# US 4,396,747 A · Zirconium-titanium catalyzed olefin polymerization

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- Number: US 4,396,747 A
- Document ID: US4396747A
- Status: Granted
- Kind: A
- Application number: 06/266,690
- Filed: 1981-05-22
- Granted: 1983-08-02
- Earliest claimed: 1981-05-22
- Assignees: Phillips Petroleum Company
- Inventors: Melvin B. Welch; Richard E. Dietz
- Web page: https://patentgrep.com/patent/US4396747A

## CPC

- C08F 10/02: Ethene
- C08F: MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS

## Abstract

Olefins such as ethylene can be polymerized in high productivities using a catalyst system wherein one catalyst component comprises a precipitated complex of zirconium tetrahydrocarbyloxide and/or titanium tetrahydrocarbyloxide and dihydrocarbylmagnesium. The productivity of the preferred catalyst containing both zirconium and titanium has been found to be substantially higher than the productivity of those catalysts obtained from either only Zr(OR').sub.4 or only Ti(OR").sub.4 and second catalyst component comprises at least one organometallic compound of a metal selected from the Groups I-III of the Mendeleev Periodic Table.

## Claims

### Claim 1

Process for polymerizing olefin comprising contacting said olefin under polymerization conditions with a catalyst comprising components A and B wherein component A is a precipitate produced by mixing a solution of a product in a solvent with a titanium tetrahalide, said product being obtained by reacting the following components:
(a) Zr(OR').sub.4 and Ti(OR").sub.4
(b) MgR.sub.2 "'
wherein R', and R" and R'" are hydrocarbyl radicals of 1 to about 20 carbon atoms and wherein component B is a cocatalyst of one or more organometallic compounds of at least one metal of Groups I, II, or III of the Mendeleev Periodic Table.

### Claim 2 (depends on 1)

Process of claim 1 wherein said contacting is carried out in a hydrocarbon diluent and wherein said polymerization conditions comprise a pressure high enough to keep the olefin and the diluent substantially in the liquid phase.

### Claim 3 (depends on 1, 2)

Process of claim 1 or 2 wherein said olefin is selected from the group consisting of ethylene and mono-1-olefins having 3-10 carbon atoms.

### Claim 4 (depends on 1)

Process in accordance with claim 1 wherein said precipitate is separated from said solution and washed.

### Claim 5 (depends on 4)

Process in accordance with claim 4 wherein said precipitate is washed with a hydrocarbon solvent in which the titanium tetrahalide is soluble.

### Claim 6 (depends on 1, 4, 5)

Process in accordance with one of the claims 1, 4 or 5 wherein said titanium tetrahalide is titanium tetrachloride.