GB886893A - Purification of olefines for low-pressure polymerisation - Google Patents
Purification of olefines for low-pressure polymerisationInfo
- Publication number
- GB886893A GB886893A GB37068/60A GB3706860A GB886893A GB 886893 A GB886893 A GB 886893A GB 37068/60 A GB37068/60 A GB 37068/60A GB 3706860 A GB3706860 A GB 3706860A GB 886893 A GB886893 A GB 886893A
- Authority
- GB
- United Kingdom
- Prior art keywords
- alumina
- silica gel
- chromium trioxide
- mass
- olefin
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Abstract
Olefins containing 2-4 carbon atoms are purified, prior to low pressure polymerization, with a purification mass containing chromium trioxide at -20 to 60 DEG C. The olefin is preferably prepurified to less than 1% impurities. The chromium trioxide may be a conventional polymerization catalyst, e.g. supported on alumina, aluminium silicate, magnesium silicate or silica gel and forming 1-10% by weight of the carrier. The mass may be diluted with polyethylene, polypropylene, alumina, aluminium or magnesium silicate or silica gel, and may be used in fixed or fluidized beds in continuous processes. Internal or external cooling may be applied, 'e.g. by decompression in the purifying tower from 50-60 down to 20-30 atmospheres. The purified olefin, e.g. ethylene or propylene, may be conventionally polymerized with a chromium trioxide or other low pressure catalyst, e.g. TiCl4 and Al(C2H5)3.ALSO:Olefins containing 2 to 4 carbon atoms are purified by contact with a purification mass containing chromium trioxide at -20 DEG C. to 60 DEG C. The olefin may be first purified conventionally, e.g. with caustic potash, alumina, silica gel or diethyl zinc and preferably contains less than 1% of impurities. The chromium trioxide may be present in an amount of 1%-10% by weight of a carrier, e.g. alumina, aluminium sili ate, magnesium silicate or silica gel and the mass may be diluted with an inert solid, e.g. polyethylene, polypropylene, alumina, aluminium silicates, magnesium silicate, iron oxide or silica gel. In batch processes the amount of the mass may be 0.01%-150% by weight of the olefin and in continuous processes may be in a fixed or fluidised bed; it may be regenerated by oxidation. Internal or external cooling may be applied, e.g. by reducing the pressure from 50-60 atmospheres down to 20-30 atmospheres.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE886893X | 1959-10-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB886893A true GB886893A (en) | 1962-01-10 |
Family
ID=6833544
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB37068/60A Expired GB886893A (en) | 1959-10-30 | 1960-10-28 | Purification of olefines for low-pressure polymerisation |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB886893A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0537628A2 (en) * | 1991-10-08 | 1993-04-21 | Montell North America Inc. | Process for the removal of carbon monoxide from alphaolefins and saturated hydrocarbons |
EP0818432A1 (en) * | 1996-07-10 | 1998-01-14 | The Lubrizol Corporation | Catalytic process for making high reactivity alkylating agents and products resulting therefrom |
-
1960
- 1960-10-28 GB GB37068/60A patent/GB886893A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0537628A2 (en) * | 1991-10-08 | 1993-04-21 | Montell North America Inc. | Process for the removal of carbon monoxide from alphaolefins and saturated hydrocarbons |
EP0537628A3 (en) * | 1991-10-08 | 1993-05-12 | Himont Incorporated | Process for the removal of carbon monoxide from alphaolefins and saturated hydrocarbons |
US5625116A (en) * | 1991-10-08 | 1997-04-29 | Montell North America Inc. | Process for the removal of carbon monoxide from alpha-olefins and saturated hydrocarbons |
EP0818432A1 (en) * | 1996-07-10 | 1998-01-14 | The Lubrizol Corporation | Catalytic process for making high reactivity alkylating agents and products resulting therefrom |
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