GB474885A - A process for producing lubricating oil or additions to lubricating oil - Google Patents
A process for producing lubricating oil or additions to lubricating oilInfo
- Publication number
- GB474885A GB474885A GB7887/37A GB788737A GB474885A GB 474885 A GB474885 A GB 474885A GB 7887/37 A GB7887/37 A GB 7887/37A GB 788737 A GB788737 A GB 788737A GB 474885 A GB474885 A GB 474885A
- Authority
- GB
- United Kingdom
- Prior art keywords
- per cent
- residue
- product
- pressures
- oils
- 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
- C10M101/00—Lubricating compositions characterised by the base-material being a mineral or fatty oil
- C10M101/02—Petroleum fractions
-
- 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
- C10M2205/22—Alkylation reaction products with aromatic type compounds, e.g. Friedel-crafts
-
- 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
- C10N2060/00—Chemical after-treatment of the constituents of the lubricating composition
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Viscous oils of high viscosity index, used as lubricants or additions to lubricating oils, are obtained by polymerizing gaseous alkenes at increased pressures and at temperatures above 125 DEG C. to products containing large proportions of gasoline, removing the gasoline, and then further polymerizing the residue in presence of a catalyst at temperatures below 125 DEG C. and at pressures lower than those used in the first stage. The product may be refined, e.g. by hydrogenation, sulphuric acid, or bleaching earth. Alkenes specified are propene, butenes, mixtures thereof, and gas mixtures containing them as the larger part of the unsaturated constituents, e.g. gases obtained by cracking paraffin wax or mineral oils or residues. The polymerization of the higher-boiling fraction may take place in presence of benzene, naphthalene, or mineral oils rich in aromatics. Suitable catalysts are aluminium chloride and boron fluoride. Catalysts are preferably present in the first polymerization; phosphoric acid, sulphuric acid, benzene-sulphonic acid, bleaching earth, and floridine are suitable. Both polymerizations may be in stages. In an example, cracking gas is passed over a phosphoric acid-kieselguhr catalyst at 200--250 DEG C. and 10--15 atmos. until 90 per cent of the olefines is converted; the product is distilled to 180 DEG C., 87,5 per cent passing over as a high anti-knock gasoline; the residue is polymerized at 100 DEG C. and atmospheric pressure for 5 hours in presence of 4 per cent of aluminium chloride.ALSO:Viscous oils of high viscosity index, used as lubricants or additions to lubricating oils, are obtained by polymerizing gaseous olefines at raised pressures and at temperatures above 125 DEG C. to products consisting largely of gasolene, removing the gasolene, and further polymerizing the residue in presence of a catalyst at lower pressures and at temperatures below 125 DEG C. The product may be refined, e.g. by hydrogenation, sulphuric acid, or bleaching earth. Alkenes specified are butenes, propene, mixtures thereof, and gas mixtures containing them as the larger part of the unsaturateds, e.g. gases obtained by cracking paraffin wax or mineral oil or residues. The polymerization of the residue may take place in presence of benzene, naphthalene, or mineral oils rich in aromatics. In an example, cracking gas is passed over a phosphoric acid-kieselguhr catalyst at 200--250 DEG C. and 10--15 atmos. until 90 per cent of the olefines is polymerized; the product is distilled to 180 DEG C., 87,5 per cent passing over as a high anti-knock gasolene; the residue is polymerized at 100 DEG C. and atmospheric pressure for 5 hours in presence of 4 per cent of aluminium chloride.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL474885X | 1936-03-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB474885A true GB474885A (en) | 1937-11-09 |
Family
ID=19786510
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB7887/37A Expired GB474885A (en) | 1936-03-25 | 1937-03-17 | A process for producing lubricating oil or additions to lubricating oil |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB474885A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4855527A (en) * | 1987-10-07 | 1989-08-08 | Mobil Oil Corporation | Olefin oligomerization with surface modified zeolite |
US4870038A (en) * | 1987-10-07 | 1989-09-26 | Mobil Oil Corporation | Olefin oligomerization with surface modified zeolite catalyst |
US5026933A (en) * | 1987-10-07 | 1991-06-25 | Mobil Oil Corporation | Olefin oligomerization with surface modified zeolite catalyst |
-
1937
- 1937-03-17 GB GB7887/37A patent/GB474885A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4855527A (en) * | 1987-10-07 | 1989-08-08 | Mobil Oil Corporation | Olefin oligomerization with surface modified zeolite |
US4870038A (en) * | 1987-10-07 | 1989-09-26 | Mobil Oil Corporation | Olefin oligomerization with surface modified zeolite catalyst |
US5026933A (en) * | 1987-10-07 | 1991-06-25 | Mobil Oil Corporation | Olefin oligomerization with surface modified zeolite catalyst |
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