# US 5,349,034 A · Process for selective production of trans-1,4-polybutadiene

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- Number: US 5,349,034 A
- Document ID: US5349034A
- Status: Granted
- Kind: A
- Application number: 08/095,050
- Filed: 1993-07-22
- Granted: 1994-09-20
- Earliest claimed: 1989-12-18
- Assignees: Sumitomo Chemical Company, Limited
- Inventors: Masahiro Kakugo; Tatsuya Miyatake; Koozi Mizunuma; Yoshio Yagi; Kazuhiro Watanabe
- Web page: https://patentgrep.com/patent/US5349034A

## CPC

- C08F 136/06: Butadiene
- C08F: MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS

## Abstract

A catalyst for production of 1,4-polybutadiene which comprises as the catalyst component (A) a transition metal compound represented by the formula M(R)l(OR')m X.sub.n-(l+m), wherein M denotes a transition metal atom, R and R' each denote a hydrocarbon group of 1-20 carbon atoms, X denotes a halogen atom, and l, m and n denote numerals satisfying the equations l.gtoreq.0, m.gtoreq.0 and n-(l+m).gtoreq.0, n corresponding to the valence of the transition metal, as the catalyst component (B) an organoaluminum compound represented by the formula AlR.sup.1.sub.a X'.sub.3-a, wherein R.sup.1 denotes a hydrocarbon group of 1-20 carbon atoms, X denotes a halogen atom, and a denotes a numeral satisfying the equation 1.ltoreq.a.ltoreq.3, or an aluminoxane obtained by the reaction of said organoaluminum compound with water, and as the catalyst component (C) an organic compound having at least two hydroxyl groups.

## Claims

### Claim 1

A process for selective production of trans-1,4-polybutadiene which comprises using a catalyst system consisting essentially of:
as the catalyst component (A), a titanium compound represented by the general formula Ti(R).sub.l (OR').sub.m X.sub.4-(l+m), wherein R and R' independently denote a hydrocarbon group of 1-20 carbon atoms, X denotes a halogen atom, and l and m denote numerals satisfying the inequalities l.gtoreq.0, m.gtoreq.0 and l+m .ltoreq.4,
as the catalyst component (B), an organoaluminum compound represented by the general formula AlR.sup.1.sub.a Z.sub.3-a, wherein R.sup.1 denotes a hydrocarbon group of 1-20 carbon atoms, Z denotes a halogen atom, and a denotes a numeral satisfying the inequality l.ltoreq.a .ltoreq.3, wherein catalyst component (B) is used relative to the catalyst component (A) in the range of 1 to 100,000 in terms of the ratio of aluminum to titanium atom, and
as the catalyst component (C), all organic compound having at least two hydroxyl groups represented by the general formula V or VI ##STR7## wherein Y denotes ##STR8## R.sup.6 being hydrogen or a hydrocarbon group of 1-6 carbon atoms; R.sup.2, R.sup.3, R.sup.4 and R.sup.5 must be the same or different from one another and independently denote a hydrocarbon group of 1-20 carbon atoms, hydroxyl group, nitro group, nitrile group, hydrocarbyloxy group or halogen atom; n' denotes 0 or an integer of 1 or more and represents the number of times of repetition of the unit Y; y, y', y", z, z' and z" independently denote the number of substituents bonded to the aromatic ring, y, y', z and z' being independently 0 or an integer of from 1 to 2, y" and z" being independently 0 or an integer of from 1 to 3;
for polymerization including reacting catalyst component (C) with catalyst component (A) prior to using said system for polymerization.

### Claim 2 (depends on 1)

A process according to claim 1, wherein the catalyst component (A) is used in the range of 10.sup.-10 to 10.sup.-3 mmol/l in terms of titanium atom.

### Claim 3 (depends on 1)

A process according to claim 1, wherein the catalyst component (C) is used in a molar ratio of 0.01 to 4 relative to the titanium atom of the catalyst component (A).

### Claim 4 (depends on 1)

A process according to claim 1, including using a solvent for polymerization wherein the solvent is selected from the group consisting of butane, pentane, hexane, heptane, octane, benzene, toluene, methylene chloride and a butadiene compound of the monomer.

### Claim 5 (depends on 30)

A process according to claim 30, wherein the polymerization is carried out at a temperature of -50.degree. C. to 200.degree. C.