US 4,952,637 AGrant
Hydrocarbon Compositions Containing Polyolefin Graft Polymers
Issue Date:1990-08-28
•2 Claims
Abstract
Fuel oils and lubricants of improved properties contain ethylene-propylene copolymers bearing units derived from N-vinyl pyrrolidone and phenothiazine.
Metadata
Assignee
- Texaco Inc.
Inventors
- Maria M. Kapuscinski
- Larry D. Grina
- Ronald E. Jones
- Rodney Lu-Dai Sung
Application Information
Application Number:US 222870&
Filing Date:1988-07-22
Priority Date:1985-04-24
Art Unit:151
Classifications
IPC:
C08F25504C08F25506
Field of Search:
525279;256;331.7;284;293;281;349;164
Patent Drawings
This patent does not have any drawings.
Description
Description of Preferred Embodiments
Example I
In this example which describes the best mode presently known, the charge EPM polymer is the polymer of molecular weight M.sub.n of 140,000 of M.sub.w /M.sub.n ratio of 1.6, and containing 60 mole % of units derived from ethylene and 40 mole % of units derived from propylene. 100 parts of this polymer are dissolved in 300 parts of commercial hexane and added to a reaction vessel.
In the first step, the mixture is heated to 155.degree. C. with agitation under nitrogen atmosphere at 200 psig. N-vinyl pyrrolidone (5 parts dissolved in 15 parts of hexane) is added followed by 5 parts of 25 w % dicumyl peroxide in hexane. The reaction mixture is stirred for one hour.
In the second step, phenothiazine (4 parts) dissolved in 16 parts of tetrahydrofuran is added followed by a solution of 2 part of dicumyl peroxide initiator in 6 parts of commercial hexane. The mixture is stirred at 155.degree. C. and 200 psig for 1 hour. Solvent Neutral Oil (SUS 100) (1076 parts) is then added; and the hexane is distilled off at 90-.degree.120.degree. C. The resulting solution contains about 8.5 w % polymer.
The product polymer contains (per 1000 carbon atoms of polymer backbone) about 6 units derived from N-vinyl pyrollidone and 3 units derived from phenothiazine.
The process of Example I may be carried out using the charge polymers of Examples II-IV:
Example Ii
The Epsyn 4006 brand of EPT marketed by Copolymer containing 58 mole % of units derived from ethylene, 40 mole % of units derived from propylene, and 2 mole % of units derived from ethylidene norbornene and having a M.sub.n of 120,000 and a M.sub.w /M.sub.n of 2.2.
Example Iii
The Ortholeum 2052 brand of EPT marketed by DuPont containing 62 mole % of units derived from ethylene, 36 mole % of units derived from propylene, and 2 mole % of units derived from 1,4-hexadiene and having a M.sub.n of 35,000 and a M.sub.w /M.sub.n of 2.
Example Iv
The Royalene brand of EPT marketed by Uniroyal containing 60 mole % of units derived from ethylene, 37 mole % of units derived from propylene and 3 mole % of units derived from dicyclopentadiene and having a M.sub.n of 100,000 and a M.sub.w /M.sub.n of 2.5.
Example V*
In this control Example, the N-vinylpyrrolidone grafted EPM (as a 25 w % solution in hexane) is prepared as in Example I. Solvent hexane is exchanged for SNO-100 oil (1076 parts) to give a solution containing 8.5 w % polymer.
There are then added 4 parts of phenothiazine dissolved in 16 parts of tetrahydrofuran; and the mixture maintained at 70.degree. C.-80.degree. C. under nitrogen for one hour.
This mixture contains the same quantity of N-vinyl pyrrolidone and of phenothiazine as does the product of Example I. In this Example V*, the phenothiazine is merely admixed.
Example Vi*
In this control example, the procedure of Example V* is followed except that the phenothiazine in tetrahydrofuran is not added.
Example Vii
In this experimental Example, the procedure of Example I is followed except that the first graft monomer is (instead of N-vinylpyrrolidone) a monomer (8 parts) prepared by heating, for one hour at 100.degree. C.-120.degree. C., a mixture of equimolar amounts of allyl glycidyl ether and morpholine. The polymer product contains (per 1000 carbon atoms in the polymer backbone) 5 units derived from the reaction product of allyl glycidyl ether and morpholine and 3 units derived from phenothiazine. It is recovered as a 8.5 wt. % solution in SNO-100 oil.
Example Viii*
In this control Example, the procedure of Example V* is followed except that the first graft monomer is the reaction product of allyl glycidyl ether and morpholine--prepared as in Example VII.
Example Ix
In this control Example, the procedure of Example VI* is followed except that the first graft monomer is the reaction product of allyl glycidyl ether and morpholine--prepared as in Example VIII .
Example X
In this experimental example, the procedure of Example I is followed except that the first functional monomer is (instead of N-vinyl pyrrolidone) a monomer (6 parts) prepared by heating for one hour at 100.degree. C.-120.degree. C., a mixture of equimolar amounts of allyl glycidyl ether and N-methylpiperazine. The polymer product contains (per 1000 carbons of polymeric chain) 4 units derived from the reaction product of allyl glycidyl ether and N-methyl piperazine and 3 units derived from phenothiazine. It is recovered as a 8.5 wt. % polymer solution is SNO-100 oil.
Example Xi
In this experimental example, the procedure of Example I is followed except that the first functional monomer is (instead of N-vinyl pyrrolidone) a monomer (8 parts) prepared by heating for one hour at 90-100.degree. C., a mixture of equimolar amounts of croton aldehyde and N-(3-aminopropyl)morpholine. The polymer product contains (per 1000 carbons of polymeric chain) 4.5 units derived from the reaction product of croton aldehyde and N-(3-aminopropyl) morpholine, and 3 units derived from phenothiazine. It is recovered as a 8.5 wt. % solution in SNO-100 oil.
Example Xii
In this experimental example, the charge EPM polymer has a molecular weight M.sub.n of 140,000, M.sub.w /M.sub.n ratio of 1.6, and contains 60 mole % of units derived from ethylene and 40 mole % of units derived from propylene. 100 parts of this polymer are dissolved in 300 parts of commercial hexane and added to a reaction vessel.
The mixture is heated to 155.degree. C. with agitation under nitrogen at 200 psig. There are added (i) 5 parts of N-vinylpyrrolidone, dissolved in 15 parts of hexane, (ii) 2 parts of phenothiazine, dissolved in 8 parts of tetrahydrofuran, and (iii) 6.0 parts of dicumyl peroxide dissolved in 18 parts of hexane.
The mixture is stirred at 155.degree. C. and 200 psig for one hour under nitrogen. Solvent Neutral Oil (SUS 100) is then added (1076 parts); and the hexane is distilled off at 90.degree. C.-120.degree. C. The resulting solution contains about 8.5 w % polymer.
The product polymer contains (per 1000 carbon atoms in the polymer backbone) about 6 units derived from N-vinyl pyrrolidone and 1.5 units derived from phenothiazine.
Each of the products of Examples I and V*-XII is formulated with a fully formulated base blend to yield a composition containing 0.85 wt. % polymer; and these compositions are subjected to the Bench VC Test (BVCT).
The fully formulated base blend contains the following components:
The products of Examples I and V*-XII are subjected to the Bench Oxidation Test to determine whether the additive is a satisfactory anti-oxidant. In this test, products of Examples I and V*-XII are formulated with SNO-130 Oil to yield a solution containing 1.5 wt. % polymer. The solution is heated with stirring and air agitation. Samples are withdrawn periodically and analyzed by Differential Infrared Absorption (DIR) to observe changes in the intensity of the carbonyl vibration based on 1710 cm.sup.-1. They are also tested in the Clarity Test and the Lumetron Turbidity Test.
The Oxidation Index is reported as the Carbonyl Group Absorbance in the Differential Infrared Spectra after 144 hours of oxidation. The Oxidation Index may range from 0 up to 100 and a low rating is desired. A rating below 4 is considered excellent.
The Clarity of the samples is also reported visually and by the Lumetron Turbidity Test after 144 hours. In the Lumetron Turbidity Test, product turbidity is determined by a Lumetron Photoelectric Colorimeter.
The Lumetron Turbidity is reported on a scale of 0-100. A rating of below about 20 is satisfactory; higher ratings are less satisfactory.
From the above Table, it is apparent that the experimental Examples I, VII, and X-XII are characterized by a desirably low Oxidation Index (i.e, freedom from oxidation), by a visually clear reading, and by a desirably low Lumetron Turbidity rating. Control Examples VI*, and IX* which fall outside the scope of this invention are characterized by undesirably higher oxidation indices, by a visually turbid reading, and by undesirably high Lumetron Turbidity rating. Control Examples V* and VIII* are unsatisfactory by the latter two criteria.
Experimental Examples I, VII, and X-XII are also characterized by satisfactory BVCT ratings.
It is clear from these tests that the products of the instant invention which contain polymers bearing first dispersant graft monomers and second anti-oxidant monomers possess the ability to form lubricating oils characterized by desirable properties including high dispersancy, anti-oxidant activity, and desirable viscosity index.
Example Xiii*
In this control Example, a base diesel fuel having the following properties is tested in the Potential Deposit Test and found to have an unsatisfactory rating of 4+.
Example Xiv
In this experimental Example, there is added to the base fuel of Example XIII*, 8.5 w % of the polymer of Example I to yield a mix containing 25 PTB (corresponding to 0.01 wt. % or alternatively to a nitrogen content of 0.054 w %).
The modified diesel fuel is found to have a PDT rating of 1 which is satisfactory.
Example Xv*
In this control Example, a commercial olefin copolymer dispersant VI improver is blended into formulated oil not containing a VI improver. The blend is subjected to the single cylinder MWM-B Diesel Engine Test. In this test, results are presented in merits which correlate with amount of deposits. Higher merits correspond to lower deposits.
Examples Xvi-Xvii
In these experimental Examples, the procedure of Example XV* is followed except that the product of Example I is added in Example XVI and the product of Example X is added in Example XVII (instead of the commercial olefin copolymer dispersant VI improver) to a formulated oil not containing a VI improver.
From the above table, it is apparent that the experimental Examples XVI and XVII are characterized by a better deposit protection (higher merits) than the commercial dispersant olefin copolymer VI improver of Example XV*.
Although this invention has been illustrated by reference to specific embodiments, it will be apparent to those skilled in the art that various changes and modifications may be made which clearly fall within the scope of this invention.
Claims
What is claimed is:
1. The process for preparing a graft polymer which comprises intimately mixing in a reaction mixture (a) an oil-soluble, substantially linear, carbon-carbon backbone polymer of molecular weight M.sub.n of 10,000-1,000,000; (b) as a first graft monomer amine containing a polymerizable ethylenically unsaturated double bond, (i) N-vinylpyrrolidone, (ii) N-vinylimidazole, (iii) the reaction product of an amine and an epoxy of an aliphatic unsaturated carbocyclic acid, (iv) the reaction product of an amine and an ether containing an epoxy group and an ethylenically unsaturated carbon-to-carbon double bond, or (v) the reaction product of an amine and an aldehyde containing a carbon-to-carbon double bond; (c) as a second functional monomer, a phenothiazine; and (d) a free radial initiator; maintaining the temperature of the reaction mixture at a temperature at least as high as the decomposition temperature of said initiator thereby effecting decomposition of said initiator and bonding of said first and second monomers onto said backbone polymer to form graft polymer; and recovering said graft polymer.
2. The process for preparing a graft polymer which comprises intimately admixing in a reaction mixture (i) an oil-soluble, substantially linear, carbon-carbon backbone polymer, (ii) first graft monomer amine containing a polymerizable ethylenically unsaturated double bond and (iii) a free radical initiator, maintaining the temperature of the reaction mixture at a temperature at least as high as the decomposition temperature of said initiator thereby effecting decomposition of said initiator and binding of said graft monomer onto said backbone polymer to form graft polymer; intimately admixing in a reaction mixture (i) said graft polymer and (iii) as a second functional monomer, a phenothiazine and (iii) a free radical initiator; maintaining the temperature of the reaction mixture at a temperature at least as high as said decomposition temperature thereby effecting decomposition of said initiator and bonding said second functional monomer onto said graft polymer to form product graft polymer; and recovering said product graft polymer.