Haze free oil additive compositions containing polymeric viscosity index improver and process for producing said compositions
AssigneeExxon Research & Engineering Co.
InventorsJohn Brooke Gardiner, Max W. Hill, Jack Ryer
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Abstract
Oil compositions comprising a lubricating oil and an oil-soluble hydrocarbon polymeric viscosity index improver such as ethylene-propylene copolymers are substantially haze-free when said composition contains an anti-hazing amount of an oil-soluble strong acid containing a hydrogen dissociating moiety which has a pK of less than about 2.5, e.g. a C.sub.25 to C.sub.70 hydrocarbyl substituted sulfonic acid. The invention also relates to the process for preparing said compositions.
Claims7
A process of decreasing haze in a composition comprising:
- a major amount of hydrocarbon lubricating oil;
- in the range of about 5 to 30 wt. %, based upon the total weight of said composition, of an oil-soluble viscosity index improver polymer which consists essentially of about 30 to 80 wt. % ethylene and propylene, said polymer being formed by a Ziegler-Natta polymerization, said polymer having a M.sub.n in the range from 700 to 500,000 and a M.sub.w /M.sub.n ratio of less than 10;
- and
- a haze forming amount, but less than 1 wt. %, based on the total weight of said composition, of an oil insoluble, haze forming material resulting from the manufacture of said polymer, which material is a disassociable metal salt of a weak organic acid having a pK of more than about 3.8, and wherein said metal is selected from the class consisting of alkaline earth metal, zinc, sodium, potassium, aluminum, vanadium, chromium, iron, manganese, cobalt, nickel, cadmium, lead, bismuth and antimony;
- which process comprises adding to said composition about 0.1 to about 2.5 equivalents, per equivalent of metal of said haze forming material, of an oil soluble hydrocarbyl substituted strong acid containing a hydrogen disassociating moiety and having a pK of less than about 2.5, and reacting for about 0.1 to about 20 hours at room temperature to about 250.degree. C. said strong acid with said haze forming material to thereby decrease haze by converting said haze forming material either to an oil soluble weak acid or a volatile product, while converting the metal into an oil soluble strong acid metal salt and/or ionic complex of said strong acid, wherein said strong acid is selected from the group consisting of maleic acid, malonic acid, phosphoric acid, thiophosphoric acids, phosphonic acid, thiophosphonic acids, phosphinic acid, thiophosphinic acids, sulfonic acid, sulfuric acid, and alpha-substituted halo- or nitro- or nitrilo-carboxylic acids;
- and wherein the oil solubilizing hydrocarbyl group or groups of said strong acid contain from about 6 to about 40 carbon atoms.
A process for reducing haze in an oil additive concentrate comprising a major proportion of hydrocarbon lubricating oil;
- from 5 to 30 wt. %, based on the total weight of said concentrate, of an ethylenepropylene copolymer viscosity index improver, having a molecular weight (M.sub.n) in the range of 700 to 500,000 and a M.sub.w /M.sub.n ratio of less than 7, said copolymer consisting essentially of about 30 to 80 wt. % ethylene and propylene and prepared by a Ziegler-Natta polymerization and particles of calcium stearate having a particle size diameter in the range of about 0.01 microns to 15 microns, which causes haze in said oil;
- said process comprising adding to said concentrate dialkyl substituted benzene sulfonic acid having a (M.sub.n) of about 500 in an amount of from about 0.1 to about 2.5 equivalent per equivalent of said calcium and maintaining said oil concentrate for a period of from about 0.1 hour to about 20 hours at a temperature in the range from about room temperature to about 250.degree. C. in order to form stearic acid and the calcium salt of said sulfonic acid, whereby haze is reduced.
Dependencies are inferred from the claim text.