GB765501A - Improvements in or relating to polymerization of ethylene propylene and isobutylene - Google Patents
Improvements in or relating to polymerization of ethylene propylene and isobutyleneInfo
- Publication number
- GB765501A GB765501A GB34175/54A GB3417554A GB765501A GB 765501 A GB765501 A GB 765501A GB 34175/54 A GB34175/54 A GB 34175/54A GB 3417554 A GB3417554 A GB 3417554A GB 765501 A GB765501 A GB 765501A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stage
- butyl
- isobutylene
- polymer
- ethylene
- 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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
<PICT:0765501/IV(a)/1> Ethylene, propylene and isobutylene are polymerized in the presence of a free-radical catalyst at a pressure above 500 atmospheres in a plurality of stages, e.g. in a plurality of reaction vessels, in which a sufficient quantity of free-radical catalyst to polymerize only a portion of the monomer is added prior to each stage and the product from each stage is deactivated and the polymer recovered at the reaction pressure. Deactivation may be effected by reducing the temperature, e.g. 10 DEG to 100 DEG C. below the reaction temperature, or by adding a more reactive monomer such as propylene, styrene, vinyl chloride, butadiene, butene, isobutylene, acrylonitrile or substances containing secondary or tertiary hydrogen. The polymer may be collected after each stage or after the final stage. Catalysts such as oxygen, benzoyl, acetyl, acetyl-benzoyl, di-t.-butyl, potassium, zinc, lauryl, succinyl, m-bromobenzoyl, urea, and cyclohexanone peroxides, t.-butyl, di-isopropylbenzene, and p-methane hydroperoxides, a -a 1-azo-bis-isobutyronitrile, peracetic and persuccinic acids, alkaline earth metal persulphates, perborates, perchlorates, dialkyl peroxy dicarbonates, ascaridole, nitric acid, manganese dioxide, tetraphenyl tin, tetraethyl lead and Grignard-type compounds may be used and polymerization effected in a liquid medium, e.g. water, benzene, toluene, chlorobenzene, 2,2,4-dimethylpentane, methyl t.-butyl ether, t.-butyl alcohol, pentamethylethylene, methyl pivalate and pivaloin. In an example ethylene containing oxygen as catalyst is compressed to 1500 atmospheres in a compressor 30, heated to 210 DEG C., 60, and passed to a reactor 10, cooled to 120 DEG C., 40, and the polymer separated in 70. Unpolymerized ethylene is heated in a second vessel 60, additional oxygen added and passed to a second reactor 12 at 210 DEG C. The cycle may be repeated to obtain the desired conversion and yield a product of uniform molecular weight suitable for films, moulded products and structural forms.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US765501XA | 1953-12-24 | 1953-12-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB765501A true GB765501A (en) | 1957-01-09 |
Family
ID=22132728
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB34175/54A Expired GB765501A (en) | 1953-12-24 | 1954-11-25 | Improvements in or relating to polymerization of ethylene propylene and isobutylene |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB765501A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2322554A1 (en) * | 1973-05-04 | 1974-11-21 | Sumitomo Chemical Co | METHOD AND DEVICE FOR THE PRODUCTION OF AETHYLENE POLYMERIZES |
DE2853069A1 (en) * | 1978-12-08 | 1980-06-12 | Erdoelchemie Gmbh | METHOD FOR PRODUCING COMPOSITE SYSTEMS AND HIGH PRESSURE POLYETHYLENE COATING RESIN |
US4229416A (en) * | 1978-10-02 | 1980-10-21 | National Distillers And Chemical Corporation | Dual reactor apparatus for polymerizing ethylene |
-
1954
- 1954-11-25 GB GB34175/54A patent/GB765501A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2322554A1 (en) * | 1973-05-04 | 1974-11-21 | Sumitomo Chemical Co | METHOD AND DEVICE FOR THE PRODUCTION OF AETHYLENE POLYMERIZES |
US4229416A (en) * | 1978-10-02 | 1980-10-21 | National Distillers And Chemical Corporation | Dual reactor apparatus for polymerizing ethylene |
DE2853069A1 (en) * | 1978-12-08 | 1980-06-12 | Erdoelchemie Gmbh | METHOD FOR PRODUCING COMPOSITE SYSTEMS AND HIGH PRESSURE POLYETHYLENE COATING RESIN |
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