GB665720A - Process for manufacturing oil gas - Google Patents

Process for manufacturing oil gas

Info

Publication number
GB665720A
GB665720A GB25127/49A GB2512749A GB665720A GB 665720 A GB665720 A GB 665720A GB 25127/49 A GB25127/49 A GB 25127/49A GB 2512749 A GB2512749 A GB 2512749A GB 665720 A GB665720 A GB 665720A
Authority
GB
United Kingdom
Prior art keywords
zone
gas
unit
blow
make
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
GB25127/49A
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.)
GAS MACHINERY CO
Original Assignee
GAS MACHINERY 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 GAS MACHINERY CO filed Critical GAS MACHINERY CO
Publication of GB665720A publication Critical patent/GB665720A/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
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • 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
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/34Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts
    • C10G9/36Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
    • C10G9/38Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours produced by partial combustion of the material to be cracked or by combustion of another hydrocarbon

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Incineration Of Waste (AREA)

Abstract

665,720. Oil gas generation. GAS MACHINERY CO. Sept. 30, 1949 [Oct. 1, 1948], No. 26127/49. Class 55 (ii). Oil gas is generated alternately, after intervening blow periods, in each of a pair of units 10, 11, comprising fixing and combustion-vaporizing zones 12, 13 and 14, 15. Zones 14, 15 are connected, or may be developed into a single chamber, and an air inlet is provided at the gas exit end of each unit. After each unit has been heated the cycle is started by passing air down unit 10 and into zone 15 to which a fluid fuel such as petroleum oil, tar, or gas is also admitted. The heat generated by burning off carbon previously deposited in zones 12, 14 reduces the amount of fuel required; supplementary air may be supplied. Combustion products pass through zone 13 to the stack. In the make stage gas-making oil and desirably a diluent, e.g. steam are admitted to zone 15 and gases generated are fixed in zone 13 at about 1000- 1400‹ F. and discharged to a wash box. The next two stages consist of a blow and a make period with unit 10 replacing unit 11. Purges may be effected between stages; thus, blasts of air and steam may be swept through the units between the blow and make and the make and blow stages respectively. High residual carbon oils may be utilized; the temperature at the exit of the fixing zone is e.g. 100-500‹ F. lower than in normal processes. Specifications 515,996 and 665,721 are referred to.
GB25127/49A 1948-10-01 1949-09-30 Process for manufacturing oil gas Expired GB665720A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US665720XA 1948-10-01 1948-10-01
US1001746XA 1948-10-01 1948-10-01
US52283A US2580766A (en) 1948-10-01 1948-10-01 Process for manufacturing oil gas

Publications (1)

Publication Number Publication Date
GB665720A true GB665720A (en) 1952-01-30

Family

ID=27368110

Family Applications (1)

Application Number Title Priority Date Filing Date
GB25127/49A Expired GB665720A (en) 1948-10-01 1949-09-30 Process for manufacturing oil gas

Country Status (2)

Country Link
US (1) US2580766A (en)
GB (1) GB665720A (en)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2734810A (en) * 1956-02-14 Method of making oil gas interchangeable with natural gas
BE498451A (en) * 1949-10-03
US7846401B2 (en) 2005-12-23 2010-12-07 Exxonmobil Research And Engineering Company Controlled combustion for regenerative reactors
US7914667B2 (en) * 2007-06-04 2011-03-29 Exxonmobil Chemical Patents Inc. Pyrolysis reactor conversion of hydrocarbon feedstocks into higher value hydrocarbons
WO2009051936A2 (en) * 2007-10-12 2009-04-23 Schlumberger Canada Limited Methods and apparatus to change the mobility of formation fluids using thermal and non-thermal stimulation
US8278231B2 (en) * 2008-11-24 2012-10-02 Exxonmobil Chemical Patents Inc. Heat stable formed ceramic, apparatus and method of using the same
US8512663B2 (en) 2009-05-18 2013-08-20 Exxonmobile Chemical Patents Inc. Pyrolysis reactor materials and methods
US8450552B2 (en) 2009-05-18 2013-05-28 Exxonmobil Chemical Patents Inc. Pyrolysis reactor materials and methods
US8399372B2 (en) * 2009-05-18 2013-03-19 Exxonmobil Chemical Patents Inc. Stabilized ceramic composition, apparatus and methods of using the same
US8932534B2 (en) 2009-11-20 2015-01-13 Exxonmobil Chemical Patents Inc. Porous pyrolysis reactor materials and methods
US9963641B2 (en) 2011-05-26 2018-05-08 Exxonmobil Chemical Patents Inc. Method of flushing pyrolysis reactor

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2192815A (en) * 1937-12-10 1940-03-05 Combustion Utilities Corp Manufacture of combustible gas

Also Published As

Publication number Publication date
US2580766A (en) 1952-01-01

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