GB827474A - Process for producing gaseous products of partial combustion of a hydrocarbon oil - Google Patents

Process for producing gaseous products of partial combustion of a hydrocarbon oil

Info

Publication number
GB827474A
GB827474A GB4064/56A GB406456A GB827474A GB 827474 A GB827474 A GB 827474A GB 4064/56 A GB4064/56 A GB 4064/56A GB 406456 A GB406456 A GB 406456A GB 827474 A GB827474 A GB 827474A
Authority
GB
United Kingdom
Prior art keywords
oil
steam
mixture
tube
oxygen
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
GB4064/56A
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.)
Texaco Development Corp
Original Assignee
Texaco Development Corp
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 Texaco Development Corp filed Critical Texaco Development Corp
Publication of GB827474A publication Critical patent/GB827474A/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
    • 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)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

<PICT:0827474/III/1> Hydrocarbon oil is reacted with free oxygen and steam to produce a gaseous mixture, the oil being introduced in liquid form into a stream of steam, the resultant mixture being subjected to turbulent flow through a long tube at a velocity greater than 20 feet, and preferably greater than 30 feet, per second, to effect intimate dispersion of the oil in the steam, the dispersion being fed, at a similar velocity, with added oxygen into a reaction zone, the partial combustion producing a temperature of from 1800 DEG to 3500 DEG F. The long tube is in length, at least 100 times, and preferably at least 500 times, its inside diameter, and the oil-steam mixture is preferably preheated in at least a part of the length of the tube. As shown, a water pump 5 feeds a heated coil 6, the steam in the pipe 7 being admixed with oil from a pump 8. Turbulent flow of the mixture is produced in the tube 11 which is heated. Oxygen, air or oxygen-enriched air is added at 14 and the mixture is admitted directly into the reaction chamber 16. The hot product gases are continuously sprayed with quench water. The steam may be 20-300% of the oil by weight, and the pressure in the tube 11 may be 50-1500 pounds per square inch, the temperature being 300-1000 DEG F. The oil may be preheated to 300-700 DEG F. before mixing with the steam, and the oil may be mixed with pulverized solid fuel. A gas, e.g. natural gas, may be mixed with the steam before the injection of the oil. Heavy metal compounds, e.g. vanadium, nickel, present in petroleum, are detrimental to the refractory, generally alumina, lining of the reaction chamber. To counteract this, at least 0.5% and not more than 10% of the carbon in the oil is liberated as free carbon. Specification 827,475 is referred to.
GB4064/56A 1955-02-10 1956-02-09 Process for producing gaseous products of partial combustion of a hydrocarbon oil Expired GB827474A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US827474XA 1955-02-10 1955-02-10

Publications (1)

Publication Number Publication Date
GB827474A true GB827474A (en) 1960-02-03

Family

ID=22173187

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4064/56A Expired GB827474A (en) 1955-02-10 1956-02-09 Process for producing gaseous products of partial combustion of a hydrocarbon oil

Country Status (1)

Country Link
GB (1) GB827474A (en)

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