GB454176A - Improvements relating to the separation of waxy constituents from hydrocarbon oils - Google Patents
Improvements relating to the separation of waxy constituents from hydrocarbon oilsInfo
- Publication number
- GB454176A GB454176A GB14107/35A GB1410735A GB454176A GB 454176 A GB454176 A GB 454176A GB 14107/35 A GB14107/35 A GB 14107/35A GB 1410735 A GB1410735 A GB 1410735A GB 454176 A GB454176 A GB 454176A
- Authority
- GB
- United Kingdom
- Prior art keywords
- wax
- solvent
- oil
- mixture
- separated
- 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
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G73/00—Recovery or refining of mineral waxes, e.g. montan wax
- C10G73/02—Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils
- C10G73/06—Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils with the use of solvents
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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
<PICT:0454176/III/1> In the de-waxing of oils, the oil is diluted with a solvent consisting of a mixture of at least two components, one of which is selected from the group, dichloro ethane, dichloro propane and the corresponding bromine or fluorine compounds, and the other from the group, dichlor ethylene, trichlorethylene, dichlor propylene, trichlor propylene, and the corresponding bromine or fluorine compounds, whereupon the mixture is chilled and the fraction rich in wax is separated. The process may be effected in a single stage, or preferably the fraction containing wax and some oil first separated is further diluted and chilled to a lower temperature. Residual oils, hydrogenated oils containing wax, and asphaltic residuals may be treated. Wax may be separated by filtration, sedimentation or by centrifuge in which both crystalline and amorphous waxes are removed. The diluent mixtures may contain benzol and also carbon tetrachloride, fluoride or bromide. Wax-containing oil is withdrawn from a tank 1 and passes to a chiller 5 to which 3 volumes of a solvent mixture of dichlorethane and dichlor ethylene are admitted from tanks 3, 4. Chilling may be effected by evaporation of part of the solvent to a temperature of 0 DEG to -10 DEG F. by slow or shock chilling. The chilled mixture containing separated wax passes to a mixer 6 where oil and solvent are added from a later stage. The mixture is then freed from wax in a centrifuge 7 of the type described in Specification 446,607 or 446,608, and the de-waxed oil is withdrawn through a pipe 8. The separated wax containing raw oil and solvent passes to a chiller 9 to which solvent is added through a pipe 10, and the mixture is fed to a centrifuge 11 preferably of the type described in Specification 418,939. Hard wax is removed through a pipe 12 and the oil solvent is either returned to the mixer 6 through a chiller 13, or distilled to recover solvent and oil. The dewaxed oil may be finally treated with acid or clay in the presence of a solvent. The Specification as open to inspection under Sect. 91 comprises also the subject-matter of Specification 456,122. This subject-matter does not appear in the Specification as accepted.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US454176XA | 1934-07-19 | 1934-07-19 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB454176A true GB454176A (en) | 1936-09-25 |
Family
ID=21937765
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB14107/35A Expired GB454176A (en) | 1934-07-19 | 1935-05-14 | Improvements relating to the separation of waxy constituents from hydrocarbon oils |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB454176A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4572588A (en) * | 1983-03-01 | 1986-02-25 | Diehl Gmbh & Co. | Connecting elements for crawler track vehicle chains pursuant to the dually-hinged pin principle |
-
1935
- 1935-05-14 GB GB14107/35A patent/GB454176A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4572588A (en) * | 1983-03-01 | 1986-02-25 | Diehl Gmbh & Co. | Connecting elements for crawler track vehicle chains pursuant to the dually-hinged pin principle |
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