GB824913A - Improvements in the production of gaseous olefins by cracking hydrocarbons - Google Patents

Improvements in the production of gaseous olefins by cracking hydrocarbons

Info

Publication number
GB824913A
GB824913A GB2364158A GB2364158A GB824913A GB 824913 A GB824913 A GB 824913A GB 2364158 A GB2364158 A GB 2364158A GB 2364158 A GB2364158 A GB 2364158A GB 824913 A GB824913 A GB 824913A
Authority
GB
United Kingdom
Prior art keywords
liquid
gas
jets
stream
product
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
GB2364158A
Inventor
Ferdinand Markert
Willibald Funk
Gottfried Richter
Otto Frey
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.)
BASF SE
Original Assignee
BASF SE
Badische Anilin and Sodafabrik 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 BASF SE, Badische Anilin and Sodafabrik AG filed Critical BASF SE
Publication of GB824913A publication Critical patent/GB824913A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/025Oxidative cracking, autothermal cracking or cracking by partial combustion
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

<PICT:0824913/IV (b)/1> In the preparation of olefines, particularly ethylene and propylene, by the high-temperature cracking of hydrocarbons the gaseous reaction stream is quenched by supplying laterally to the stream one or more compact jets of liquid in an amount sufficient to cool the gas by at least 100 DEG C. and with a pressure head such that the liquid penetrates the gas and is disintegrated therein. Cracking may be effected in the presence of a fluidized solid, at 650-850 DEG C., and 1-5 atmospheres, e.g. in reactor 1, to which oxygen is also supplied. Solids are removed from the product stream by cyclone 2 from which the gaseous product leaves by pipe 4. Jets of liquid, e.g. liquid reaction products boiling below 300 DEG C., are injected into the gas from jets 6. Preferably the product of (a) the ratio of the pressure head of liquid to that of the gas (measured at the point of entry to the cooling chamber) and (b) the ratio of the mean diameter of the liquid jet to that of the gas, should lie in the range 0.01 to 3. Where several jets are used such products may differ for each jet and the jets may be in different planes. The walls of the cooling chamber are preferably washed with the cooling liquid, e.g. from atomizer 7. Products leave by line 8.
GB2364158A 1957-08-03 1958-07-23 Improvements in the production of gaseous olefins by cracking hydrocarbons Expired GB824913A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE1957B0045563 DE1052396B (en) 1957-08-03 1957-08-03 Method and apparatus for producing gaseous olefins by cracking coal

Publications (1)

Publication Number Publication Date
GB824913A true GB824913A (en) 1959-12-09

Family

ID=25949397

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2364158A Expired GB824913A (en) 1957-08-03 1958-07-23 Improvements in the production of gaseous olefins by cracking hydrocarbons

Country Status (3)

Country Link
DE (1) DE1052396B (en)
FR (1) FR1200693A (en)
GB (1) GB824913A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1262251B (en) * 1959-05-13 1968-03-07 Basf Ag Process for the continuous dehydrogenation of gaseous or vaporous hydrocarbons

Also Published As

Publication number Publication date
DE1052396B (en) 1959-03-12
FR1200693A (en) 1959-12-23

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