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GB664359A - - Google Patents

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Publication number
GB664359A
GB664359A GB664359DA GB664359A GB 664359 A GB664359 A GB 664359A GB 664359D A GB664359D A GB 664359DA GB 664359 A GB664359 A GB 664359A
Authority
GB
United Kingdom
Prior art keywords
oil
oxygen
per cent
chamber
weight
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.)
Active
Application number
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.)
Publication of GB664359A publication Critical patent/GB664359A/en
Active legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B31/00—Charging devices
    • C10B31/12—Charging devices for liquid materials
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00—Aliphatic unsaturated hydrocarbons
    • C07C11/02—Alkenes
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B55/00—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/34—Thermal 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
    • C10G9/36—Thermal 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
    • C10G9/38—Thermal 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 produced by partial combustion of the material to be cracked or by combustion of another hydrocarbon

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

664,359. Cracking hydrocarbons to make olefines. KAFTAL, G., and BALLABIO, G. May 18, 1948 [May 30, 1947], No. 13481/48. Class 32 Olefines of low molecular weight are obtained from mineral oils, mineral oil distillates (petrol, kerosene, gas oil), coal tar oils and pitch, by atomizing the raw material in intimate admixture with air or oxygen into a heated chamber, the amount of oxygen being sufficient, by combustion of part of the raw material, to maintain the chamber at a temperature greater than 480‹C. The reaction may be carried out in the presence of steam ; and a catalyst such as pulverized silica gel, may be employed. Chamber A which is lined with refractory material, was preheated to 600‹C. by means of burner M. The combustion gases leave through chimney L. A fuel oil (Engler viscosity 6 at 60‹C.) was then sprayed with oxygen (containing nitrogen as impurity) through sprayer I; burner M was turned down, chimney L was closed and outlet O was opened. The proportion of oxygen to oil was adjusted so as to maintain the chamber at 620‹C. Coke (6 per cent by weight of the feed-oil) was discharged from the bottom of the chamber. The vapours leaving through outlet O were passed through dustremover B, and then cooled in heat-exchanger C which is also used to preheat the feed-oil and oxygen. The vapours were then passed through cooler D where a liquid condensed, and the olefine-rich gas remaining was then washed free from carbon dioxide in scrubber N. The condensate was divided into two aromatic fractions with a cut-point at 180‹C. The olefine-rich gas, which comprised 58 per cent by weight of the feedoil, contained ethylene (28 per cent), propylene (10 per cent) and butylene (5 per cent). The saturated hydrocarbons separated from the gas, and the higher-boiling liquid fraction, may be returned to the reaccolumn 3.
GB664359D 1947-05-30 Active GB664359A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT664359X 1947-05-30

Publications (1)

Publication Number Publication Date
GB664359A true GB664359A (en)

Family

ID=30012283

Family Applications (1)

Application Number Title Priority Date Filing Date
GB664359D Active GB664359A (en) 1947-05-30

Country Status (2)

Country Link
FR (1) FR960408A (en)
GB (1) GB664359A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1032246B (en) * 1953-05-20 1958-06-19 Bataafsche Petroleum Process for the production of olefins

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1205958C2 (en) * 1961-10-14 1973-07-12 Koppers Gmbh Heinrich Method and apparatus for producing a gas rich in olefins

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1032246B (en) * 1953-05-20 1958-06-19 Bataafsche Petroleum Process for the production of olefins

Also Published As

Publication number Publication date
FR960408A (en) 1950-04-18

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