GB297398A - Process for splitting hydrocarbons - Google Patents

Process for splitting hydrocarbons

Info

Publication number
GB297398A
GB297398A GB1310127A GB1310127A GB297398A GB 297398 A GB297398 A GB 297398A GB 1310127 A GB1310127 A GB 1310127A GB 1310127 A GB1310127 A GB 1310127A GB 297398 A GB297398 A GB 297398A
Authority
GB
United Kingdom
Prior art keywords
oxides
metals
charged
compounds
passed
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
GB1310127A
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.)
IG Farbenindustrie AG
Original Assignee
IG Farbenindustrie 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 IG Farbenindustrie AG filed Critical IG Farbenindustrie AG
Priority to GB1310127A priority Critical patent/GB297398A/en
Publication of GB297398A publication Critical patent/GB297398A/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
    • C07C4/04Thermal processes
    • 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04Oxides
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/02Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the alkali- or alkaline earth metals or beryllium
    • C07C2523/04Alkali metals

Landscapes

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

Abstract

297,398. Johnson, J. Y., (I. G. Farbenindustrie Akt.-Ges.). May 16, 1927. Olefines; diolefines. - Mineral or artificially prepared hydrocarbons containing more than four .carbon atoms in the molecule are converted into olefines and diolefines containing a smaller number of carbon atoms in the molecule than the initial materials by bringing their vapours, at normal or reduced pressure and at a temperature of at least 600‹ C., into contact with catalysts consisting wholly or for the most part of difficulty reducible metallic oxides or mixtures or compounds thereof, alone or in conjunction with supports. A metallic oxide is defined as difficultly reducible if it is not reduced to the metallic state in hydrogen at temperatures up to 600‹ C. The preferred catalysts consist of or are derived from the difficulty reducible oxides of metals situated on or near the maxima, of the atomic volume curve, and in this connection reference is made (1) to the oxides of the alkali and alkaline-earth metals (including magnesium and beryllium) and their oxygen-containing salts, such as aluminates, chromates, tungstates, vanadates, uranates, and phosphates, (2) to oxide combinations which readily emit electrons, such as strontium oxide-barium oxide combinations, alone or on a platinum substratum, and (3) to the oxides of scandium, titanium, yttrium, zirconium, lanthanum, tungsten, molybdenum, thorium, and uranium or mixtures of these or their compounds. The difficultly reducible oxides of metals situated on or near the minima of the atomic volume curve, such as aluminium, chromium, and zinc, are less suitable, but they may be used in the form of their salts with oxygen-containing acids of elements of the fifth, sixth, and seventh periodic groups forming not readily volatile oxides, such as phosphorus, chromium, and vanadium. The catalysts may be used in lump form or deposited on carriers, such as magnesium or aluminium silicate, and metals having a feeble dehydrogenating action, such as copper, platinum, molybdenum, or tungsten, may also be present. Metals having a strong dehydrogenating action, such as iron or nickel, are beneficial if added in small amounts. The process may be carried out in the presence or absence of gases such as nitrogen, carbon dioxide, and water vapour, but halogens or their .compounds, or substantial amounts of hydrogen, must not be present. According to the examples, (1) tetrahydrobenzene vapour is passed at 625‹ C. through a furnace made of porcelain, clay, or noble metal and charged with lumps of lime; the products are fractionally cooled and include ethylene, propylene, butadiene, and butylene; (2) hexahydrobenzene is passed at 600‹ C. through an apparatus made of or lined with quartz or clay and charged with cubes of calcium aluminate; the products include ethylene and butadienes; (3) the vapour of Russian benzine is passed at 625‹ C. through a metal apparatus internally enamelled and charged with lumps of lime; liquid unsaturated hydrocarbons are obtained.
GB1310127A 1927-05-16 1927-05-16 Process for splitting hydrocarbons Expired GB297398A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1310127A GB297398A (en) 1927-05-16 1927-05-16 Process for splitting hydrocarbons

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1310127A GB297398A (en) 1927-05-16 1927-05-16 Process for splitting hydrocarbons

Publications (1)

Publication Number Publication Date
GB297398A true GB297398A (en) 1928-09-17

Family

ID=10016843

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1310127A Expired GB297398A (en) 1927-05-16 1927-05-16 Process for splitting hydrocarbons

Country Status (1)

Country Link
GB (1) GB297398A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2158073A1 (en) * 1971-11-23 1973-05-24 Toyo Engineering Corp Steam cracking of hydrocarbons - to produce olefins, using alkaline earth/alumina catalysts
FR2192162A1 (en) * 1972-07-07 1974-02-08 Rhone Progil

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2158073A1 (en) * 1971-11-23 1973-05-24 Toyo Engineering Corp Steam cracking of hydrocarbons - to produce olefins, using alkaline earth/alumina catalysts
FR2192162A1 (en) * 1972-07-07 1974-02-08 Rhone Progil

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