US2198562A - Method of making sulphurized - Google Patents

Method of making sulphurized Download PDF

Info

Publication number
US2198562A
US2198562A US2198562DA US2198562A US 2198562 A US2198562 A US 2198562A US 2198562D A US2198562D A US 2198562DA US 2198562 A US2198562 A US 2198562A
Authority
US
United States
Prior art keywords
sulphur
oil
sulphurized
cutting
making
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
Publication date
Application granted granted Critical
Publication of US2198562A publication Critical patent/US2198562A/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
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M135/00Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing sulfur, selenium or tellurium
    • C10M135/02Sulfurised compounds
    • C10M135/06Esters, e.g. fats
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/20Metal working
    • C10N2040/22Metal working with essential removal of material, e.g. cutting, grinding or drilling
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2060/00Chemical after-treatment of the constituents of the lubricating composition
    • C10N2060/10Chemical after-treatment of the constituents of the lubricating composition by sulfur or a compound containing sulfur

Definitions

  • Our present invention relates to an improved method of making a sulphurized cutting oil.
  • Cutting oils as at present used are of two kinds: (1) the oil is emulsified with water and the emulsion used for cooling and lubricating. the
  • the crude tall oil is purified by distillation and K separation of the rosin acids by crystallization.
  • Tall oil is capable of absorbing in excess of 25% by weight of sulphur.
  • the sulphurized tall oil is then as a rule diluted with other oils having lubricating quali- 25 ties, either vegetable or mineral or both (previously saturated with sulphur), the sulphurretaining capacity. of which is substantially less than that of the tall oil.
  • the sulphur should be heated with tall oil until such time as a test sample when cooled shows no deposition of sulphur, but in general for a timeless than four hours, after which appreciable decomposition of the oil results especially at the higher temperatures as evidenced by the evolution of hydrogen sulphide.
  • the temperature should not be substantially less than 300 F. nor substantially over 400 F.
  • the sulphur present should go into solution before any substantial evolution of hydrogen sulphide occurs; should appreciable quantities of hydrogen sulphide be formed, the heating should be stopped and the mixture allowed to'cool and either decanted from the uhdissolved sulphur or filtered, since continued heating under these circumstances will result in destruction of the oil substance.
  • the tall 011 is first sulphurizedand then diluted with lubricating (cutting) oil, if desired the tall oil may be at least partly diluted prior to the sulphurizing operation.
  • the tall oil may be at least partly diluted prior to the sulphurizing operation.
  • oils by heating tall oil with agitation with up to byweight of sulphur in the temperature range 01' approximately 300-400 F. the step of. controlling the solution of the sulphur to give a minimum of sludging by terminating the heating within a period of from two to four hours, beyond which period a greater amount of sludge will be produced.

Description

Patented Apr. 23, 1940 UNITED S ATES PATENT orrics METHOD or MAKING SULPHURIZE CUTTING OILS Arthur Pollak and Randall Hastings, New York,
. N. Y., assignors to West Virginia Pulp and Paper Company, New York, N. Y., a corporation of Delaware No Drawing. Application April 27, 1939,
Serial No.
1 Claim.
Our present invention relates to an improved method of making a sulphurized cutting oil. Cutting oils as at present used are of two kinds: (1) the oil is emulsified with water and the emulsion used for cooling and lubricating. the
metal during the cutting operation; (2) the oil;
and rosin acids occurring in pine and other nondeciduous woods, and is obtained as a by-product in paper manufacture. In some instances the crude tall oil is purified by distillation and K separation of the rosin acids by crystallization.
Tall oil, especially the refined variety, is capable of absorbing in excess of 25% by weight of sulphur. The sulphurized tall oil is then as a rule diluted with other oils having lubricating quali- 25 ties, either vegetable or mineral or both (previously saturated with sulphur), the sulphurretaining capacity. of which is substantially less than that of the tall oil.
Difliculty has been experienced in maintaining an the quality of such cutting oils, as ordinarily the sulphurized oil deposits a sludge upon standing which detracts from the usefulness of the oil for cutting purposes. We have now discovered that this deposition of sludge may be reduced to a. ragpoint where such sludge is no longer objectionable. In general our method consists in heating the tall oil and sulphur in admixture therewith under controlled conditions as to time and temperature. For the best understanding of our 49 inveptionreterence is made to the following specific example illustrative thereof: 400 grams or refined tall oil is placedin a flask provided with a thermometer, the flask atc-tached to a stirrer and placed in a vat of trias cresyl phosphate heated by a Bunsen burner. 80 grams (20%) of powdered sulphur is added and the heating continued with agitation until a temperature of 350? I". is reached. Alter maintaining'the temperature at this value for two hours c a clear solutionjs obtained upon cooling.- When sulphurized tall oil so prepared was diluted with a mineral cutting oil nine times its weight the solution remainedclear. A sample oi the oil so obtained was kept at 200 F. for ten'days and iound to yield only 0.64% sludge.
In general the following conditions are to be, observed: The sulphur should be heated with tall oil until such time as a test sample when cooled shows no deposition of sulphur, but in general for a timeless than four hours, after which appreciable decomposition of the oil results especially at the higher temperatures as evidenced by the evolution of hydrogen sulphide. The temperature, on the other hand, should not be substantially less than 300 F. nor substantially over 400 F. By observing these conditions, from to 30% of sulphur may be incorporated in the tall oil and a stable product obtained which may be diluted with a hydrocarbon or other cutting oil and such mixture used directly for cutting purposes or emulsified with water in known man ner. In general an optimum time and temperature within the limits above stated will be found for various amounts of sulphur. Thus, in a series of test runs the sludge deposition was found to result when using 15% sulphur at 350 F. temperature in three hours heating time; for
% sulphur, minimum deposition occurred with two hours heating time at the same temperature; with sulphur, minimum deposition was found 85 to result at 400 F. and two hours heating time, temperatures higher or lower, or different periods of heating giving' a greater' amount -of sludge. The sulphur present should go into solution before any substantial evolution of hydrogen sulphide occurs; should appreciable quantities of hydrogen sulphide be formed, the heating should be stopped and the mixture allowed to'cool and either decanted from the uhdissolved sulphur or filtered, since continued heating under these circumstances will result in destruction of the oil substance. v v
While preferably the tall 011 is first sulphurizedand then diluted with lubricating (cutting) oil, if desired the tall oil may be at least partly diluted prior to the sulphurizing operation. Other variations in the disclosed method will occur to,those skilled in the art within the scope of our invention.
We claim: 45
- In the method of making sulphurized cutting, oils by heating tall oil with agitation with up to byweight of sulphur in the temperature range 01' approximately 300-400 F., the step of. controlling the solution of the sulphur to give a minimum of sludging by terminating the heating within a period of from two to four hours, beyond which period a greater amount of sludge will be produced.
- ARTHUR POLLAK.
RANDALL memos.
US2198562D Method of making sulphurized Expired - Lifetime US2198562A (en)

Publications (1)

Publication Number Publication Date
US2198562A true US2198562A (en) 1940-04-23

Family

ID=3431221

Family Applications (1)

Application Number Title Priority Date Filing Date
US2198562D Expired - Lifetime US2198562A (en) Method of making sulphurized

Country Status (1)

Country Link
US (1) US2198562A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2417283A (en) * 1942-12-23 1947-03-11 Standard Oil Dev Co Lubricant
US2429198A (en) * 1944-06-08 1947-10-14 Socony Vacuum Oil Co Inc Cutting oil composition
US2431737A (en) * 1943-06-30 1947-12-02 Nopco Chem Co Noncorrosive lubricating composition
US2631129A (en) * 1949-06-02 1953-03-10 Tide Water Associated Oil Comp Sulfurized tall oil-containing compositions
US2870132A (en) * 1957-01-22 1959-01-20 Ridbo Lab Inc Low viscosity sulfurized tall oil and process for making the same

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2417283A (en) * 1942-12-23 1947-03-11 Standard Oil Dev Co Lubricant
US2431737A (en) * 1943-06-30 1947-12-02 Nopco Chem Co Noncorrosive lubricating composition
US2429198A (en) * 1944-06-08 1947-10-14 Socony Vacuum Oil Co Inc Cutting oil composition
US2631129A (en) * 1949-06-02 1953-03-10 Tide Water Associated Oil Comp Sulfurized tall oil-containing compositions
US2870132A (en) * 1957-01-22 1959-01-20 Ridbo Lab Inc Low viscosity sulfurized tall oil and process for making the same

Similar Documents

Publication Publication Date Title
US2198562A (en) Method of making sulphurized
US1319129A (en) Henry matthew wells
US2289438A (en) Sulphurization of esters
US2313611A (en) Process of sulphurization
US2198567A (en) Driving journal lubricant
US2167439A (en) Sulphur cutting o
US2444720A (en) Manufacture of lithium base greases
US2381377A (en) Mineral oil
US2179065A (en) Manufacture of sulphurized monoesters of fatty acids
US2118915A (en) Manufacture of wax acids
US2156919A (en) Sulphur oils
US1844400A (en) Sulphur-containing oil composition and method of making the same
US2540093A (en) Thienylthiolesters in lubricating compositions
US1929955A (en) Lubricant
US2043962A (en) Lubricants
US2178325A (en) Sulphurized cutting oil
US1904065A (en) Lubricating oil
US2147578A (en) Sulphurized lubricant
US2268232A (en) High film strength lubricant and method of preparing same
US2097468A (en) Production of hydrocarbons of high molecular weight
US2159908A (en) Method of producing stable solutions of sulphur in mineral and other oils
US2410578A (en) Mineral oil composition
US2252133A (en) Metal fabricating compocnb
US1806933A (en) Of san francisco
USRE23274E (en) Phenol esters of silicon oxychlo