GB680159A - Process for the utilisation of heavy oils and residues for the production of oxygen-containing organic compounds - Google Patents

Process for the utilisation of heavy oils and residues for the production of oxygen-containing organic compounds

Info

Publication number
GB680159A
GB680159A GB14690/50A GB1469050A GB680159A GB 680159 A GB680159 A GB 680159A GB 14690/50 A GB14690/50 A GB 14690/50A GB 1469050 A GB1469050 A GB 1469050A GB 680159 A GB680159 A GB 680159A
Authority
GB
United Kingdom
Prior art keywords
oxygen
gas
tower
returned
heat exchanger
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
GB14690/50A
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.)
Ruhrchemie AG
Original Assignee
Ruhrchemie 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 Ruhrchemie AG filed Critical Ruhrchemie AG
Publication of GB680159A publication Critical patent/GB680159A/en
Expired legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/36—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/22—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

<PICT:0680159/III/1> Hydrocarbon residues such as heavy oils, tars, and cracked residues are subjected to incomplete combustion with such an amount of oxygen or gas containing free oxygen as to yield a gas mixture, containing 0.7 to 0.9 volumes of hydrogen per volume of carbon monoxide, which is then used in the catalytic synthesis of oxygen-containing organic compounds. Water vapour, carbon dioxide, and/or methane may be added to the oxygen and the combustion should be carried out under elevated pressure. Fuel oil is pumped to combustion chamber 3 from tank 1 and burns with oxygen passing through line 4 and preheater 5. The hot synthesis gas passes through reaction chamber 6 having heat exchanger 7, heat exchanger 5 and cooler 8 to desulphurization device 9. The gas is then passed to synthesis furnace 10 containing an iron catalyst, and the products are separated in device 11 comprising a condenser, a washer, and an activated carbon absorber. The remaining gases pass to wash tower 12 and are washed with water under pressure, which passes to depressurization vessels 13, 14 and degasifying tower 15 to recover carbon dioxide, which is returned to the combustion chamber, and wash liquid, which is returned to tower 12. Methane, obtained as residual gas from tower 12, may be returned to the combustion chamber, or added to the gas before the synthesis furnace. In alternative arrangements the hot gases at say 1,600 DEG C are passed directly through a gas turbine after reaction 6 or the heat exchanger 7 is replaced by the tube system of a closed circuit turbine system.
GB14690/50A 1949-06-27 1950-06-13 Process for the utilisation of heavy oils and residues for the production of oxygen-containing organic compounds Expired GB680159A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE1018552X 1949-06-27

Publications (1)

Publication Number Publication Date
GB680159A true GB680159A (en) 1952-10-01

Family

ID=7711374

Family Applications (1)

Application Number Title Priority Date Filing Date
GB14690/50A Expired GB680159A (en) 1949-06-27 1950-06-13 Process for the utilisation of heavy oils and residues for the production of oxygen-containing organic compounds

Country Status (2)

Country Link
FR (1) FR1018552A (en)
GB (1) GB680159A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1062880B (en) * 1957-10-10 1959-08-06 Bataafsche Petroleum Process for the production of methane-rich gases
DE1102112B (en) * 1958-07-26 1961-03-16 Basf Ag Process for the simultaneous production of synthesis gas and of oxygen and nitrogen
DE1188050B (en) * 1961-08-17 1965-03-04 Conch Int Methane Ltd Process for reforming natural gas
WO2010078871A1 (en) * 2009-01-07 2010-07-15 Aquarden Technologies Aps Method and apparatus for production of hydrogen from methanol

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1185548B (en) * 1959-02-24 1965-01-14 Bernard Taubert Tool set for inserting and removing flexible watch glasses

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1062880B (en) * 1957-10-10 1959-08-06 Bataafsche Petroleum Process for the production of methane-rich gases
DE1102112B (en) * 1958-07-26 1961-03-16 Basf Ag Process for the simultaneous production of synthesis gas and of oxygen and nitrogen
DE1188050B (en) * 1961-08-17 1965-03-04 Conch Int Methane Ltd Process for reforming natural gas
WO2010078871A1 (en) * 2009-01-07 2010-07-15 Aquarden Technologies Aps Method and apparatus for production of hydrogen from methanol
US8586003B2 (en) 2009-01-07 2013-11-19 Aquarden Technologies Aps Method and apparatus for production of hydrogen from methanol

Also Published As

Publication number Publication date
FR1018552A (en) 1953-01-09

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