GB340811A - An improved process for obtaining valuable distillates by the destructive hydrogenation of carbonaceous materials - Google Patents

An improved process for obtaining valuable distillates by the destructive hydrogenation of carbonaceous materials

Info

Publication number
GB340811A
GB340811A GB2085/30A GB208530A GB340811A GB 340811 A GB340811 A GB 340811A GB 2085/30 A GB2085/30 A GB 2085/30A GB 208530 A GB208530 A GB 208530A GB 340811 A GB340811 A GB 340811A
Authority
GB
United Kingdom
Prior art keywords
oil
pipe
valve
reaction
pump
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
GB2085/30A
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.)
Standard Oil Development Co
Original Assignee
Standard Oil Development Co
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 Standard Oil Development Co filed Critical Standard Oil Development Co
Publication of GB340811A publication Critical patent/GB340811A/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
    • 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
    • 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
    • C10G1/065—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 in the presence of a solvent

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

In the destructive hydrogenation of fluent carbonaceous materials such as petroleum, tars, and suspensions of coal in oil, a portion of the reaction mixture is withdrawn from the reaction vessel and the pressure on this portion is reduced so that a substantial part of the hydrocarbon liquid is distilled. Oil or the like, heated in a pipe still 1, passes to a reaction drum 3, from which a part of the oil is continuously re-cycled by a pump 6 back to the pipe still. Hydrogen is pumped by a compresser 8 into the still through valve 11, and into the reaction drum through valve 12. Vapours pass from the drum to a heat-exchanger 15 and condenser 16; hydrogen purified, if necessary, from hydrogen sulphide and gaseous hydrocarbons, is returned by a pump 18 to the pipe 10. A part <PICT:0340811/III/1> of the reaction mass is withdrawn by a pipe 19 through a pressure reduction valve 20 to a vaporizing chamber 21. Solid residues are discharged through a double bell closure 23<1>, and vapours are passed through a condenser 25 to a gas separator 26. Inert gas may be introduced through a valve 21a. Fresh oil is introduced into the system by pumps 31, 33 through the preheater 15 and the pipe 34. Carbonaceous solids may be added from a pulverizer 32, and oil from the separator 26 may be re-cycled through a pump 29.
GB2085/30A 1929-01-22 1930-01-21 An improved process for obtaining valuable distillates by the destructive hydrogenation of carbonaceous materials Expired GB340811A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US334148A US1940648A (en) 1929-01-22 1929-01-22 Process for obtaining valuable distillates from carbonaceous materials

Publications (1)

Publication Number Publication Date
GB340811A true GB340811A (en) 1931-01-08

Family

ID=23305806

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2085/30A Expired GB340811A (en) 1929-01-22 1930-01-21 An improved process for obtaining valuable distillates by the destructive hydrogenation of carbonaceous materials

Country Status (4)

Country Link
US (1) US1940648A (en)
FR (1) FR687415A (en)
GB (1) GB340811A (en)
NL (1) NL29952C (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2453641A (en) * 1944-02-05 1948-11-09 Lummus Co Method of producing colloidal fuel
US3505203A (en) * 1967-06-26 1970-04-07 Universal Oil Prod Co Solvent extraction method
US3505202A (en) * 1967-06-26 1970-04-07 Universal Oil Prod Co Solvent extraction method
US3503864A (en) * 1967-12-29 1970-03-31 Universal Oil Prod Co Coal liquefaction method
US3477941A (en) * 1968-01-25 1969-11-11 Universal Oil Prod Co Method of treating coal
DE2943494C2 (en) * 1979-10-27 1987-04-16 Basf Ag, 6700 Ludwigshafen Process for producing liquid hydrocarbons from coal
US4324644A (en) * 1980-08-26 1982-04-13 Occidental Research Corporation Pyrolysis process for stabilizing volatile hydrocarbons utilizing a beneficially reactive gas
US4324637A (en) * 1980-08-26 1982-04-13 Occidental Research Corporation Pyrolysis process with feed pretreatment utilizing a beneficially reactive gas
US4324640A (en) * 1980-08-26 1982-04-13 Occidental Research Corporation Pyrolysis process
US4324641A (en) * 1980-08-26 1982-04-13 Occidental Research Corporation Pyrolysis process utilizing a beneficially reactive gas
US4324643A (en) * 1980-08-26 1982-04-13 Occidental Research Corporation Pyrolysis process for producing condensed stabilized hydrocarbons
US4324638A (en) * 1980-08-26 1982-04-13 Occidental Research Corporation Pyrolysis process for stabilizing volatile hydrocarbons
US4324639A (en) * 1980-08-26 1982-04-13 Occidental Research Corporation Pyrolysis process with feed pretreatment
US4324642A (en) * 1980-08-26 1982-04-13 Occidental Research Corporation Pyrolysis process for producing condensed stabilized hydrocarbons utilizing a beneficially reactive gas
DE3914057A1 (en) * 1989-04-28 1990-10-31 Ruhrkohle Ag STRIPING OF RESIDUES

Also Published As

Publication number Publication date
NL29952C (en)
FR687415A (en) 1930-08-08
US1940648A (en) 1933-12-19

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