US2455649A - Solidified oils and methods of manufacture - Google Patents

Solidified oils and methods of manufacture Download PDF

Info

Publication number
US2455649A
US2455649A US551772A US55177244A US2455649A US 2455649 A US2455649 A US 2455649A US 551772 A US551772 A US 551772A US 55177244 A US55177244 A US 55177244A US 2455649 A US2455649 A US 2455649A
Authority
US
United States
Prior art keywords
oil
oils
fatty
soap
acids
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
US551772A
Inventor
Beerbower Alan
Jr Harold A Ricards
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 Development Co
Original Assignee
Standard Oil Development 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 Development Co filed Critical Standard Oil Development Co
Priority to US551772A priority Critical patent/US2455649A/en
Application granted granted Critical
Publication of US2455649A publication Critical patent/US2455649A/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
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L7/00Fuels produced by solidifying fluid fuels
    • C10L7/02Fuels produced by solidifying fluid fuels liquid fuels
    • 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
    • C10M5/00Solid or semi-solid compositions containing as the essential lubricating ingredient mineral lubricating oils or fatty oils and their use
    • 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
    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/02Water
    • 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
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • 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
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • C10M2203/102Aliphatic fractions
    • 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
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • C10M2203/104Aromatic fractions
    • 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
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • C10M2203/106Naphthenic fractions
    • 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
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • C10M2203/108Residual fractions, e.g. bright stocks
    • 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
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/02Hydroxy compounds
    • C10M2207/021Hydroxy compounds having hydroxy groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/022Hydroxy compounds having hydroxy groups bound to acyclic or cycloaliphatic carbon atoms containing at least two hydroxy groups
    • 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
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/125Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of eight up to twenty-nine carbon atoms, i.e. fatty acids
    • 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
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/129Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of thirty or more carbon atoms
    • 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
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/20Rosin acids
    • 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
    • C10N2050/00Form in which the lubricant is applied to the material being lubricated
    • C10N2050/10Semi-solids; greasy

Definitions

  • the present invention V relates to improvements in solidified oils which may be used for fuels or lubricants and more specifically to a stabilized solidified fuel and to an improved process for producing the same.
  • Thickened oils have been used for many years both as fuels and lubricants.
  • the oils used are generally high boiling petroleum lubricating oils; These oils range from the lighter spindle oils to the heavier residuals such as cylinder stocks.
  • lighter, more readily vaporizable hydro carbons are used such as gasoline, naphthas, kerosene or even gas oils.
  • the thickening or solidification is brought about through the oils of a thickening agent which is usually a soap, that is an alkaline soap such as a soda soap.
  • the thickened lubricating oils are known as greases and in many cases are reasonably stable, but they are often unstable which by the dispersion u chime. (01. 252-42) imperfection is exhibited by a tendency to bleed oil and in bad cases actual separation of the soap from the oil occurs. This instability is more marked in the fuel compositions because of the use of less viscous oils in these compositions.
  • the preferred soap producing organic materials are the more saturated fatty acids, such as stearic, palmitic acids, etc., in mixture with rosin or abietic acid.
  • the fatty acid is present in the larger proportion.
  • the acids of saturated oils such as fully hydrogenated oils can be employed as well.
  • To this acid mixture is added an equal amount of petroleum oil, which serves as a flux or solvent, and from one-third to twothirds, based on the weight of the fatty acid, of a selected fatty oil is then added. The nature of this selected fatty oil will be described more fully below.
  • the mixture is melted together (this can be done even at room temperature, for example from 60 to 110 F., without difliculty) and it is then mixed with a substantial portion of the oil to be solidified.
  • the entire amount of oil can be added at this point or, if desired, a smaller amount say one-fifth to one-third of the oil can be added, the remainder being added slowly from 2 time to time later. may be 30 to 110 F.
  • Saponification starts almost immediately and the main reaction primarily between the free acid and the soda is over in 10 to 30 minutes and the mixture gradually solidifies. Secondary reactions appear to occur for several hours or even days depending on the temperature of the operation and it is believed that the fatty oil addedis 'then slowly saponified. In any case, the material gradually hardens into a stable grease or paste which is smooth without any marked fibrous structure and is extremely stable on standing. It shows no bleeding even when the oil used is a light naphtha in which case the tendency toward bleeding and fuel separation is at its worst.
  • the selected fatty oil referred to generally above is an important ingredient in the above composition since its function is to stabilize the mixture.
  • the fatty oils should contain a major amount of saturated fatty acids or unsaturated fatty acids which contain hydroxyl groups, and with only minor amounts of simple unsaturated acids such as oleic.
  • fatty oils containing saturated fatty acids such as stearic, palmitic or the fully hydrogenated acids are preferred but hydroxy acids such as ricinoleic appear to be about equally good.
  • Oleic acid should be avoided and therefore most of the edible fats are not desirable for this purpose.
  • castor oil is extremely good because it contains only small amounts of oleic acid compounds and large amounts of ricinoleic. Similarly, hard tallows in which the oleic acid content is small can be used. Fats which have been hydrogenated to reduce the oleic acid content; may also be employed. These various materials are used in about one-third to' twothirds of the free acids which were added to make up the main quantity of the soap.
  • the petroleum oil makes up the balance of the composition and consists of from to 93% by weight of the entire mixture.
  • the amount of water is ordinarily from 1 to 4% in the mixture and the remainder is made up of the soap and
  • the temperature of the oil say 40 or 50% strength and the mix- 3 the free glycerin The greater the proportion of soap in the mixture, the harder the grease will be.
  • Example 1 As an example of the present composition and its method of manufacture, the following materials were mixed at room temperature:
  • the above mentioned product has a variety of uses. When made up with gasoline, it is a good canned fuel, which can be ignited with a match and burns with a steady flame so that it may be used to heat various cooking utensils and for other purposes. It may be used also as -a fuel in cigarette lighters and for similar deyices where small flames are employed. As a grease it is extremely stable and useful for rough work chiefly where moisture is not encountered.
  • a stabilized, solidified mineral oil consisting essentially of a mineral oil gelled by a soap formed in situ from free saturated fatty acids, and stabilized by the saponification in situ of a fatty oil rich in esters selected from the group consisting of esters of saturated fatty acids and esters of hydroxylated unsaturated acids, said. fatty oil being added to the initial mixture in the proportion of A; to of the said free saturated fatty acids.
  • a stabilized, solidified mineral oil consisting essentially of a mineral oil gelled by a soap formed in situ from free saturated fatty acids and stabilized by the saponification in situ of a fatty oil rich in esters selected from the group consisting of esters of saturated fatty acids and esters of hydroxylated unsaturated acids, said fatty oil being added to the initial mixture in the proportion of A to of the said free saturated acids, and a small quantity of rosin.
  • a process for producing stable gelled oils which consists essentially of preparing a solution of a mineral oil, free saturated fatty acids and a fatty oil rich in the esters selected from the group consisting of esters of saturated fatty acids, and esters of hydroxylated unsaturated acids, said fatty oil being in the proportion of to of the said free saturated fatty acid, adding caustic soda to said solution maintained at room temperature, thereby forming a soap with the said fatty acids, and slowly saponifying the said fatty oil.

Description

Patented Dec. 7, 1948 SOLIDIF'IED OILS AND METHODS OF MANUFACTURE Alan Beerbower, Westfleld, and Harold A. Ricards, J13, Granford, N. .L, assignorsto Standard Oil Development Company, a corporation of Dela- .ware
' No Drawing. Application August 29, 1944,
Serial No. 551,772-
The present invention V relates to improvements in solidified oils which may be used for fuels or lubricants and more specifically to a stabilized solidified fuel and to an improved process for producing the same.
Thickened oils have been used for many years both as fuels and lubricants. For lubricating purposes the oils used are generally high boiling petroleum lubricating oils; These oils range from the lighter spindle oils to the heavier residuals such as cylinder stocks. For the manufacture of fuels, lighter, more readily vaporizable hydro carbons are used such as gasoline, naphthas, kerosene or even gas oils. The thickening or solidification is brought about through the oils of a thickening agent which is usually a soap, that is an alkaline soap such as a soda soap. The thickened lubricating oils are known as greases and in many cases are reasonably stable, but they are often unstable which by the dispersion u chime. (01. 252-42) imperfection is exhibited by a tendency to bleed oil and in bad cases actual separation of the soap from the oil occurs. This instability is more marked in the fuel compositions because of the use of less viscous oils in these compositions.
It is desired therefore to stabilize these compositions and it has been found that this can be done by incorporating in the grease a small amount of certain selected fatty oils. The action of these materials is not fully understood but it is believed that the fatty oil is saponified during the manufacture at least to some extent, but in any case the particular type and the amount of the fatty oil is highly critical.
In the manufacture of stabilized solidified oils, the preferred soap producing organic materials are the more saturated fatty acids, such as stearic, palmitic acids, etc., in mixture with rosin or abietic acid. The fatty acid is present in the larger proportion. The acids of saturated oils such as fully hydrogenated oils can be employed as well. To this acid mixture is added an equal amount of petroleum oil, which serves as a flux or solvent, and from one-third to twothirds, based on the weight of the fatty acid, of a selected fatty oil is then added. The nature of this selected fatty oil will be described more fully below. The mixture is melted together (this can be done even at room temperature, for example from 60 to 110 F., without difliculty) and it is then mixed with a substantial portion of the oil to be solidified. The entire amount of oil can be added at this point or, if desired, a smaller amount say one-fifth to one-third of the oil can be added, the remainder being added slowly from 2 time to time later. may be 30 to 110 F.
When the mass is thoroughly mixed, a sufflcient quantity of sodium hydroxide is then added for complete saponification of the fatty acids and also of the fatty oil which has been added. The soda is generally used in an aqueous solution of ture' is stirred together so that the soap is formed in the presence of the oil, that is to say in situ."
Saponification starts almost immediately and the main reaction primarily between the free acid and the soda is over in 10 to 30 minutes and the mixture gradually solidifies. Secondary reactions appear to occur for several hours or even days depending on the temperature of the operation and it is believed that the fatty oil addedis 'then slowly saponified. In any case, the material gradually hardens into a stable grease or paste which is smooth without any marked fibrous structure and is extremely stable on standing. It shows no bleeding even when the oil used is a light naphtha in which case the tendency toward bleeding and fuel separation is at its worst.
The selected fatty oil referred to generally above is an important ingredient in the above composition since its function is to stabilize the mixture. In general, it has been found that the fatty oils should contain a major amount of saturated fatty acids or unsaturated fatty acids which contain hydroxyl groups, and with only minor amounts of simple unsaturated acids such as oleic. In other words, fatty oils containing saturated fatty acids such as stearic, palmitic or the fully hydrogenated acids are preferred but hydroxy acids such as ricinoleic appear to be about equally good. Oleic acid, however, should be avoided and therefore most of the edible fats are not desirable for this purpose. Of the commercial raw materials, castor oil is extremely good because it contains only small amounts of oleic acid compounds and large amounts of ricinoleic. Similarly, hard tallows in which the oleic acid content is small can be used. Fats which have been hydrogenated to reduce the oleic acid content; may also be employed. These various materials are used in about one-third to' twothirds of the free acids which were added to make up the main quantity of the soap.
The petroleum oil makes up the balance of the composition and consists of from to 93% by weight of the entire mixture. The amount of water is ordinarily from 1 to 4% in the mixture and the remainder is made up of the soap and The temperature of the oil say 40 or 50% strength and the mix- 3 the free glycerin The greater the proportion of soap in the mixture, the harder the grease will be.
Example As an example of the present composition and its method of manufacture, the following materials were mixed at room temperature:
Parts by weight This mixture was gently heated to about 90 F. and melted together. About 85 parts of gasoline were then added. Saponification was accomplished at room temperature with the aid of two parts by weight of 40 to 50% 'caustic soda, and two parts of water were also added. The mixture was stirred at room temperature and set in about ten minutes but hardening appeared to continue fora period of some 48 hours while the material was left standing. The product was found to be a firm solid gel. It was easily softened by agitation but when left standing, the gel gradually reformed and hardened in the same manner in which the original hardening occurred. It wasextremely stable against bleeding and separation of the soap, and when ignited, it burned readily.
If the fatty oil is omitted from the above mentioned composition, the product is found to form quite well but subsequently separates almost completely.
The above mentioned product has a variety of uses. When made up with gasoline, it is a good canned fuel, which can be ignited with a match and burns with a steady flame so that it may be used to heat various cooking utensils and for other purposes. It may be used also as -a fuel in cigarette lighters and for similar deyices where small flames are employed. As a grease it is extremely stable and useful for rough work chiefly where moisture is not encountered.
We claim:
1. A stabilized, solidified mineral oil consisting essentially of a mineral oil gelled by a soap formed in situ from free saturated fatty acids, and stabilized by the saponification in situ of a fatty oil rich in esters selected from the group consisting of esters of saturated fatty acids and esters of hydroxylated unsaturated acids, said. fatty oil being added to the initial mixture in the proportion of A; to of the said free saturated fatty acids.
2. A stabilized, solidified mineral oil as in claim 1, wherein the said fatty oil consists principally of castor oil.
3. A stablized, solidified mineral oil as in claim 1, wherein the said mineral oil comprises 75 to 93% of the composition, the remainder being soap of the free fatty acids, the saponified fatty oil, glycerol and a minor proportion of water.
4. A stabilized, solidified mineral oil as in claim 1, wherein the said mineral oil consists principally of volatile hydrocarbons.
5. A stabilized, solidified mineral oil as in claim 1, wherein the said mineral oil consists primarily of kerosene.
6. A stablized, solidified mineral oil as in claim 1, wherein the said mineral oil consists primarily of gasoline.
7. A stabilized, solidified mineral oil consisting essentially of a mineral oil gelled by a soap formed in situ from free saturated fatty acids and stabilized by the saponification in situ of a fatty oil rich in esters selected from the group consisting of esters of saturated fatty acids and esters of hydroxylated unsaturated acids, said fatty oil being added to the initial mixture in the proportion of A to of the said free saturated acids, and a small quantity of rosin.
8. A stabilized, solidified mineral oil as in claim 1, wherein the said soap is a sodium soap.
9. A process for producing stable gelled oils which consists essentially of preparing a solution of a mineral oil, free saturated fatty acids and a fatty oil rich in the esters selected from the group consisting of esters of saturated fatty acids, and esters of hydroxylated unsaturated acids, said fatty oil being in the proportion of to of the said free saturated fatty acid, adding caustic soda to said solution maintained at room temperature, thereby forming a soap with the said fatty acids, and slowly saponifying the said fatty oil.
10. A process for producing stable gelled oils as in claim 9 wherein the said mineral oil conin the naphtha to kerosene range.
11. A process for producing stable gelled oils as in claim 9, wherein the said mineral oil is a normally liquid hydrocarbon boiling in the naphtha to kerosene range and comprises to 93% of the said solution, and the said fatty oil consists primarily of castor oil.
ALAN BEERBOWER. HAROLD A. RICARDS, JR.
REFERENCES CITED The following references are of record in the file of thispatent:
UNITED STATES PATENTS Number Name Date 1,266,080 Strobl May 14, 1918 1,484,190 Ray Feb. 19, 1924 1,863,962 Bierlich June 21, 1932 1,989,196 Hilliker Jan. 29, 1935 2,038,688 Taylor Apr. 28, 1936 2,049,072 Mikeska July 28, 1936 2,334,239 Barnett Nov. 16, 1943 2,380,960 Fraser Aug. 7, 1945
US551772A 1944-08-29 1944-08-29 Solidified oils and methods of manufacture Expired - Lifetime US2455649A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US551772A US2455649A (en) 1944-08-29 1944-08-29 Solidified oils and methods of manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US551772A US2455649A (en) 1944-08-29 1944-08-29 Solidified oils and methods of manufacture

Publications (1)

Publication Number Publication Date
US2455649A true US2455649A (en) 1948-12-07

Family

ID=24202621

Family Applications (1)

Application Number Title Priority Date Filing Date
US551772A Expired - Lifetime US2455649A (en) 1944-08-29 1944-08-29 Solidified oils and methods of manufacture

Country Status (1)

Country Link
US (1) US2455649A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2850454A (en) * 1952-12-01 1958-09-02 Exxon Research Engineering Co Production of greases by alkali fusion of materials containing hydroxy fatty acid and glycerine radicals
US10214225B2 (en) * 2013-01-07 2019-02-26 Whitmore Manufacturing, Llc Thixotropic gel or liquid for friction control and method of using the same

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1266080A (en) * 1915-02-11 1918-05-14 Sternau & Company Inc S Solid alcohol and process of producing same.
US1484190A (en) * 1921-11-08 1924-02-19 Arthur B Ray Solidification of organic liquids
US1863962A (en) * 1930-11-13 1932-06-21 J H Bierlich Solidified alcoholic fuel
US1989196A (en) * 1930-10-06 1935-01-29 Standard Oil Co Journal grease
US2038688A (en) * 1933-07-10 1936-04-28 Mccoll Frontenac Oil Co Ltd Solid lubricant
US2049072A (en) * 1933-08-29 1936-07-28 Standard Oil Dev Co Lubricants
US2334239A (en) * 1941-12-30 1943-11-16 Texas Co Stabilizfd grease composition
US2380960A (en) * 1940-01-09 1945-08-07 Internat Lubricant Corp Production of lubricants

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1266080A (en) * 1915-02-11 1918-05-14 Sternau & Company Inc S Solid alcohol and process of producing same.
US1484190A (en) * 1921-11-08 1924-02-19 Arthur B Ray Solidification of organic liquids
US1989196A (en) * 1930-10-06 1935-01-29 Standard Oil Co Journal grease
US1863962A (en) * 1930-11-13 1932-06-21 J H Bierlich Solidified alcoholic fuel
US2038688A (en) * 1933-07-10 1936-04-28 Mccoll Frontenac Oil Co Ltd Solid lubricant
US2049072A (en) * 1933-08-29 1936-07-28 Standard Oil Dev Co Lubricants
US2380960A (en) * 1940-01-09 1945-08-07 Internat Lubricant Corp Production of lubricants
US2334239A (en) * 1941-12-30 1943-11-16 Texas Co Stabilizfd grease composition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2850454A (en) * 1952-12-01 1958-09-02 Exxon Research Engineering Co Production of greases by alkali fusion of materials containing hydroxy fatty acid and glycerine radicals
US10214225B2 (en) * 2013-01-07 2019-02-26 Whitmore Manufacturing, Llc Thixotropic gel or liquid for friction control and method of using the same

Similar Documents

Publication Publication Date Title
US2735814A (en) Die forging compound
GB603967A (en) An improved lubricating grease composition
US3095375A (en) Extreme pressure lubricants containing highly oxidized waxes
GB399527A (en) A process for improving oils, especially lubricating oils
US2455649A (en) Solidified oils and methods of manufacture
GB601346A (en) Improvements in or relating to lithium base lubricating grease compositions and method of preparing the same
US2413121A (en) Greases
US2360631A (en) Lubricant
GB560885A (en) Improvements in or relating to lubricating greases
US2198567A (en) Driving journal lubricant
US2142998A (en) Extreme pressure lubricants and method of preparing same
US2444720A (en) Manufacture of lithium base greases
US2503749A (en) Barium soap grease compositions and method of preparation
US2303558A (en) Premium cup grease of improved heat and texture stability
USRE22299E (en) Lubricating composition
US2801220A (en) Production of lubricating greases from monohydric alcohol esters of hydroxy fatty acids
US2576031A (en) Lubricating grease containing soaps of tall oil
US2229368A (en) Grease and the method of preparing the same
US2343737A (en) Lubricant
US1970902A (en) Lubricant
US2043961A (en) Lubricants
US2580570A (en) Smooth-textured lithium-base greases
US2420274A (en) Heavy-duty motor oil composition
US1982198A (en) Lubricant
US2854409A (en) Method for a calcium soap grease containing a hydrocarbon wax