GB942749A - Production of olefin polymers - Google Patents
Production of olefin polymersInfo
- Publication number
- GB942749A GB942749A GB4327059A GB4327059A GB942749A GB 942749 A GB942749 A GB 942749A GB 4327059 A GB4327059 A GB 4327059A GB 4327059 A GB4327059 A GB 4327059A GB 942749 A GB942749 A GB 942749A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reaction zone
- olefin
- catalyst
- charge
- reaction
- 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
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
A cyclic process for polymerizing an olefin comprises passing the olefin through a cooling zone and then into a reaction zone, introducing catalyst at the inlet of the reaction zone, diluting a major portion of the reaction zone effluent with incoming olefin charge comprising fresh charge and recycled unreacted olefin in an amount sufficient to stop the reaction, recycling the thus diluted portion of the reaction zone effluent through the cooling zone and reaction zone, withdrawing the residual minor portion of the reaction zone effluent for product recovery and recycling unreacted olefin from said residual minor portion to the incoming olefin charge. Catalyst in the withdrawn stream may be converted to an adduct (e.g. by the use of NH3) which is then removed prior to the addition of an oil to form a solution of polymer in lubricating oil. The process is applicable to the polymerization of propylene, alpha-methyl styrene, butene and butene/isobutene mixture, but is advantageously applied to the polymerization of isobutylene using BF3 as catalyst. Up to 20% of closely boiling hydrocarbons also may be present. The invention is illustrated by reference to a suitable apparatus.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE585872D BE585872A (en) | 1959-12-21 | ||
GB4327059A GB942749A (en) | 1959-12-21 | 1959-12-21 | Production of olefin polymers |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB4327059A GB942749A (en) | 1959-12-21 | 1959-12-21 | Production of olefin polymers |
Publications (1)
Publication Number | Publication Date |
---|---|
GB942749A true GB942749A (en) | 1963-11-27 |
Family
ID=10428031
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4327059A Expired GB942749A (en) | 1959-12-21 | 1959-12-21 | Production of olefin polymers |
Country Status (2)
Country | Link |
---|---|
BE (1) | BE585872A (en) |
GB (1) | GB942749A (en) |
-
0
- BE BE585872D patent/BE585872A/xx unknown
-
1959
- 1959-12-21 GB GB4327059A patent/GB942749A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
BE585872A (en) |
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