GB963970A - Process for the preparation of synthetic lubricants - Google Patents
Process for the preparation of synthetic lubricantsInfo
- Publication number
- GB963970A GB963970A GB15025/63A GB1502563A GB963970A GB 963970 A GB963970 A GB 963970A GB 15025/63 A GB15025/63 A GB 15025/63A GB 1502563 A GB1502563 A GB 1502563A GB 963970 A GB963970 A GB 963970A
- Authority
- GB
- United Kingdom
- Prior art keywords
- effected
- mixture
- titanium halide
- monomer
- catalyst
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M107/00—Lubricating compositions characterised by the base-material being a macromolecular compound
- C10M107/02—Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation
- C10M107/10—Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation containing aliphatic monomer having more than 4 carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F10/14—Monomers containing five or more carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
- C10M2205/02—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
- C10M2205/028—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers containing aliphatic monomers having more than four carbon atoms
- C10M2205/0285—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers containing aliphatic monomers having more than four carbon atoms used as base material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/02—Pour-point; Viscosity index
Abstract
Polymeric lubricating oils comprising a mixture of normally liquid and normally solid polymers are obtained by polymerising a C6-C16 alpha-olefin in two stages, the first being effected for 1 minute to 2 hours in the presence of a titanium halide and AlRnX3-n in which R is hydrocarbyl, X is hydrogen or halogen and n is 1, 2 or 3, in amounts such that the Ti:Al atomic ratio is 1:1-20 whereby normally solid polymer is formed and in the second adding titanium halide to the mixture to bring the Ti:Al ratio to 2-20:1 and polymerising for a further 1-16 hours to produce liquid polymers; the product is preferably hydrogenated. Polymerization is effected in each stage at 40-200 DEG F. preferably in the presence of a saturated or aromatic hydrocarbon solvent in an amount of 20-80% by volume of the total mixture of solvent and monomer; the total amount of catalyst, after addition of the further titanium halide, may be 1-10% by weight of the monomer. The catalyst is destroyed with water, an alcohol or dilute aqueous acid. Diluent and preferably dimer are removed by distillation and hydrogenation is effected at 1,000-10,000 p.s.i.g.; and 350-450 DEG F. in the presence of nickel/kieselguhr or platinum dioxide. Exemplified olefins are decene-1, and hexadecene-1.ALSO:Polymeric lubricating oils comprising a mixture of normally liquid and normally solid polymers are obtained by polymerizing a C6-C16 alpha-olefin in two stages, the first being effected for 1 minute to 2 hours in the presence of a titanium halide and AIRnX3-n in which R is hydrocarbyl, X is hydrogen or halogen and n is 1, 2 or 3, in amounts such that the Ti:Al atomic ratio is 1:1-20 whereby normally solid polymer is formed and in the second adding titanium halide to the mixture to bring the Ti:Al ratio to 2-20:1 and polymerizing for a further 1-16 hours to produce liquid polymers; the product is preferably hydrogenated. Polymerization is effected in each stage at 40-200 DEG F. preferably in the presence of a saturated or aromatic hydrocarbon solvent in an amount of 20-80% by volume of the total mixture of solvent and monomer; the total amount of catalyst, after addition of the further titanium halide, may be 1-10% by weight of the monomer. The catalyst is destroyed with water, an alcohol or dilute aqueous acid. Diluent and preferably dimer are removed by distillation and hydrogenation is effected at 1000-10,000 p.s.i.g.; and 350-450 DEG F. in the presence of nickel/kieselguhr or platinum dioxide.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US193325A US3113167A (en) | 1962-05-08 | 1962-05-08 | High viscosity synthetic lubricants from alpha-olefins |
Publications (1)
Publication Number | Publication Date |
---|---|
GB963970A true GB963970A (en) | 1964-07-15 |
Family
ID=22713168
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB15025/63A Expired GB963970A (en) | 1962-05-08 | 1963-04-17 | Process for the preparation of synthetic lubricants |
Country Status (3)
Country | Link |
---|---|
US (1) | US3113167A (en) |
DE (1) | DE1495030A1 (en) |
GB (1) | GB963970A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5177276A (en) * | 1985-06-17 | 1993-01-05 | Chevron Research Company | Alpha-olefin oligomers useful as base stocks and viscosity index improvers, and lubricating oils containing same |
US5315053A (en) * | 1985-06-17 | 1994-05-24 | Chevron Research Company | Normally liquid alpha-olefin oligomers useful as base stocks and viscosity index improvers, and lubricating oils containing same |
US5382739A (en) * | 1992-07-28 | 1995-01-17 | Bp Chemicals Limited | Lubricating oils |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL299227A (en) * | 1962-10-16 | |||
GB1019419A (en) * | 1963-09-26 | 1966-02-09 | Socony Mobil Oil Co Inc | Grease composition |
US3367909A (en) * | 1963-10-24 | 1968-02-06 | Gulf Research Development Co | Poly-alpha-olefin heat seal composition |
US3303239A (en) * | 1963-12-23 | 1967-02-07 | Phillips Petroleum Co | Olefin polymerization |
US3280031A (en) * | 1963-12-31 | 1966-10-18 | Mobil Oil Corp | High temperature lubricating oils |
US3506573A (en) * | 1968-05-29 | 1970-04-14 | Mobil Oil Corp | Greases containing a hydrogenated olefin polymer vehicle,organophilic clay thickener and calcium acetate dispersion |
US3876722A (en) * | 1968-09-16 | 1975-04-08 | Exxon Research Engineering Co | Copolymer of c' 3 'to c' 8 'alpha-olefin and c' 22 'to c' 40 'alpha-olefin |
US3947507A (en) * | 1973-03-05 | 1976-03-30 | Lion Fat & Oil Co., Ltd. | Method of producing liquid olefin polymer |
JPS5145012B2 (en) * | 1973-03-05 | 1976-12-01 | ||
IT981299B (en) * | 1973-03-12 | 1974-10-10 | Snam Progetti | PRODUCTION OF LIQUID POLYMERS WITH VERY HIGH VISCOSITY |
US4244831A (en) * | 1976-04-07 | 1981-01-13 | Union Carbide Corporation | Silicone-hydrocarbon compositions |
US4642410A (en) * | 1985-03-14 | 1987-02-10 | Uniroyal Chemical Company, Inc. | Catalytic poly alpha-olefin process |
US4912272A (en) * | 1988-06-23 | 1990-03-27 | Mobil Oil Corporation | Lubricant blends having high viscosity indices |
US6075174A (en) * | 1995-05-08 | 2000-06-13 | Bp Amoco Corporation | BF3 removal from BF3 catalyzed olefin oligomer |
DE69936203T2 (en) * | 1998-06-30 | 2008-01-31 | Chevron Phillips Chemical Co. Lp, Houston | POLYALPHAOLEFINS WITH IMPROVED OXIDATION STABILITY AND METHOD FOR THE PRODUCTION THEREOF |
US7880047B2 (en) * | 2008-05-06 | 2011-02-01 | Chemtura Corporation | Polyalphaolefins and processes for forming polyalphaolefins |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB873067A (en) * | 1959-04-28 | 1961-07-19 | Shell Res Ltd | Hydrocarbon polymers |
-
1962
- 1962-05-08 US US193325A patent/US3113167A/en not_active Expired - Lifetime
-
1963
- 1963-04-17 GB GB15025/63A patent/GB963970A/en not_active Expired
- 1963-05-02 DE DE19631495030 patent/DE1495030A1/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5177276A (en) * | 1985-06-17 | 1993-01-05 | Chevron Research Company | Alpha-olefin oligomers useful as base stocks and viscosity index improvers, and lubricating oils containing same |
US5315053A (en) * | 1985-06-17 | 1994-05-24 | Chevron Research Company | Normally liquid alpha-olefin oligomers useful as base stocks and viscosity index improvers, and lubricating oils containing same |
US5382739A (en) * | 1992-07-28 | 1995-01-17 | Bp Chemicals Limited | Lubricating oils |
Also Published As
Publication number | Publication date |
---|---|
DE1495030A1 (en) | 1969-05-14 |
US3113167A (en) | 1963-12-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB963970A (en) | Process for the preparation of synthetic lubricants | |
EP0023249B1 (en) | Process for the production of substantially amorphous copolymers of butene-1, propylene and ethylene with a high softening point | |
DE913826C (en) | Process for the preparation of polymerization products | |
US3522180A (en) | Lubricating oil compositions containing amorphous ethylene-propylene copolymers | |
US2554280A (en) | Preparation of resin-drying oil mixture | |
CA1051464A (en) | Synthetic saturated oils, and their production and use | |
Modena et al. | Some low molecular weight polymers of d‐limonene and related terpenes obtained by Ziegler‐type catalysts | |
GB824460A (en) | Hydrocarbon polymers; processes for preparing said polymers; and compositions containing said polymers | |
US2265450A (en) | Polymeric n-vinyl lactams and process of producing same | |
US4219691A (en) | Process for producing olefin oligomer | |
US2637720A (en) | Method of polymerizing isobutylene in the presence of nu-butenes and ether | |
US3285902A (en) | Emulsifiable waxes and their production | |
GB940143A (en) | Liquid polymers from alpha-olefins | |
US2357926A (en) | Polymerization | |
US3433845A (en) | Process of solubilizing,via hydrogenation,alpha-methylstyrene polymers and product obtained thereby | |
US3413278A (en) | Process for the production of telomers of ethylene with amines and products | |
DE938978C (en) | Mineral lubricating oils with an increased viscosity index | |
DE3150270A1 (en) | High-pressure polymerisation of ethylene | |
DE557306C (en) | Process for improving lubricating oils | |
US3043793A (en) | Process for lowering the brittle point of solid heptane-insoluble polypropylene | |
DE2407164A1 (en) | METHOD OF PRODUCING A THERMOPLASTIC RESIN | |
US2255409A (en) | Cyclopentadiene resin | |
US2767229A (en) | Stabilizing drying oils | |
US2530772A (en) | Phenolic condensation product | |
DE1266502B (en) | Process for the production of high molecular weight polymers of vinyl alkyl ethers |