GB332336A - Improvements in the working up of distillable carbonaceous liquids containing substances of high molecular weight - Google Patents

Improvements in the working up of distillable carbonaceous liquids containing substances of high molecular weight

Info

Publication number
GB332336A
GB332336A GB1520029A GB1520029A GB332336A GB 332336 A GB332336 A GB 332336A GB 1520029 A GB1520029 A GB 1520029A GB 1520029 A GB1520029 A GB 1520029A GB 332336 A GB332336 A GB 332336A
Authority
GB
United Kingdom
Prior art keywords
adsorbent
adsorbents
catalyst
treated
molecular 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.)
Expired
Application number
GB1520029A
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 GB1520029A priority Critical patent/GB332336A/en
Publication of GB332336A publication Critical patent/GB332336A/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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/24Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
    • 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/24Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
    • C10G47/26Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles suspended in the oil, e.g. slurries

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)

Abstract

332,336. Johnson, J. Y., (I. G. Farbenindustrie Akt.-Ges.). May 15, 1929. Hydrogenation, destructive. - In obtaining valuable hydrocarbon products from carbonaceous liquids containing substances of high molecular weight, the latter are removed from the liquids by adsorbents, and are destructively hydrogenated together with the adsorbents at elevated temperatures and pressures. The treatment with adsorbents may be carried out at ordinary or elevated temperatures, and the treated liquid mav be worked up further in any desired manner. Suitable adsorbents are silica gel and alumina gel; preferably the adsorbent should also be a destructive hydrogenation catalyst, such as molybdic acid, or alternatively should be impregnated with such a catalyst. The adsorbent may be used in a colloidal state. After the destructive hydrogenation the adsorbent may be regenerated and used again. In an example, a middle oil containing 7 per cent of constituents boiling between 325‹ C. and 350‹ C. and 5 per cent boiling above 350‹ C. is treated at 70-80 C‹. with a silica adsorbent which has been made catalytic by impregnation with a solution of the nitrates of molybdenum and zinc, followed by heat treatment. The middle oil is separated by centrifuging from the adsorbent and is destructively hydrogenated at 440-450‹ C. and under a pressure of 200 atmospheres of hydrogen in the presence of a catalyst containing molybdic and chromic acids. The activity of the catalyst remains practically unimpaired, whereas, without the preliminary treatment with adsorbent, poisoning occurs rapidly. The adsorbent and adsorbed substances are treated with hydrogen at 460‹ C. and 200 atmospheres. and the low-boiling products formed are returned to the main process. The adsorbent is preferably regenerated by heating for re-use.
GB1520029A 1929-05-15 1929-05-15 Improvements in the working up of distillable carbonaceous liquids containing substances of high molecular weight Expired GB332336A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1520029A GB332336A (en) 1929-05-15 1929-05-15 Improvements in the working up of distillable carbonaceous liquids containing substances of high molecular weight

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1520029A GB332336A (en) 1929-05-15 1929-05-15 Improvements in the working up of distillable carbonaceous liquids containing substances of high molecular weight

Publications (1)

Publication Number Publication Date
GB332336A true GB332336A (en) 1930-07-24

Family

ID=10054787

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1520029A Expired GB332336A (en) 1929-05-15 1929-05-15 Improvements in the working up of distillable carbonaceous liquids containing substances of high molecular weight

Country Status (1)

Country Link
GB (1) GB332336A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4071435A (en) * 1977-06-06 1978-01-31 Atlantic Richfield Company Denitrogenation of syncrude
GB2142930A (en) * 1983-03-19 1985-01-30 Asahi Chemical Ind A process for cracking a heavy hydrocarbon
FR2556000A1 (en) * 1983-12-02 1985-06-07 Asahi Chemical Ind Process for converting a heavy hydrocarbon into a product of higher value or a lighter one

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4071435A (en) * 1977-06-06 1978-01-31 Atlantic Richfield Company Denitrogenation of syncrude
GB2142930A (en) * 1983-03-19 1985-01-30 Asahi Chemical Ind A process for cracking a heavy hydrocarbon
US4770764A (en) * 1983-03-19 1988-09-13 Asahi Kasei Kogyo Kabushiki Kaisha Process for converting heavy hydrocarbon into more valuable product
FR2556000A1 (en) * 1983-12-02 1985-06-07 Asahi Chemical Ind Process for converting a heavy hydrocarbon into a product of higher value or a lighter one

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