GB992537A - Polymerization process - Google Patents
Polymerization processInfo
- Publication number
- GB992537A GB992537A GB4430/64A GB443064A GB992537A GB 992537 A GB992537 A GB 992537A GB 4430/64 A GB4430/64 A GB 4430/64A GB 443064 A GB443064 A GB 443064A GB 992537 A GB992537 A GB 992537A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reactor
- butene
- monomer
- styrene
- temperature
- 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
- C08F2/00—Processes of polymerisation
- C08F2/04—Polymerisation in solution
- C08F2/06—Organic solvent
-
- 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
-
- 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
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/04—Monomers containing three or four carbon atoms
- C08F110/06—Propene
Abstract
A continuous process for solution polymerizing an olefinic compound of the formula CH2 = CHR, wherein R is hydrogen or an alkyl, aryl, cycloalkyl or haloaryl radical containing not more than 12 carbon atoms comprises polymerizing a stirred reaction mixture at a temperature just above the precipitation temperature of the polymer and controlling the monomer concentration in the reactor. Polymers exemplified are homopolymers of propylene, butene-1, n-pentene-1, 3-methyl-butene-1, and n-octene-1; copolymers of propylene with ethylene, styrene, butadiene, and vinyl cyclohexane; and copolymers of butene-1 with p-methyl styrene, and n-pentene-1 with p-chloro styrene. Catalysts exemplified are: the reaction product of titanium trichloride, aluminium triethyl, thiocresol and lithium triethanolamine; TiCl4 + Al(C2H5)3; TiCl3 + Al triisobutyl; ZrCl4 + Al(C2H5)3; ZrCl3 + Al tributyl; n-butyl Li; LiAl(C2H5)4; and TiCl4 + Ti metal. Many other monomers and catalysts are specified. Suitable solvents are xylene or mixed octanes. The polymers produced have a high isotactic content. The polymerization is effected in a reactor under isothermal and essentially adiabatic conditions. The temperature of the reactor is automatically controlled by simultaneously varying the monomer and solvent feed rates while maintaining the ratio of the two. The monomer concentration in the reactor is varied by adjusting the monomer/solvent feed ratio. A flow diagram is given.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US25659863A | 1963-02-06 | 1963-02-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB992537A true GB992537A (en) | 1965-05-19 |
Family
ID=22972841
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4430/64A Expired GB992537A (en) | 1963-02-06 | 1964-02-03 | Polymerization process |
Country Status (4)
Country | Link |
---|---|
BE (1) | BE643455A (en) |
DE (1) | DE1495493A1 (en) |
GB (1) | GB992537A (en) |
NL (1) | NL6400976A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0519009A1 (en) * | 1990-03-09 | 1992-12-23 | Board Of Control Of Michigan Technological University | Free-radical retrograde precipitation-polymerization process |
WO2003059960A1 (en) * | 2002-01-11 | 2003-07-24 | National Starch And Chemical Investment Holding Corporation | Free radical retrograde precipitation polymer dispersions |
WO2020178010A1 (en) * | 2019-03-04 | 2020-09-10 | Borealis Ag | Polymerization process |
-
1964
- 1964-02-03 GB GB4430/64A patent/GB992537A/en not_active Expired
- 1964-02-06 BE BE643455A patent/BE643455A/xx unknown
- 1964-02-06 DE DE19641495493 patent/DE1495493A1/en active Pending
- 1964-02-06 NL NL6400976A patent/NL6400976A/xx unknown
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0519009A1 (en) * | 1990-03-09 | 1992-12-23 | Board Of Control Of Michigan Technological University | Free-radical retrograde precipitation-polymerization process |
EP0519009A4 (en) * | 1990-03-09 | 1993-08-04 | Michigan Technological University | Free-radical retrograde precipitation-polymerization process |
WO2003059960A1 (en) * | 2002-01-11 | 2003-07-24 | National Starch And Chemical Investment Holding Corporation | Free radical retrograde precipitation polymer dispersions |
WO2020178010A1 (en) * | 2019-03-04 | 2020-09-10 | Borealis Ag | Polymerization process |
Also Published As
Publication number | Publication date |
---|---|
BE643455A (en) | 1964-08-06 |
DE1495493A1 (en) | 1969-06-12 |
NL6400976A (en) | 1964-08-07 |
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