screen with fuel and combustion air. Solid paraffin-containing substances may be converted into ethene or a mixture of olefins at 700-800 DEG C. in the presence of steam and in some cases oxygen. Other reactions referred to are the conversion of methane by steam into carbon monoxide and hydrogen; the conversion of methane by oxygen into ethyne or aromatics; the oxidation of ammonia to nitrogen oxides at 700-1000 DEG C.; the conversion of alkanes to alkenes; the formation of allyl chloride from propene and chlorine at 500 DEG C.; the pyrolytic aromatization of alkanes at 750-900 DEG C.; the reaction between methene, ammonia and oxygen in the presence of platinum catalyst to form hydrogen cyanide; and the reaction between methane and nitrogen oxide at 1000 DEG C. to form hydrogen cyanide.
GB2914/56A 1955-01-31 1956-01-30 Improvements in or relating to processes and apparatus for effecting a rapid change in temperature of gaseous fluid or for rapidly vaporising liquid fluid Expired GB790166A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL790166X 1955-01-31

Publications (1)

Publication Number Publication Date
GB790166A true GB790166A (en) 1958-02-05

Family

ID=19832729

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2914/56A Expired GB790166A (en) 1955-01-31 1956-01-30 Improvements in or relating to processes and apparatus for effecting a rapid change in temperature of gaseous fluid or for rapidly vaporising liquid fluid

Country Status (1)

Country Link
GB (1) GB790166A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2117885A (en) * 1982-03-30 1983-10-19 Chevron Res Process and device for recovering heat from a particulate solid containing diverse particle sizes
GB2145347A (en) * 1981-11-16 1985-03-27 Foster Wheeler Energy Corp Fluidized return of particulate material to a fluidized bed combustor
GB2242438A (en) * 1990-03-26 1991-10-02 Amoco Corp Catalytic cracking with quenching
US5087427A (en) * 1990-03-26 1992-02-11 Amoco Corporation Catalytic cracking unit with internal gross cut separator and quench injector
US5626741A (en) * 1990-03-26 1997-05-06 Amoco Corporation Catalytic cracking with quenching
WO2014173791A1 (en) * 2013-04-23 2014-10-30 Bayer Technology Services Gmbh Process for the preparation of benzene from methane and carbon dioxide with a fluid-tight dividing wall in the reactor

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2145347A (en) * 1981-11-16 1985-03-27 Foster Wheeler Energy Corp Fluidized return of particulate material to a fluidized bed combustor
GB2117885A (en) * 1982-03-30 1983-10-19 Chevron Res Process and device for recovering heat from a particulate solid containing diverse particle sizes
GB2242438A (en) * 1990-03-26 1991-10-02 Amoco Corp Catalytic cracking with quenching
US5087427A (en) * 1990-03-26 1992-02-11 Amoco Corporation Catalytic cracking unit with internal gross cut separator and quench injector
GB2242438B (en) * 1990-03-26 1994-10-26 Amoco Corp Catalytic cracking with quenching
US5626741A (en) * 1990-03-26 1997-05-06 Amoco Corporation Catalytic cracking with quenching
WO2014173791A1 (en) * 2013-04-23 2014-10-30 Bayer Technology Services Gmbh Process for the preparation of benzene from methane and carbon dioxide with a fluid-tight dividing wall in the reactor

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