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GB2199591A - Stability improver for water-in-oil emulsion - Google Patents

Stability improver for water-in-oil emulsion Download PDF

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Publication number
GB2199591A
GB2199591A GB08700413A GB8700413A GB2199591A GB 2199591 A GB2199591 A GB 2199591A GB 08700413 A GB08700413 A GB 08700413A GB 8700413 A GB8700413 A GB 8700413A GB 2199591 A GB2199591 A GB 2199591A
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GB
United Kingdom
Prior art keywords
emulsion
percent
weight
water
oil
Prior art date
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Withdrawn
Application number
GB08700413A
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GB8700413D0 (en
Inventor
Joosup Shim
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.)
Mobil Oil AS
ExxonMobil Oil Corp
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Mobil Oil AS
Mobil Oil Corp
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Application filed by Mobil Oil AS, Mobil Oil Corp filed Critical Mobil Oil AS
Priority to GB08700413A priority Critical patent/GB2199591A/en
Publication of GB8700413D0 publication Critical patent/GB8700413D0/en
Publication of GB2199591A publication Critical patent/GB2199591A/en
Withdrawn legal-status Critical Current

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    • 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
    • C10M173/00Lubricating compositions containing more than 10% water
    • 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
    • C10M135/04Hydrocarbons
    • 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
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant Compositions
    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
    • C10M2215/04Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to acyclic or cycloaliphatic 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
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant Compositions
    • C10M2215/26Amines
    • 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
    • C10M2219/00Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/02Sulfur-containing compounds obtained by sulfurisation with sulfur or sulfur-containing compounds
    • C10M2219/022Sulfur-containing compounds obtained by sulfurisation with sulfur or sulfur-containing compounds of hydrocarbons, e.g. olefines
    • 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
    • C10M2219/00Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/04Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
    • C10M2219/044Sulfonic acids, Derivatives thereof, e.g. neutral salts
    • 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
    • C10M2223/045Metal containing thio derivatives
    • 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
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/08Hydraulic fluids, e.g. brake-fluids
    • 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
    • C10N2050/01Emulsions, colloids, or micelles

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Lubricants (AREA)

Abstract

A water-in-oil emulsion, having improved thermal stability, is provided which comprises about 40 to 80 percent by weight of an oil of lubricating viscosity; about 10 to less than about 60 percent by weight water, said percentages based on the total weight of the emulsion; a water-in-oil emulsifier; and an emulsion stabilizing amount of a stabilizer selected from the group consisting of sulfurized diisobutylene, sulfurized triisobutylene and mixtures thereof.

Description

STABILITY IMPROVER FOR WATER-IN-OIL EMULSION The present invention is directed to a process for providing thermal stability to a water-in-oil emulsion which is useful in industrial applications, such as in hydraulic fluids.
More specifically, the present invention is directed to a water-in-oil emulsion containing sulfurized diisobutylene and/or triisobutylene which is useful for industrial applications as a hydraulic fluid.
The use of water-in-oil emulsion fluids as lubricants in industrial applications, for example, as hydraulic fluids, and in other applications where lubricants are necessitated is well known to those skilled in the art. An essential aspect of water-in-oil emulsion lubricants is the presence of oil as the continuous phase with water dispersed therein. The continuous oil phase of the lubricant provides the necessary lubricity. At the same time the discontinuous, dispersed water phase contributes fire-resistance.
Thus, water-in-oil emulsion lubricant fluids combine lubricating inflammability characteristics.
A major difficulty in utilizing these otherwise excellent hydraulic lubricating fluids is the possibility of loss of stability of the emulsion. In many water-in-oil emulsions of the prior art water particles tended to agglomerate in clusters and to settle to the lower part of the reservoir in which the fluid was maintained.
The result of this emulsion breakdown is a continuous oil phase which is obviously non-fire resistant. Not only does such a result eliminate a major requirement of emulsifiable lubricants, fire resistance, but, moreover, such a condition, in which free water is present, can cause corrosion of lines and working parts as well as rapid wear of pump parts due to lack of lubrication. Obviously, therefore, it is essential that the water-in-oil hydraulic fluids maintain their stability over the long period of time in which they are in service.
A major cause of breakdown of emulsifiable lubricants including hydraulic fluids is high temperature. As those skilled in the art are aware, continued exposure to elevated temperatures tends to break down water-in-oil emulsion hydraulic fluids.
The problem of maintaining stability of water-in-oil emulsion hydraulic fluids has been addressed in the prior art. For example, it is known to use a stabilizing amount of stabilizer consisting of (1) a water-soluble aminohydroxy compound, or (2) a heterocyclic amine, or (3) an alkenylsuccinic anhydride having a number average molecular weight of about 300 to 3,000, alone, or in combination with (a) a rosin salt; or (b) an amine and a rosin soap.
According to the prior art, water-in-oil emulsions are known with good high temperature stability achieved by the addition thereto of polyethylene.
The prior art also teaches the use of a calcium petroleum sulfonate as an emulsifier. For example, a calcium soap of a long chain aliphatic fatty acid is utilized, or a potassium salt of a saturated straight-chain fatty acid. According to the prior art, the calcium petroleum sulfonate is used in combination with an alkali metal hydroxide naphthenic acid. Also, an alkali metal or alkaline earth metal sulfonate as a component in a water-in-oil emulsion fire-resistant fluid is known.
Other similar teachings utilizing calcium sulfonate as the basic emulsifier suggest to combine the sulfonate emulsifier with naphthenic acid salts or soaps of several metals, with calcium being the particularly preferred metal, as the stabilizing medium, to produce fire-resistant water-in-oil emulsions.
Further, according to the prior art the utilization of a hydrogenated polyisobutylene as the lubricating oil base in a water-in-oil emulsion is known, as well as the teaching that hydrogenated polyisobutylene emulsions are more stable than polybutylene emulsions.
According to the present invention, it has now been discovered that water-in-oil emulsions are stabilized against breaking of the emulsion when exposed to elevated temperatures over long periods of time by use of additives consisting of sulfurized diisobutylene, sulfurized triisobutylene, and mixtures thereof.
In accordance with one embodiment of the present invention a water-in-oil emulsion is provided which comprises about 40 to 80 percent of an oil of lubricating viscosity; about 10 to less than 60 percent water, said percentages being by weight, based on the total weight of the water-in-oil emulsion; and an emulsion stabilizing amount of a long term thermal stabilizer which may be any one of (a) sulfurized diisobutylene, (b) sulfurized triisobutylene, and (c) mixtures of (a) and (b).
Another embodiment of the invention comprises a water-in-oil emulsion having about 40 to 80 percent of an oil of lubricating viscosity; about 10 to less than 60 percent water; a water-in-oil emulsifier present in a concentration of between about 0.5 percent and 15 percent and an emulsion stabilizing amount of a long term thermal stabilizer which may be any one of (a) sulfurized diisobutylene, (b) sulfurized triisobutylene, and (c) mixtures of (a) and (b), all of the foregoing percentages being by weight based upon the total composition of the emulsion.
In a further embodiment, the water-in-oil emulsion contains about 40 to 80 percent of an oil of lubricating viscosity; about 10 to less than 60 percent of water; a water-in-oil emulsifier present in a concentration of between about 0.5 to about 15 percent; and a long term thermal stabilizer present in a concentration of between about 0.01 and 2 percent, all of the foregoing percentages being by weight and the long term thermal stabilizer being either a sulfurized diisobutylene or a sulfurized triisobutylene or a mixture of sulfurized diisobutylene and sulfurized triisobutylene.
Further, another embodiment of the invention comprises a water-in-oil emulsion containing between about 50 and 70 percent of an oil of lubricating viscosity; water present in an amount of about 10 to 50 percent; an emulsifier in a concentration of between about 1 and 10 percent and from about 0.01 to about 2 percent of a long term thermal stabilizer which is either a sulfurized diisobutylene, or a sulfurized triisobutylene, or a mixture of sulfurized diisobutylene and sulfurized triisobutylene, all of the foregoing percentages being by weight and based upon the total weight of said emulsion.
In a further embodiment the emulsion according to the present invention may contain the long term stabilizer in a concentration of between about 0.075 and 0.5 percent by weight based on the total weight of said emulsion.
In a further embodiment of the invention, the emulsion contains an emulsifier which is a mixture of sulfonates, amines, zinc dithiophosphate and ethylene glycol.
The invention is also embodied in a process for providing thermal stability to a water-in-oil emulsion which is characterized by the presence of between about 40 to 80 percent by weight of an oil of lubricating viscosity; about 10 to less than about 60 percent by weight of water; about 0.5 to 15 percent by weight of a water-in-oil emulsifier, all said percentages based on the total weight of said emulsion and this process comprises adding an emulsion stabilizing amount of a long term thermal stabilizer which is either sulfurized diisobutylene, or sulfurized triisobutylene or a mixture of sulfurized diisobutylene and sulfurized triisobutylene.
In a preferred embodiment of the aforesaid process, the oil of lubricating viscosity is present in a concentration of between about 50 percent and 70 percent by weight based upon the total weight of said emulsion. In a further embodiment, said process is characterized by said stabilizer being present in a concentration of between about 0.01 and 2 percent by weight based on the total weight of said emulsion. In a still further embodiment, the process is characterized by the stabilizer being present in a concentration of between about 0.05 and 1 percent by weight based on the total weight of said emulsion. In still another further embodiment of the aforesaid process, the stabilizer is present in a concentration of between about 0.075 and 0.5 percent by weight based on the total weight of said emulsion.
The water-in-oil emulsion fluid of the present invention, principally utilized as a hydraulic fluid, possesses long term thermal stability. In the emulsion fluid of this invention the oil is the continuous phase, constituting about 40 to 80 percent by weight of the total composition. More preferably, the concentration of the continuous phase represents from about 50 to about 70 percent by weight. The discontinuous, dispersed phase is water, constituting from about 10 to less than 70 percent by weight of the total emulsion. More preferably, the water constitutes about 10 to less than 50 percent by weight of the total emulsion.
The continuous oil phase, which provides the lubricant effect, may comprise mineral oils, synthetic oils, especially synthetic hydrocarbon oils, or a combination of mineral oil with synthetic oils of lubricating viscosity. In the preferred embodiment wherein mineral oils are employed as the oil phase, these oils have a viscosity of at least 40 Saybolt Universal seconds (SUS) at 1000F. More preferably, a mineral oil having a viscosity in the range of between about 60 SUS and 300 SUS at 1000F. is typically employed. When synthetic lubricants are utilized, either alone or in addition to mineral oils, various compounds may be utilized for this purpose.Typical synthetic oils include polypropylene glycol, polyalpha-olefins, trimethylolpropane esters, neopentyl and pentaerythritol esters, di-(2-ethylhexyl)sebacate, di-(2-ethylhexyl)adipate, dibutylphthalate, fluorocarbons, silicate esters, silane esters of phosphorus-containing acids, liquid ureas, ferrocene derivatives, hydrogenated mineral oils, chain-type polyphenyls, siloxanes and polysiloxanes, alkyl-substituted diphenyl ethers typified by a butyl-substituted bis-(p-phenoxyphenyl)ether, phenoxy phenylethers and the like.
The synthetic hydrocarbons which may be used in the present invention are of the type normally made by polymerizing monoolefins in the presence of a suitable catalyst such as boron trifluoride or aluminum trichloride. Lower olefins may be utilized as the monoolefinic monomers provided the degree of polymerization is sufficient. For example, ethylene, propylene, butylene and the like may be utilized as the monoolefin monomer. Typically, however, the monoolefins of the present invention contain at least 10 carbon atoms. One such member is made by trimerizing decene. The synthetic hydrocarbon or polyolefin suitable for use in this invention has an upper limit of about 75 carbon atoms. Hydrocarbon fluids of this type retain their fluidity at lower temperatures and have enhanced resistance to flammability and explosion.
About 0.5 to about 15 percent by weight of the water-in-oil emulsion of this invention is an emulsifier. More preferably, the emulsifier of the present invention constitutes about 1 to 10 weight percent of the emulsion. Among the preferred emulsifiers within the contemplation of the present invention are sulfonate emulsifiers, particularly zinc alkylbenzene sulfonates and amine emulsifiers and mixtures thereof.
Tn addition to the above components the water-inoil emulsion fire-resistant hydraulic fluid of the present invention is possessed of high-temperature emulsion stability by the addition thereto of a emulsion stabilizing amount of a stabilizer selected from the group consisting of sulfurized diisobutylene, sulfurized triisobutylene and mixtures thereof.
In a preferred embodiment the emulsion stabilizing amount of the emulsion stabilizers of the present invention constitutes about 0.01 to 2 percent by weight, based on the total weight of the water-in-oil emulsion fluid. More preferably, the concentration preferred to produce emulsion stability is in the range of about 0.05 to 1 percent by weight. Still more preferably, this concentration is in the range of about 0.075 and 0.5 percent by weight. It is emphasized that all percentages by weight are based on the total weight of the emulsion.
The following examples are given to illustrate the present invention. Since these examples are given for illustrative purposes only, the scope of the present invention should not be limited thereto.
EXAMPLE 1 Water-In-Oil Emulsion Base Fluid A water-in-oil emulsion base fluid was prepared by mixing a 100 SUS paraffinic neutral oil, present in a concentration of 48.6 percent by weight with 43.0 weight percent of distilled water and an emulsifier compri#sing a mixture of sulfonates, amines, zinc dithiophosphate and ethylene glycol, present in a concentration of 8.4 weight percent, all percentages based on the total weight of the emulsion. The three components when homogenized produced a thick milky white, smooth, homogeneous water-in-oil emulsion fluid.
EXAMPLES 2-4 Preparation of Stable Water-in-Oil Emulsions In Example 2, 99.9 parts by weight of the base emulsion fluid of Example 1 were combined with 0.1 part by weight of sulfurized diisobutylene. The sulfurized diisobutylene of this example was produced in a high pressure process for producing a class of compounds which includes sulfurized diisobutylene under suproatmospheric pressure (a high pressure process) described in U.S. Patent 4,119,550.
In Example 3, 0.1 part by weight of sulfurized diisobutylene produced at low pressure was combined with 99.9 parts by weight of the base fluid. Again, U.S. Patent 4,119,550, which describes a process for making a class of compounds which includes sulfurized diisobutylene under low pressure, i.e., at atmospheric pressure, is incorporated herein by reference.
Example 4 was a duplicate of Examples 2 and 3 except that instead of sulfurized diisobutylene, 0.1 parts by weight of sulfurized triisobutylene was combined with 99.9 parts by weight of the base fluid. See U.S. Patent 4,119,550 which describes a process for making sulfurized triisobutylene.
EXAMPLES CE1 AND CE2 (COMPARATIVE EXAMPLES 1 and 2) Preparation of Water-in-Oil Emulsion Containing Non-Inventive Stabilizers Comparative Example 1 (Example CE1) was run to determine the criticality of utilizing sulfurized diisobutylene or triisobutylene rather than sulfurized monoisobutylene. In this example sulfurized monoisobutylene was combined with the base fluid in the same concentration as was the sulfurized isobutylenes of Examples 2-4. That is, 99.9 parts of the base fluid of Example 1 were combined with 0.1 part of sulfurized monoisobutylene. A method of preparing sulfurized monoisobutylene is described in U.S. Patent 4,119,550.
In Comparative Example 2 (Example CE2) an emulsion stabilizer of the prior art, the zinc sulfonate complex of succinimide, was combined with the base fluid of Example 1 in the same concentration ratio, 99.9 parts of the base fluid with 0.1 part of the succinimide. This prior art emulsion stabilizer was particularly selected because it includes sulfur.
EXAMPLE 5 Stability Testing of the Emulsions The water-in-oil emulsions of Examples 1-4 and Comparison Examples 1 and 2 were tested to determine their emulsion stability.
In this test 100 milliliters of each of the emulsions of Examples 1-4 and Comparative Examples 1 and 2 were disposed in a stoppered 100 ml graduated cylinder. The cylinders were placed in a forced air ventilated oven maintained at a temperature of 2OO0F. Every 24 hours the cylinders containing the 100 ml. samples were inspected.
When any of the emulsions demonstrated 10 percent by volume free water, that is, 10 ml of separated water or 15 percent by volume of free oil, that is, 15 ml of continuous phase oil free of water, the emulsion was judged to be no longer stable. At that point the number of days that the emulsion was maintained in the oven was recorded. The results of this test are summarized in the Table below.
TABLE EMULSION STABILITY OF WATER-IN-OIL EMULSION HYDRAULIC FLUIDS EXAMPLE NO. 1 2 3 4 CE1 CE2 Component, Parts by Wt.
W/O Emulsion Base Fluid, 100 99.9 99.9 99.9 99.9 99.9 Sulfurized Diisobutylenel 0.1 Sulfurized Diisobutylene2 0.1 Sulfurized Triisobutylene 0.1 Sulfurized Monoisobutylene 0.1 Zinc Sulfonate Complex of Succinimide 0.1 Result Emulsion Stability at 2000F., in days 21 49 58 51 20 22 Notes: 1. Manufactured at high pressure 2. Manufactured at low pressure DISCUSSION OF TEST RESULTS The results summarized in the Table establish the unexpectedly improved stability afforded by sulfurized diisobutylene, whether formulated at high or low pressure, and sulfurized triisobutylene. Whereas in the absence of any emulsion stabilizer the water-in-oil emulsion was stable for 21 days, the same emulsion provided with sulfurized diisobutylene, produced at high or low pressure retained stability under the same conditions for 49 and 58 days, respectively.Similarly, the use of sulfurized triisobutylene effected thermal stability in the same emulsion for 51 days.
On the other hand, when closely related sulfurized monoisobutylene was employed as stabilizer of this emulsion it provided no improved result over the unstabilized emulsion. The emulsion containing sulfurized monoisobutylene was stable for 20 days, 1 day less than the unstabilized emulsion.
The sulfur-containing stabilizer of the prior art, the zinc sulfonate complex of succinimide, provided the emulsion with equally unimpressive stability. This stabilizer increased the period of stability at elevated temperature by only 1 day, to 22 days, over the unstabilized emulsion.
The above described preferred embodiments and examples are given to illustrate the scope and spirit of the present invention but are not intended to limit the scope of the invention described and claimed herein.

Claims (19)

WHAT IS CLAIMED IS:
1. A water-in-oil emulsion comprising about 40 to 80 percent by weight, based on the total weight of the emulsion, of an oil of lubricating viscosity; about 10 to less than about 60 percent by weight, based on the total weight of said emulsion, of water; a water-in-oil emulsifier; and an emulsion stabilizing amount of: a long term thermal stabilizer selected from the group consisting of sulfurized diisobutylene, sulfurized triisobutylene and mixtures thereof.
2. An emulsion in accordance with Claim 1 wherein said stabilizer is sulfurized diisobutylene.
3. An emulsion in accordance with Claim 1 wherein said stabilizer is sulfurized triisobutylene.
4. An emulsion in accordance with Claim 1 wherein said stabilizer is a mixture of sulfurized diisobutylene and sulfurized triisobutylene.
5. An emulsion in accordance with any one of Claims 1 to 4 wherein said water-in-oil emulsifier is present in a concentration of between about 0.5 percent and 15 percent by weight, based on the total weight of said emulsion.
6. An emulsion in accordance with any one of Claims 1 to 5 wherein said stabilizer is present in a concentration of between about 0.01 and 2 percent by weight, based on the total weight of said emulsion.
7. An emulsion in accordance with any one of Claims 1 to 6 wherein said oil of lubricating viscosity is present in a concentration of between about 50 and 70 percent by weight; said water is present in a concentration of about 10 to 50 percent by weight; and said emulsifier is present in a concentration of between about 1 and 10 percent by weight, said percentages being based on the total weight of said emulsion.
8. An emulsion in accordance with any one of Claims 1 to 7 wherein said stabilizer is present in a concentration of between about 0.05 and 1 percent by weight, based on the total weight of said emulsion.
9. An emulsion in accordance with any one of Claims 1 to 7 wherein said stabilizer is present in a concentration of between about 0.075 and 0.5 percent by weight based on the total weight of said emulsion.
10. An emulsion in accordance with any one of Claims 1 to 9 wherein said emulsifier is a mixture of sulfonates, amines, zinc dithiophosphate and ethylene glycol.
11. A process for providing thermal stability to a water-in-oil emulsion, said emulsion characterized by the presence of between about 40 to 80 percent by weight of an oil of lubricating viscosity; about 10 to less than about 60 percent by weight water; about 0.5 to 15 percent by weight of a water-in-oil emulsifier, all said percentages based on the total weight of said emulsion, comprising adding an emulsion stabilizing amount of a long term thermal stabilizer selected from the group consisting of sulfurized diisobutylene, sulfurized triisobutylene and mixtures thereof.
12. A process in accordance with Claim 11 wherein said stabilizer is sulfurized diisobutylene.
13. A process in accordance with Claim 11 wherein said stabilizer is sulfurized triisobutylene.
14. A process in accordance with Claim 11 wherein said stabilizer is a mixture of sulfurized diisobutylene and sulfurized triisobutylene.
15. A process in accordance with any one of Claims 11 to 14 wherein said oil of lubricating viscosity is present in a concentration of between about 50 percent and 70 percent by weight; said water is present in a concentration of between about 10 and 50 percent by weight; and said emulsifier is present in a concentration of between about 1 and 10 percent by weight, all said percentages based on the total weight of said emulsion.
16. A process in accordance with any one of Claims 11 to 15 wherein said stabilizer is present in a concentration of between about 0.01 and 2 percent by weight, based on the total weight of said emulsion.
17. A process in accordance with any one of Claims 11 to 15 wherein said stabilizer is present in a concentration of between about 0.05 ano 1 percent by weight, based on the total weight of said emulsion.
18. A process in accordance with any one of Claims 11 to 15 wherein said stabilizer is present in a concentration of between about 0.075 and 0.5 percent by weight, based on the total weight of said emulsion.
19. The invention as substantially described herein.
GB08700413A 1987-01-08 1987-01-08 Stability improver for water-in-oil emulsion Withdrawn GB2199591A (en)

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GB2199591A true GB2199591A (en) 1988-07-13

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Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2024855B (en) * 1978-06-30 1982-11-03 Mobil Oil Corp Metal working lubricants

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2024855B (en) * 1978-06-30 1982-11-03 Mobil Oil Corp Metal working lubricants

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