GB1170299A - Process for the Manufacture of Olefin Polymers having a broad Molecular Weight Distribution - Google Patents
Process for the Manufacture of Olefin Polymers having a broad Molecular Weight DistributionInfo
- Publication number
- GB1170299A GB1170299A GB3651767A GB3651767A GB1170299A GB 1170299 A GB1170299 A GB 1170299A GB 3651767 A GB3651767 A GB 3651767A GB 3651767 A GB3651767 A GB 3651767A GB 1170299 A GB1170299 A GB 1170299A
- Authority
- GB
- United Kingdom
- Prior art keywords
- weight
- molecular weight
- reaction product
- weight distribution
- polymers
- 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
Abstract
1,170,299. Olefin polymers. FARBWERKE HOECHST A.G. 9 Aug., 1967 [9 Aug., 1966], No. 36517/67. Heading C3P. Olefin polymers having a broad molecular weight distribution are made by polymerizng ethylene alone or if desired with up to 10% by weight of propylene or butene-1, in suspension or in the gaseous phase, using hydrogen as a modifier, in the presence of a catalyst which comprises (a) 0À5 to 10 parts by weight of the solid reaction product of Ti(OR) 4-n Cl n , n being 1, 2 or 3 and R a C 1 to C 8 hydrocarbon radical, with one or more chlorine-containing alkyl-aluminium compounds and (b), 1 part by weight of the solid reaction product of TiCl 4 with one or more chlorine containing alkylaluminium compounds, the concentration of (a) and (b) being in the range of 0À05 to 0À3 millimole per litre of dispersing agent in the suspension process or per 0À5 litre of reactor volume when operating in the gaseous phase, and as activator, (c) one or more organo-aluminium compounds selected from compounds of the general formula AlR<SP>1</SP> 3 where R<SP>1</SP> stands for a C 4 to C 40 hydrocarbon radical, or a reaction product of a trialkylaluminium or a dialkylaluminium hydride with a diolefin, e.g. butadiene-1,3 or isoprene, in a concentration of 0À2 to 3 millimoles of aluminium equivalent per litre of dispersing agent or reactor volume. Exemplified polymers are a copolymer of ethylene and 2% by volume of butene-(1), and polyethylene. These polymers have an ash content of less than 0À02% by weight and a u-value greater than or equal to 10, (u-value, a measure of the broadness of the molecular weight distribution, is defined in the Specification).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEF0049906 | 1966-08-09 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1170299A true GB1170299A (en) | 1969-11-12 |
Family
ID=7103365
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3651767A Expired GB1170299A (en) | 1966-08-09 | 1967-08-09 | Process for the Manufacture of Olefin Polymers having a broad Molecular Weight Distribution |
Country Status (11)
Country | Link |
---|---|
AT (1) | AT278348B (en) |
BE (1) | BE702472A (en) |
CS (1) | CS158612B2 (en) |
DE (1) | DE1595665C3 (en) |
ES (1) | ES343723A1 (en) |
FI (1) | FI46852C (en) |
GB (1) | GB1170299A (en) |
NL (1) | NL154751B (en) |
NO (1) | NO125681B (en) |
SE (1) | SE339997B (en) |
YU (1) | YU31351B (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4363902A (en) * | 1980-03-17 | 1982-12-14 | Wacker-Chemie Gmbh | Process and heavy metal catalyst for the polymerization of α-olefins, particularly polyethylene |
US4366298A (en) * | 1979-07-05 | 1982-12-28 | Wacker-Chemie Gmbh | Process and heavy metal catalyst for the polymerization of α-olefins, particularly polyethylene |
EP0134100A1 (en) * | 1983-08-31 | 1985-03-13 | Exxon Research And Engineering Company | Cocatalyst for use with a transition metal compound in polyethylene production |
US4935474A (en) * | 1983-06-06 | 1990-06-19 | Exxon Research & Engineering Company | Process and catalyst for producing polyethylene having a broad molecular weight distribution |
WO2005100414A1 (en) * | 2004-04-07 | 2005-10-27 | Union Carbide Chemicals & Plastics Technology Corporation | Method of controlling olefin polymerization |
-
1966
- 1966-08-09 DE DE19661595665 patent/DE1595665C3/en not_active Expired
-
1967
- 1967-07-25 YU YU148367A patent/YU31351B/en unknown
- 1967-08-02 ES ES343723A patent/ES343723A1/en not_active Expired
- 1967-08-07 NO NO16928267A patent/NO125681B/no unknown
- 1967-08-07 AT AT730467A patent/AT278348B/en not_active IP Right Cessation
- 1967-08-08 SE SE1126067A patent/SE339997B/xx unknown
- 1967-08-08 NL NL6710898A patent/NL154751B/en unknown
- 1967-08-08 FI FI214067A patent/FI46852C/en active
- 1967-08-09 BE BE702472D patent/BE702472A/xx unknown
- 1967-08-09 GB GB3651767A patent/GB1170299A/en not_active Expired
- 1967-08-09 CS CS573867A patent/CS158612B2/cs unknown
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4366298A (en) * | 1979-07-05 | 1982-12-28 | Wacker-Chemie Gmbh | Process and heavy metal catalyst for the polymerization of α-olefins, particularly polyethylene |
US4363902A (en) * | 1980-03-17 | 1982-12-14 | Wacker-Chemie Gmbh | Process and heavy metal catalyst for the polymerization of α-olefins, particularly polyethylene |
US4935474A (en) * | 1983-06-06 | 1990-06-19 | Exxon Research & Engineering Company | Process and catalyst for producing polyethylene having a broad molecular weight distribution |
EP0134100A1 (en) * | 1983-08-31 | 1985-03-13 | Exxon Research And Engineering Company | Cocatalyst for use with a transition metal compound in polyethylene production |
WO2005100414A1 (en) * | 2004-04-07 | 2005-10-27 | Union Carbide Chemicals & Plastics Technology Corporation | Method of controlling olefin polymerization |
US7601783B2 (en) | 2004-04-07 | 2009-10-13 | Dow Global Technologies, Inc. | Method of controlling olefin polymerization |
AU2005233566B2 (en) * | 2004-04-07 | 2011-01-06 | Union Carbide Chemicals & Plastics Technology Llc | Method of controlling olefin polymerization |
Also Published As
Publication number | Publication date |
---|---|
SE339997B (en) | 1971-11-01 |
CS158612B2 (en) | 1974-11-25 |
DE1595665A1 (en) | 1970-04-30 |
NL154751B (en) | 1977-10-17 |
DE1595665C3 (en) | 1975-08-14 |
FI46852B (en) | 1973-04-02 |
NL6710898A (en) | 1968-02-12 |
BE702472A (en) | 1968-02-09 |
ES343723A1 (en) | 1968-12-01 |
DE1595665B2 (en) | 1974-12-19 |
NO125681B (en) | 1972-10-16 |
FI46852C (en) | 1973-07-10 |
AT278348B (en) | 1970-01-26 |
YU31351B (en) | 1973-04-30 |
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