GB865373A - Process and apparatus for carrying out chemical reactions at high temperatures - Google Patents

Process and apparatus for carrying out chemical reactions at high temperatures

Info

Publication number
GB865373A
GB865373A GB7210/59A GB721059A GB865373A GB 865373 A GB865373 A GB 865373A GB 7210/59 A GB7210/59 A GB 7210/59A GB 721059 A GB721059 A GB 721059A GB 865373 A GB865373 A GB 865373A
Authority
GB
United Kingdom
Prior art keywords
inlets
fuel
gas
atmospheres
oxidising gas
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
GB7210/59A
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.)
Hoechst AG
Original Assignee
Hoechst AG
Farbwerke Hoechst 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 Hoechst AG, Farbwerke Hoechst AG filed Critical Hoechst AG
Publication of GB865373A publication Critical patent/GB865373A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/34Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts
    • C10G9/36Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20C2-C4 olefins

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

<FORM:0865373/IV (b)/1> <FORM:0865373/IV (b)/2> <FORM:0865373/IV (b)/3> <FORM:0865373/IV (b)/4> <FORM:0865373/IV (b)/5> The process of the parent Specification, which comprises the formation of acetylene, ethylene and other unsaturated hydrocarbons by pyrolysis of more saturated hydrocarbons by contact with hot combustion gases which are formed by introducing finely divided fuel and oxygen into a combustion chamber, at least one being introduced tangentially at a velocity corresponding to Mach number at least o,8 and introducing the hydrocarbon to be pyrolysed into the combustion gas, is modified in that the fuel and oxidising gas may be introduced at lower velocities but in such a manner that they form atmospheres in coaxial spaces of different diameters. Alternate annular atmospheres preferably contrarotate, the total sum of angular momenta being zero, and adjacent atmospheres are preferably of fuel and oxidising gas. One form of apparatus is shown in Figs. 1 and 2 the fuel is introduced through one ring of inlets 2, 2a, 2b in one direction of rotation and oxidising gas through inlets 3a, and 3b and 3c in the opposite direction. One reactant is also introduced through axial inlet 11, preferably that not introduced at the uppermost inlets, i.e. fuel not oxidising gas. A secondary gas may be introduced by inlets 4a and 4b at a point where burning is complete to cool the walls, the direction of rotation being the same as at the adjacent inlets above. Alternative arrangements are shown in Figs. 3, 4 and 5.
GB7210/59A 1958-02-28 1959-03-02 Process and apparatus for carrying out chemical reactions at high temperatures Expired GB865373A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE865373X 1958-02-28

Publications (1)

Publication Number Publication Date
GB865373A true GB865373A (en) 1961-04-19

Family

ID=6801831

Family Applications (1)

Application Number Title Priority Date Filing Date
GB7210/59A Expired GB865373A (en) 1958-02-28 1959-03-02 Process and apparatus for carrying out chemical reactions at high temperatures

Country Status (1)

Country Link
GB (1) GB865373A (en)

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