GB286206A - Process for the hydrogenation of organic substances, especially of the products of the distillation of coals and petroleum oils - Google Patents

Process for the hydrogenation of organic substances, especially of the products of the distillation of coals and petroleum oils

Info

Publication number
GB286206A
GB286206A GB18997/27A GB1899727A GB286206A GB 286206 A GB286206 A GB 286206A GB 18997/27 A GB18997/27 A GB 18997/27A GB 1899727 A GB1899727 A GB 1899727A GB 286206 A GB286206 A GB 286206A
Authority
GB
United Kingdom
Prior art keywords
pipe
hydrogenation
autoclave
distillation
effected
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
GB18997/27A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of GB286206A publication Critical patent/GB286206A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • 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
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/06—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12—Inorganic carriers

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)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Working-Up Tar And Pitch (AREA)

Abstract

286,206. Hugel, G., Paul, M., and Boistel, M. Feb. 28, 1927, [Convention date]. Hydrogenation, destructive.- The hydrogenation of organic substances, particularly the products of distillation of coal and petroleum is effected by means of hydrides of alkali or alkaline earth metals which are coated with oil substances such as tetrahydronaphthalene or with more readily oxidizable substances such as the amides of the alkali and alkali earth metals. The process may be effected below 300‹ C. and 100 kilos pressure and is not affected by the presence of contact poisons such as nitrogen, sulphur, arsenic, and oxygen compounds. Sodium in finely-divided or fragmentary condition is introduced into an autoclave A having a stirrer a, and hydrogen is admitted under pressure through a branch pipe f by action of a compressor H which draws the gas from a holder G. The sodium hydride which is formed below 300‹ C., is stabilized as described above. The hydrogenation is effected in an autoclave B having stirrers b. The stabilized catalyst and the substance to be hydrogenated are introduced into the autoclave B by a pipe c, which mav also serve for withdrawing the product. Hydrogen is admitted through a pipe d supplied by the compressor H and bubbles through the material in the autoclave. Unused hydrogen escapes by a pipe e to the gas holder G. The product is withdrawn by the pipe c and branch g to a distillation apparatus D. Pitch from coal-tar may be hydrogenated in this manner at about 300‹ C. and below 100 kilos pressure, using about 10 per cent of sodium hydride. The product is a liquid which on distillation yields fractions from benzene to heavy oils. The treatment of natural asphaltum is also mentioned. Specification 18232/14 is referred to. The Specification as open to inspection under Sect. 91 (3) (a) states that the hydrides may be made during the process. This subject-matter does not appear in the Specification as accepted.
GB18997/27A 1927-02-28 1927-07-18 Process for the hydrogenation of organic substances, especially of the products of the distillation of coals and petroleum oils Expired GB286206A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE286206X 1927-02-28

Publications (1)

Publication Number Publication Date
GB286206A true GB286206A (en) 1928-12-18

Family

ID=6059005

Family Applications (1)

Application Number Title Priority Date Filing Date
GB18997/27A Expired GB286206A (en) 1927-02-28 1927-07-18 Process for the hydrogenation of organic substances, especially of the products of the distillation of coals and petroleum oils

Country Status (1)

Country Link
GB (1) GB286206A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005061665A3 (en) * 2003-12-19 2006-04-20 Shell Oil Co Systems and methods of producing a crude product
US7763160B2 (en) 2003-12-19 2010-07-27 Shell Oil Company Systems and methods of producing a crude product

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005061665A3 (en) * 2003-12-19 2006-04-20 Shell Oil Co Systems and methods of producing a crude product
US7763160B2 (en) 2003-12-19 2010-07-27 Shell Oil Company Systems and methods of producing a crude product
US7811445B2 (en) 2003-12-19 2010-10-12 Shell Oil Company Systems and methods of producing a crude product
US7828958B2 (en) 2003-12-19 2010-11-09 Shell Oil Company Systems and methods of producing a crude product
US7879223B2 (en) 2003-12-19 2011-02-01 Shell Oil Company Systems and methods of producing a crude product
US7959797B2 (en) 2003-12-19 2011-06-14 Shell Oil Company Systems and methods of producing a crude product
US8025791B2 (en) 2003-12-19 2011-09-27 Shell Oil Company Systems and methods of producing a crude product
US8070936B2 (en) 2003-12-19 2011-12-06 Shell Oil Company Systems and methods of producing a crude product
US8394254B2 (en) 2003-12-19 2013-03-12 Shell Oil Company Crude product composition
US8608938B2 (en) 2003-12-19 2013-12-17 Shell Oil Company Crude product composition
US8613851B2 (en) 2003-12-19 2013-12-24 Shell Oil Company Crude product composition
US8663453B2 (en) 2003-12-19 2014-03-04 Shell Oil Company Crude product composition

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