GB832505A - Process for the continuous production of polyolefines of uniform molecular weight - Google Patents
Process for the continuous production of polyolefines of uniform molecular weightInfo
- Publication number
- GB832505A GB832505A GB5309/56A GB530956A GB832505A GB 832505 A GB832505 A GB 832505A GB 5309/56 A GB5309/56 A GB 5309/56A GB 530956 A GB530956 A GB 530956A GB 832505 A GB832505 A GB 832505A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- reactor
- column
- residence time
- polyolefines
- 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)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
A Ziegler catalyst for use in the continuous production of polyolefines, is stabilized by using in an initial polymerization at about 20-60 DEG C. and for a short residence time in a pre-reactor before continuously introducing into the main reactor which is at a higher temperature, e.g. about 80 DEG C. In an example the catalyst is formed by mixing aluminium diethyl chloride and titanium tetrachloride in cyclohexane.ALSO:Polyolefines of uniform molecular weight are obtained by a continuous process using Ziegler catalysts, characterized in that the catalyst is used in an initial polymerization at about 20-60 DEG C. and for a short residence time in a pre-reactor, and is then continuously introduced into the main reactor which is at a temperature above that of the pre-reactor, e.g. at about 80 DEG C. In the example ethylene is polymerized with cyclohexane as diluent and with a catalyst formed from aluminium diethyl chloride and titanium tetrachloride. The apparatus used consists of 3 reaction columns through which the reaction components flow. In the first column the catalyst components and diluent are mixed and then flow into the second column, at 20 DEG to 60 DEG C., into which ethylene is also introduced. The residence time in this pre-reactor is 10 minutes and the catalyst and reaction medium containing some polymer then passes into the third column into which further ethylene and cyclohexane are also introduced. The residence time in the third column is 3 hours.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE832505X | 1955-11-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB832505A true GB832505A (en) | 1960-04-13 |
Family
ID=6756653
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5309/56A Expired GB832505A (en) | 1955-11-05 | 1956-02-21 | Process for the continuous production of polyolefines of uniform molecular weight |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB832505A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3723403A (en) * | 1968-10-30 | 1973-03-27 | Ici Ltd | Olefine polymerization at high pressures using a dispersed ziegler-type catalyst |
-
1956
- 1956-02-21 GB GB5309/56A patent/GB832505A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3723403A (en) * | 1968-10-30 | 1973-03-27 | Ici Ltd | Olefine polymerization at high pressures using a dispersed ziegler-type catalyst |
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