US2629721A - Sulfurized fatty and waxy materials - Google Patents

Sulfurized fatty and waxy materials Download PDF

Info

Publication number
US2629721A
US2629721A US85253A US8525349A US2629721A US 2629721 A US2629721 A US 2629721A US 85253 A US85253 A US 85253A US 8525349 A US8525349 A US 8525349A US 2629721 A US2629721 A US 2629721A
Authority
US
United States
Prior art keywords
parts
sulfurized
temperature
water
weight
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
US85253A
Inventor
Conrad J Sunde
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.)
N I Malmstrom & Co
Original Assignee
N I Malmstrom & 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 N I Malmstrom & Co filed Critical N I Malmstrom & Co
Priority to US85253A priority Critical patent/US2629721A/en
Application granted granted Critical
Publication of US2629721A publication Critical patent/US2629721A/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
    • C10M159/00Lubricating compositions characterised by the additive being of unknown or incompletely defined constitution
    • C10M159/12Reaction products
    • C10M159/123Reaction products obtained by phosphorus or phosphorus-containing compounds, e.g. P x S x with organic compounds
    • 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
    • C10M2223/00Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/02Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
    • C10M2223/04Phosphate esters
    • C10M2223/047Thioderivatives not containing metallic elements
    • 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
    • C10M2223/00Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/12Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions obtained by phosphorisation of organic compounds, e.g. with PxSy, PxSyHal or PxOy
    • 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
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/02Groups 1 or 11
    • 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
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/04Groups 2 or 12
    • 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
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/08Groups 4 or 14
    • 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
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/14Group 7
    • 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
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/16Groups 8, 9, or 10

Definitions

  • Another object is to provide a novel sulfurized wool grease or degras which may be most effectively utilized as an additive for mineral oils so that they, may be used in high pressure lubricants and also generally in motor oils and other lubricating combinations.
  • a heavy metal salt may be added in the form of a water soluble salt and a sulfurized, metallized wool grease may thus be produced.
  • This wool grease or degras is then heated to a temperature of about 270 to 280 F. in the presence of about 10% caustic soda for a period of about one hour in the presence of a minimum amount of water.
  • 100 parts by weight of wool grease may be first heated to a temperature of 210 F. Then 10 parts by weight of caustic soda are added 2 in three portions, over a period of fifteen minutes with stirring, the caustic soda being dissolved in a minimum quantity of Water. The temperature during this operation is gradually raised about 1 1 per minute to a final temperature of 275 F. At about the end of one hour the major portion of the water is driven off.
  • the hot reaction mixture will consist of the sodium salts of the wool grease acids, unsaponifiable matter, some unchanged esters, and a small amount of water.
  • the hot reaction mixture may be dried in at about C. or more rapidly under vacuum. If desired, however, the product may be dried by first adding it to a lubricating oil and blowing with air at an elevated temperature.
  • the product may be placed in about '75 parts by weight of mineral oil and the temperature raised gradually up to 275' to 300 F.
  • the temperature is raised, air is blown through until substantially all the moisture has been removed.
  • the temperature is then regulated to about 285 F.
  • a slurry is prepared of about 23 parts by Weight of phosphorus Dentasulfide in 25 parts of mineral oil. About 12 parts of the slurry are added with stirring to the mixture, While the mixture is held at a temperature of 250 F. to 350 F., but preferably at 285 to 300 F.
  • the remainder of the slurry may be added, about 12 to 13 parts by weight at a time, at intervals of five minutes, and the temperature is maintained at 285 to 300 F. for about one hour, during which the foaming will subside.
  • reaction mixture After heating for about one hour, the reaction mixture is cooled and filtered to give a relatively high yield of sulfurized degras of about 215 parts by weight as compared with the original amounts of wool grease utilized, which was about 100 parts by weight.
  • heavy metal salts such as lead
  • this may be done by combining about 100 parts by weight of sulfurized alkali treated wool grease with about 24 parts of lead acetate. Specifically, 100 parts by weight of sulfurized alkali treated wool grease or degras" are heated to approximately 200 F. A solution of 24 parts by weight of lead acetate in' about 24 grams of water is added to the mixture, heated to about 200 to 210 F. for 45 minutes.
  • the acetic acid may be removed in a number of ways.
  • the product may be 3 cooled and excess water added, followed by heating in a steam bath and stirring. After cooling, the wash water may be decanted and after three or four washings, the product may be dried at 212 F.
  • the residual acetic acid and water may also be removed by raising the temperature of the product to 210 to 220 F. followed by blowing with air for 45 minutes.
  • the blowing-air process is preferred as a method of removing water and acetic acid.
  • the final composition will be a most desirable additive to motor oils and to high pressure lubricants, such as those used on gears.
  • a process of making leaded sulfurized saponified degras which comprises heating wool grease to about 270 to 280 F. in the presence of about 10% caustic soda for about one hour, and the caustic soda being in a concentrated solution in a minimum amount of water, drying the hot reaction mixture by adding it to a lubricant oil and blowing with hot air at a temperature of about 285 F., about 100 to 125 parts of the reaction mixture being placed in about 75 parts of the mineral oil, then mixing with a slurry of about 23 parts of phosphorous pentasulfide and 25 parts of mineral oil and maintaining with stirring a temperature of 235 to 300 F. and then treating the thus sulfurized saponified wool grease with a solution of lead acetate at a tem-- perature of about 200 to 212 F. and finally removing the acetic acid CONRAD J. SUNDE.

Description

Patented Feb. 24, 1953 SULFURIZED FATTY AND WAXY MATERIALS Conrad J. Sunde, Garden City, N. Y., assignor to N. I. Malmstrom & Company, Brooklyn, N. Y.,
a copartnership No Drawing. Application April 2, 1949, Serial No. 85,253
1 Claim. 1
yields of highly sulfurized products with less conversion to undesirable lay-products.
Another object is to provide a novel sulfurized wool grease or degras which may be most effectively utilized as an additive for mineral oils so that they, may be used in high pressure lubricants and also generally in motor oils and other lubricating combinations.
Still further objects and advantages will appear in the more detailed description set forth below, it being understood, however, that this more detailed description is given by way of illustration and explanation only and not by way of limitation, since various changes therein may be made by those skilled in the art without departing from the scope and spirit of the present invention.
According to the present invention, it has been found most satisfactory first to heat the lanolin, wool grease or degras in the presence of a strong alkali partially or completely to saponify the same. This partially or completely saponifled material is then mixed with a mineral oil with or without previous drying and after removal of the water, is treated with a sulfurizing agent, a phosphorus sulfide being preferred.
If desired, as a last step, a heavy metal salt may be added in the form of a water soluble salt and a sulfurized, metallized wool grease may thus be produced.
To give a specific example of the above procedure:
Example I A wool grease or degras is selected, containing up to 15% free fatty acids, 5 to free fatty alcohols and '75 to 95% fatty acid esters.
This wool grease or degras is then heated to a temperature of about 270 to 280 F. in the presence of about 10% caustic soda for a period of about one hour in the presence of a minimum amount of water.
Generally, 100 parts by weight of wool grease may be first heated to a temperature of 210 F. Then 10 parts by weight of caustic soda are added 2 in three portions, over a period of fifteen minutes with stirring, the caustic soda being dissolved in a minimum quantity of Water. The temperature during this operation is gradually raised about 1 1 per minute to a final temperature of 275 F. At about the end of one hour the major portion of the water is driven off.
The hot reaction mixture will consist of the sodium salts of the wool grease acids, unsaponifiable matter, some unchanged esters, and a small amount of water.
The hot reaction mixture may be dried in at about C. or more rapidly under vacuum. If desired, however, the product may be dried by first adding it to a lubricating oil and blowing with air at an elevated temperature.
For example, between 100 and parts by weight of the product may be placed in about '75 parts by weight of mineral oil and the temperature raised gradually up to 275' to 300 F.
As the temperature is raised, air is blown through until substantially all the moisture has been removed. The temperature is then regulated to about 285 F.
Then a slurry is prepared of about 23 parts by Weight of phosphorus Dentasulfide in 25 parts of mineral oil. About 12 parts of the slurry are added with stirring to the mixture, While the mixture is held at a temperature of 250 F. to 350 F., but preferably at 285 to 300 F.
Some foaming will result which will increase as additional amounts of the slurry and phosphorus pentasulfide are added.
The remainder of the slurry may be added, about 12 to 13 parts by weight at a time, at intervals of five minutes, and the temperature is maintained at 285 to 300 F. for about one hour, during which the foaming will subside.
After heating for about one hour, the reaction mixture is cooled and filtered to give a relatively high yield of sulfurized degras of about 215 parts by weight as compared with the original amounts of wool grease utilized, which was about 100 parts by weight.
It is often desirable to add heavy metal salts, such as lead, and this may be done by combining about 100 parts by weight of sulfurized alkali treated wool grease with about 24 parts of lead acetate. Specifically, 100 parts by weight of sulfurized alkali treated wool grease or degras" are heated to approximately 200 F. A solution of 24 parts by weight of lead acetate in' about 24 grams of water is added to the mixture, heated to about 200 to 210 F. for 45 minutes.
The acetic acid may be removed in a number of ways. For example, the product may be 3 cooled and excess water added, followed by heating in a steam bath and stirring. After cooling, the wash water may be decanted and after three or four washings, the product may be dried at 212 F.
The residual acetic acid and water may also be removed by raising the temperature of the product to 210 to 220 F. followed by blowing with air for 45 minutes. Generally, the blowing-air process is preferred as a method of removing water and acetic acid.
The final composition will be a most desirable additive to motor oils and to high pressure lubricants, such as those used on gears.
In lieu of or in addition to lead salts, it is also possible to utilize compounds of the following metals and particularly their water-soluble salts for metallizing purposes, these metals being:
Mercury Tin Iron Silver Copper Nickel Lead Cadmium Carnauba wax Waste grease Japan wax Cottonseed oil Sperm oil Peanut oil Coconut oil Whale oil Lard oil Spermaceti Tallow Soya bean oil In combination with the sulfurized degras, it is also possible to utilize various alkyl and aryl thiophosphates or thiophosphites. Instead of phosphorous pentasulfide in addition thereto it 4. is also possible to use phosphorous sesquisulfide.
The embodiment of the invention shown and described herein is to be considered merely as illustrative, as the invention is susceptible to variations, modification and change within the spirit and scope of the appended claim.
Having now particularly described and ascertained the nature of the invention, and in what manner the same is to be performed, what is claimed is:
A process of making leaded sulfurized saponified degras which comprises heating wool grease to about 270 to 280 F. in the presence of about 10% caustic soda for about one hour, and the caustic soda being in a concentrated solution in a minimum amount of water, drying the hot reaction mixture by adding it to a lubricant oil and blowing with hot air at a temperature of about 285 F., about 100 to 125 parts of the reaction mixture being placed in about 75 parts of the mineral oil, then mixing with a slurry of about 23 parts of phosphorous pentasulfide and 25 parts of mineral oil and maintaining with stirring a temperature of 235 to 300 F. and then treating the thus sulfurized saponified wool grease with a solution of lead acetate at a tem-- perature of about 200 to 212 F. and finally removing the acetic acid CONRAD J. SUNDE.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 2,420,274 Williams et a1. May 6, 1947 2,439,821 Musselman Apr. 20, 1948
US85253A 1949-04-02 1949-04-02 Sulfurized fatty and waxy materials Expired - Lifetime US2629721A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US85253A US2629721A (en) 1949-04-02 1949-04-02 Sulfurized fatty and waxy materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US85253A US2629721A (en) 1949-04-02 1949-04-02 Sulfurized fatty and waxy materials

Publications (1)

Publication Number Publication Date
US2629721A true US2629721A (en) 1953-02-24

Family

ID=22190417

Family Applications (1)

Application Number Title Priority Date Filing Date
US85253A Expired - Lifetime US2629721A (en) 1949-04-02 1949-04-02 Sulfurized fatty and waxy materials

Country Status (1)

Country Link
US (1) US2629721A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2929778A (en) * 1956-09-13 1960-03-22 Pure Oil Co Corrosion resistant sulfurized-phosphorized extreme pressure lubricant
US3014862A (en) * 1957-09-23 1961-12-26 Gulf Oil Corp Drilling mud of enhanced lubricating properties
DE2243981A1 (en) * 1971-09-08 1973-03-15 Lubrizol Corp SULFUR-CONTAINING LUBRICANT ADDITIVES, PROCESS FOR THEIR MANUFACTURING AND THEIR USE IN LUBRICANTS

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2420274A (en) * 1944-03-25 1947-05-06 Pure Oil Co Heavy-duty motor oil composition
US2439821A (en) * 1942-08-19 1948-04-20 Standard Oil Co Lubricant preparation

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2439821A (en) * 1942-08-19 1948-04-20 Standard Oil Co Lubricant preparation
US2420274A (en) * 1944-03-25 1947-05-06 Pure Oil Co Heavy-duty motor oil composition

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2929778A (en) * 1956-09-13 1960-03-22 Pure Oil Co Corrosion resistant sulfurized-phosphorized extreme pressure lubricant
US3014862A (en) * 1957-09-23 1961-12-26 Gulf Oil Corp Drilling mud of enhanced lubricating properties
DE2243981A1 (en) * 1971-09-08 1973-03-15 Lubrizol Corp SULFUR-CONTAINING LUBRICANT ADDITIVES, PROCESS FOR THEIR MANUFACTURING AND THEIR USE IN LUBRICANTS

Similar Documents

Publication Publication Date Title
US2234379A (en) Preservation of soap
US2173448A (en) Preparation of alkylolamine derivatives
US2303256A (en) Grease and process of making same
US2629721A (en) Sulfurized fatty and waxy materials
US2483571A (en) Reaction of organic substances with phosphorous sesquisulfide
US2488515A (en) Utilization of waste wax paper
GB631851A (en) Lubricants and extreme pressure additives therefor
US2375061A (en) Stabilized lubricant and the method of preparing the lubricant additive for this lubricanat
US2443823A (en) Sulfurized terpenes
US2267148A (en) Method of making aluminum soaps
US2563856A (en) Defoaming agent for pulp and paper stock
US2422630A (en) Preparation of lubricants
US1989196A (en) Journal grease
US2188863A (en) Grease and method of making the same
US2507184A (en) Alkali-refining of fatty glycerides in the presence of an inorganic phosphate compound
US2349224A (en) Lubricating composition
US2179062A (en) Manufacture of sulpho-halogenated mono-esters and improved lubricants containing same
US2268232A (en) High film strength lubricant and method of preparing same
US2360905A (en) Manufacture of sulpho-halogenated aliphatic monoesters
US2710836A (en) Sulfurizing and leading unsaponifiable portions of degras
US2198562A (en) Method of making sulphurized
US2399243A (en) Composition of matter suitable for use as a lubricant and lubricant comprising the same
US2116472A (en) Process of reacting nitriles with phosphorus pentasulphide
US2659695A (en) Lubricating greases
US2442828A (en) Lubricating greases