GB355214A - Improved manufacture of lubricating oils - Google Patents

Improved manufacture of lubricating oils

Info

Publication number
GB355214A
GB355214A GB5399/30A GB539930A GB355214A GB 355214 A GB355214 A GB 355214A GB 5399/30 A GB5399/30 A GB 5399/30A GB 539930 A GB539930 A GB 539930A GB 355214 A GB355214 A GB 355214A
Authority
GB
United Kingdom
Prior art keywords
wax
oil
per cent
oils
hours
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
GB5399/30A
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 Co
Original Assignee
Standard Oil 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 Co filed Critical Standard Oil Co
Publication of GB355214A publication Critical patent/GB355214A/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
    • C10G57/00Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process
    • C10G57/02Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process with polymerisation
    • 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/10Lubricating oil

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)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Lubricating oils are obtained by cracking hydrocarbons consisting of not less than 30 per cent of hydrocarbon wax, and polymerizing the product, or fractions thereof, in presence of a polymerizing agent. Suitably, paraffin wax, slop wax, ozokerite, slack wax, or sweat oil is cracked substantially as vapour at 750-1100 DEG F. at atmospheric pressure or pressures below or above 100 lb., and one or more wax-free fractions up to an end point of 500 DEG F. are agitated at 100-250 DEG F. for 3-50 hours in presence of 0.5-4.0 per cent of aluminium chloride. Most of the sludge is removed by settling and decantation; the remainder by filtering with clay fines or other adsorbemt, or by prolonged settling, e.g. 48 hours at 100-150 DEG F. The oil may be neutralized by a 5-10 per cent solution of caustic soda, and freed from light oils and naphtha by distillation. The product may be fractioned to yield oils of desired viscosity. The aluminium chloride sludge may be used to polymerize fresh oil wholly or in part. In an example, slack wax or sweat oil from Midcontinent oil is vaporized, and the vapours are passed at atmospheric pressure through a continuous pipe still or a pipe still and digesting chamber at 900-980 DEG F. The vapours are freed from base and fractionally condensed, condensate above 500 DEG F. being mixed with raw material for cracking. The distillate up to 500 DEG F. is mixed with 1-3 per cent of aluminium chloride, and agitated at 210 DEG F. for 18 hours, Specification 141,753, [Class 91, Oils &c.], is referred to.
GB5399/30A 1929-03-15 1930-02-18 Improved manufacture of lubricating oils Expired GB355214A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US355214XA 1929-03-15 1929-03-15

Publications (1)

Publication Number Publication Date
GB355214A true GB355214A (en) 1931-08-18

Family

ID=21883213

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5399/30A Expired GB355214A (en) 1929-03-15 1930-02-18 Improved manufacture of lubricating oils

Country Status (1)

Country Link
GB (1) GB355214A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE763062C (en) * 1935-08-25 1952-11-24 Ruhrchemie Ag Process for the production of high molecular weight hydrocarbon oils

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE763062C (en) * 1935-08-25 1952-11-24 Ruhrchemie Ag Process for the production of high molecular weight hydrocarbon oils

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