IPC분류정보
국가/구분 |
United States(US) Patent
등록
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국제특허분류(IPC7판) |
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출원번호 |
US-0409744
(1982-08-19)
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발명자
/ 주소 |
- Brownscombe, Thomas F.
- Willis, Carl L.
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출원인 / 주소 |
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대리인 / 주소 |
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인용정보 |
피인용 횟수 :
13 인용 특허 :
4 |
초록
▼
Completely polymerizing olefinic monomer feed, in contact with a coordination catalyst suitable for olefin polymerization, in a mold having the shape of the article, at conditions under which the polymer is produced as a coherent, useful article in the shape of the interior of the mold, and removing
Completely polymerizing olefinic monomer feed, in contact with a coordination catalyst suitable for olefin polymerization, in a mold having the shape of the article, at conditions under which the polymer is produced as a coherent, useful article in the shape of the interior of the mold, and removing the article from the mold. This method permits the production of polyolefin articles which are difficult or impossible to produce from polyolefin powder or pellets by conventional methods, such as articles of polyolefins of such high molecular weight that the polymer would not be processable by a melt process; articles containing extremely high filler loading; articles containing interconnected reinforcement; and articles from molds which require substantial flows through narrow passages.
대표청구항
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1. A method for producing an olefin polymer article which comprises substantially completely polymerizing an olefinic monomer feed selected from the group consisting of ethylene, C 3 to C 12 aliphatic and cycloaliphatic alpha monoolefins, and mixtures thereof in contact with a coordination catalyst
1. A method for producing an olefin polymer article which comprises substantially completely polymerizing an olefinic monomer feed selected from the group consisting of ethylene, C 3 to C 12 aliphatic and cycloaliphatic alpha monoolefins, and mixtures thereof in contact with a coordination catalyst in a mold having the shape of the article, at conditions under which the polymer is produced as a coherent, useful article in the shape of the interior of the mold. 2. A method for producing an olefin polymer article which comprises charging a fluid olefinic monomer feed selected from the group consisting of ethylene, C 3 to C 12 aliphatic and cycloaliphatic alpha monoolefins, and mixtures thereof under pressure, and a coordination catalyst, to a pressure-tight mold; retaining the mixture in the mold in liquid or supercritical phase at polymerization conditions conducive to formation of a cohesive mass of polymer; and supplying at least additional monomer as the polymerization proceeds until conversion of monomer to a polymer mass which fills the mold is substantially complete. 3. A method for producing an olefin polymer article which comprises filling a pressure-tight mold, which has at least one movable wall section, with a fluid olefinic monomer feed selected from the group consisting of ethylene, C 3 to C 12 aliphatic and cycloaliphatic alpha monoolefins, and mixtures thereof under pressure in liquid or supercritical phase and with a catalytic amount of a coordination catalyst, maintaining the mold at polymerization conditions while reducing the mold volume by inward movement of said movable wall section to compensate for shrinkage of the reaction mixture as polymerization proceeds, until the reaction mixture has been substantially completely converted to a coherent article in the shape of the mold, and removing the article from the mold. 4. A method for producing an olefin polymer article which comprises placing at least one constituent of a coordination catalyst in a pressure-tight mold having the shape of the article; charging a fluid monoolefinic feed selected from the group consisting of ethylene, C 3 to C 12 aliphatic and cycloaliphatic alpha monoolefins, and mixtures thereof under pressure, and any additional catalyst constituents required to produce an effective catalyst, to the mold; substantially completely polymerizing the feed at conditions under which the polymer is produced as a coherent, useful article in the shape of the interior of the mold; and removing the article from the mold. 5. The method of claims 1, 2, 3, or 4 wherein said olefinic feed is a single aliphatic α-olefin of from 2 to 16 carbon atoms per molecule. 6. The method of claims 1, 2, 3, or 4 wherein said olefinic feed is ethylene. 7. The method of claims 1, 2, 3, or 4 wherein said olefinic feed is propylene. 8. The method of claims 1, 2, 3, or 4 wherein said olefinic feed is butene-1. 9. The method of claims 1, 2, 3, or 4 wherein said olefinic feed is a mixture of at least two α-monoolefins. 10. The method according to claims 1, 2, or 3 wherein said catalyst comprises a procatalyst and a cocatalyst, and wherein said olefinic feed is at least initially charged to the mold in at least two separate streams, one of which contains the procatalyst component and the other the cocatalyst component of the catalyst, in predetermined proportions to provide an effective polymerization catalyst when combined. 11. The method according to claim 10 wherein said feed streams are combined and intensively mixed in a mixing zone upstream from the mold. 12. The method according to claim 10 wherein said catalyst components are a catalytically active titanium halide composition and an effective aluminum alkyl cocatalyst, respectively; feed and catalyst components are combined while at a first temperature in the range from 0° to 150° C.; and the reaction mixture is maintained at a second temperature in the range from 0° C. to 200° C. until the reaction is complete. 13. The method according to claim 12 wherein the olefin in said feed is propylene, and said second temperature range is from 60° to 170° C. 14. The method according to claim 13 wherein said propylene is charged in liquid phase at a temperature below 90° C. 15. The method according to claim 10 wherein the olefin in said feed is 1-butene; said catalyst components are a catalytically active titaium halide composition and an effective aluminum alkyl cocatalyst, respectively; feed and catalyst components are combined while at a first temperature in the range from 0° to 90° C.; and the reaction mixture is maintained at a second temperature in the range from 0° to 120° C. until the reaction is complete. 16. The method according to claim 15 wherein the reaction temperature does not exceed 90° C. and the article, as removed from the mold, is in crystal form I. 17. The method according to claim 12 wherein said catalyst components are, respectively, a solid composition consisting essentially of titanium chloride, magnesium chloride and an aromatic ester electron donor; and an aluminum trialkyl having 2-8 carbon atoms per alkyl group; and wherein an aromatic ester is added as selectivity control agent, either combined with the feed stream containing the cocatalyst or in as a third stream in a portion of monomer feed. 18. The method according to claims 1, 2, 3, or 4 wherein a particulate or reticulate reinforcing or filler composition is present in the mold prior to injection of the reactive feed. 19. The method according to claim 1, 2, 3, or 4 wherein a particulate reinforcing or filler composition is charged to the mold in at least one monomer feed stream. 20. The method according to claims 1, 2, 3, or 4 wherein one or more additives selected from the group consisting of antioxidants, stabilizers against actinic radiation, pigments, plasticizers, mold release agents, flame retardants and impact modifiers are present in the mold prior to addition of feed or are added in suspension as solution in a feed stream. 21. A method for producing a cellular olefin polymer article which comprises charging a fluid olefinic monomer feed selected from the group consisting of ethylene, C 3 to C 12 aliphatic and cycloaliphatic alpha monoolefins, and mixtures thereof under pressure, and a coordination catalyst, to a pressure-tight mold; retaining the mixture in the mold in liquid phase at polymerization conditions conducive to formation of a cohesive mass of polymer; supplying at least additional monomer as the polymerization proceeds until conversion of monomer to a polymer mass which fills the mold is partially complete, quickly reducing pressure in the mold to cover the liquid polymer to foam, and containing polymerization in the mold to substantial completion. 22. The method according to claim 21 wherein a finely divided foam nucleating solid is placed in the mold prior to introduction of feed. 23. The method according to claim 21 wherein a finely divided foam nucleating solid is present in the feed charged to the mold.
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