US1776753A - Manufacture of lubricating oils - Google Patents

Manufacture of lubricating oils Download PDF

Info

Publication number
US1776753A
US1776753A US281369A US28136928A US1776753A US 1776753 A US1776753 A US 1776753A US 281369 A US281369 A US 281369A US 28136928 A US28136928 A US 28136928A US 1776753 A US1776753 A US 1776753A
Authority
US
United States
Prior art keywords
manufacture
stock
distillation
lubricating oils
constituents
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 - Lifetime
Application number
US281369A
Inventor
Edeleanu Lazar
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.)
Edeleanu GmbH
Original Assignee
Edeleanu GmbH
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 Edeleanu GmbH filed Critical Edeleanu GmbH
Application granted granted Critical
Publication of US1776753A publication Critical patent/US1776753A/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • C10G19/00Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment
    • 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
    • C10G21/00Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/06Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
    • C10G21/08Inorganic compounds only
    • C10G21/10Sulfur dioxide

Definitions

  • the present invention pertains to the manufacture of lubricating oils, and aims to produce lubricating oils of superior properties from mineral oils.
  • distillation products thus obtained are distinguished from those heretofore produced by complete freedom from acid, by
  • eating 0115 which comprises treating with reduced content of tar, by stability of color, and by increased resistance to oxidation.
  • the process may be operated as follows: 1 v.
  • the residual material obtained after ex tracting the lubricating oil stock with liquefied sulfur dioxide at a' temperature between 10 C. and +30 'C. is mixed with a concentrated aqueous solution of caustic soda amounting to 1% of NaOH in respect of the oil treated, and the mixture is thoroughly agitated prior to being distilled.
  • the distillation proceeds preferably in the known manner according to the vacuum process, with a pressure of 7-15 mm. mercury, and with or without passing a current of steam throughthe stillfitHighly satisfactory results have thus been obtained?
  • the process is not restricted to the specific materials and exactv operations described, but may be applied to the production of lubricating oils generally from .available petroleum stocks, particularly in the Texas and California fields.
  • the step in the manufacture of 1ubrieating oils which comprises treating with lique ed sulfur dioxide petroleum lubricating oil stock obtained by fractional distillation, and subjecting the portion insoluble in liquefied sulfurous acid to vacuum distillation under a pressure of 7-15 mm. mercury in the presence ofa concentrated aqueous solution of caustic soda.
  • An acid free lubricating oil low in tar obtained by the treatment of suitable min-- eral oil fractions'with liquefied sulfur dioxide to dissolve unsaturated hydrocarbons and separation of the latter to remove the constituents soluble thereimfollowed by distillation of the insoluble constituents in the presence of an alkali.
  • a substantially acid-free lubricating oil of low viscosity and tar content obtained by the extraction of suitable natural mineral oil fractionswith liquefied sulfur dioxide to dissolve unsaturated hydrocarbons and sepa-.
  • a substantially acid-free lubricating oil of low viscosity and tar content obtained by the extraction of suitable natural mineral oil fractions with liquefied sulfur dioxide to dissolve unsaturated hydrocarbons and separation of the latter to remove the constituents soluble therein, followed by distillation of the insoluble constituents in the presence of an alkali and steam.

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

Description

Patented Sept. 23, 1930 UNITED STATES PATENT orrlca GESELLSCHAFT, M. H., OF BERLIN, GERMANY MANUFACTURE OI LUBBICATING OILS No Drawing. Application filed May 28, 1928, Serial No. 281,369, and in Great Britain April 14, 1928.
The present invention pertains to the manufacture of lubricating oils, and aims to produce lubricating oils of superior properties from mineral oils.
" More particularly, it relates to the treatment of lubricating oil stock after removing the lighter fractions, and consists in subjecting appropriate mineral oil fractions to the Well known extractiontreatment with liquefied sulfur dioxide to remove constituf ents soluble therein, for exam le, unsatu-. rated aromatic hydrocarbons, followed by distillation of the insoluble constituents in the presence of a little alkali, with or with out reduced pressure, and with or without the presence of water vapor.
The distillation products thus obtained are distinguished from those heretofore produced by complete freedom from acid, by
eating 0115 which comprises treating with reduced content of tar, by stability of color, and by increased resistance to oxidation.
In particular (a) all of the fractions obtained when distilling previously extracted lubricating oil stock in the presence of'causv tic soda are completely free from acid; (b) the tar content is on the average 2% less than with the same extracted stock not distilled in the presence of caustic soda or alkali. a
By way of example, the process may be operated as follows: 1 v.
The residual material obtained after ex tracting the lubricating oil stock with liquefied sulfur dioxide at a' temperature between 10 C. and +30 'C. is mixed with a concentrated aqueous solution of caustic soda amounting to 1% of NaOH in respect of the oil treated, and the mixture is thoroughly agitated prior to being distilled. The distillation proceeds preferably in the known manner according to the vacuum process, with a pressure of 7-15 mm. mercury, and with or without passing a current of steam throughthe stillfitHighly satisfactory results have thus been obtained? The process is not restricted to the specific materials and exactv operations described, but may be applied to the production of lubricating oils generally from .available petroleum stocks, particularly in the Texas and California fields.
I claim the following as my. invention:.
1. In the manufacture. of lubricating oil from mineral oil stock, extracting the stock with liquefied sulphur dioxide at low temperatures toseparate the, desirable lubricating stock from the soluble undesirable constituents and distilling the insoluble lubricatin stock in the presence of an alkali.
2. n the manufacture of lubricating oil from mineral oil stock, extracting the stock with liquefied sulphur dioxide at low temperatures to separate the desirable lubricating stock from the soluble undesirable constituents and distilling'the insoluble lubrieating stock under a Vacuum in the presence of an alkali.
3. The step in the manufacture of lubrilique d sulfur dioxide petroleum lubricatoil stock obtained by fractional distillation, and subjecting the portion insoluble in-liquefied sulfurous acid to distillation in the presence of a concentrated aqueous solution of caustic soda amounting to 1% NaOH with respect to the oil being treated.
4. The step in the manufacture of 1ubrieating oils which comprises treating with lique ed sulfur dioxide petroleum lubricating oil stock obtained by fractional distillation, and subjecting the portion insoluble in liquefied sulfurous acid to vacuum distillation under a pressure of 7-15 mm. mercury in the presence ofa concentrated aqueous solution of caustic soda.
5. An acid free lubricating oil low in tar obtained by the treatment of suitable min-- eral oil fractions'with liquefied sulfur dioxide to dissolve unsaturated hydrocarbons and separation of the latter to remove the constituents soluble thereimfollowed by distillation of the insoluble constituents in the presence of an alkali.
. 6. A substantially acid-free lubricating oil of low viscosity and tar content obtained by the extraction of suitable natural mineral oil fractionswith liquefied sulfur dioxide to dissolve unsaturated hydrocarbons and sepa-.
ration of the latter to remove the constituents 2 r mam soluble therein, followed by vacuum distillation of the insoluble constituents in the presence of an alkali.
7. A substantially acid-free lubricating oil of low viscosity and tar content obtained by the extraction of suitable natural mineral oil fractions with liquefied sulfur dioxide to dissolve unsaturated hydrocarbons and separation of the latter to remove the constituents soluble therein, followed by distillation of the insoluble constituents in the presence of an alkali and steam.
In testimony whereoflI have signed my name to this specification.
' LAZAR EDELEANU.
US281369A 1928-04-14 1928-05-28 Manufacture of lubricating oils Expired - Lifetime US1776753A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1776753X 1928-04-14

Publications (1)

Publication Number Publication Date
US1776753A true US1776753A (en) 1930-09-23

Family

ID=10890372

Family Applications (1)

Application Number Title Priority Date Filing Date
US281369A Expired - Lifetime US1776753A (en) 1928-04-14 1928-05-28 Manufacture of lubricating oils

Country Status (1)

Country Link
US (1) US1776753A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2905638A (en) * 1956-06-11 1959-09-22 Phillips Petroleum Co Removal of sulfur dioxide from oils
US2966456A (en) * 1957-01-02 1960-12-27 Sun Oil Co Removing acids from petroleum

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2905638A (en) * 1956-06-11 1959-09-22 Phillips Petroleum Co Removal of sulfur dioxide from oils
US2966456A (en) * 1957-01-02 1960-12-27 Sun Oil Co Removing acids from petroleum

Similar Documents

Publication Publication Date Title
US2276526A (en) Process for refining hydrocarbon oils
US2217918A (en) Process of producing rubber miscible oils
US1776753A (en) Manufacture of lubricating oils
US2018715A (en) Treating hydrocarbon oils with formaldehyde, a condensing agent, and acetic acid
US2420108A (en) Process for treating a solvent-extracted petroleum distillate with clay and lime
US2024106A (en) Preparation of fluorescent and pour point reducing bodies from petroleum residue
US2142916A (en) Treating lubricating oils
US2070627A (en) Oxidation refining of lubricating oil
US2010423A (en) Method of manufacturing asphalt and product thereof
US2308184A (en) Art of producing wax modifying agents
US2313385A (en) Process of extraction of oils from hardwood tar and purification thereof
US2178321A (en) Solvent refining
US2036973A (en) Method of preparing valuable hydrocarbon products from acid sludge
US2035868A (en) Treatment of tars
DE657171C (en) Process for the production of hydrocarbons soluble in sulfuric acid
US1816872A (en) Process of refining lubricating oils
US2711990A (en) Refining of lubricating oils
US1631401A (en) Process of making motor fuel
US2058696A (en) Process of stabilizing oils
US1521283A (en) Art of refining oils
US2249276A (en) Treatment of cracked hydrocarbon distillates
US1851580A (en) Manufacture of white oils
US1883374A (en) Treatment of oils
US2108448A (en) Purification of naphthenic acids
US2210867A (en) Manufacture of lubricating oil