Random copolymer containing derivative of bicyclo [2.2.1] hept-2-ene compound

• US 4,931,520 A
• Filed: 01/17/1989
• Issued: 06/05/1990
• Est. Priority Date: 01/20/1988
• Status: Expired due to Fees

• Current Assignee: Nippon Oil Corporation (ENEOS Holdings, Inc.)
• Original Assignee: Nippon Oil Corporation (ENEOS Holdings, Inc.)
• Inventors: Ozawa, Hiroyuki, Yamanashi, Teruaki, Yuasa, Hitoshi, Satoh, Tetsuo, Matsuno, Mitsuo
• Primary Examiner(s): Schofer, Joseph L.
• Assistant Examiner(s): Teskin, F. M.
• Application Number:
  US07/298,180
• Time in Patent Office: 504 Days
• Field of Search: 526/169.2, 526/280, 526/281, 526/308, 526/75
• US Class Current: 526/281
• CPC Class Codes: C08F 210/02 Ethene
• CPC Class Codes: C08F 4/68 Vanadium, niobium, tantalum or compounds thereof

Abstract

A random copolymer comprises recurring units each having the formula of; ##STR1## wherein R¹ to R¹⁰ stand for a hydrogen atom or an alkyl group with or without R⁵ being bonded to R⁶ or R¹⁰ via an alkylene group having 1 to 3 carbon atoms. The random copolymer contains 50 to 90 mol % of ethylene. The random copolymer has an intrinsic viscosity [η] of 0.3 to 10 dl/g measured in Decalin®, i.e., decahydronphthalene at 30° C.

Claims

1. A random copolymer comprising:

(a) recurring units each having the formula of;

##STR8## wherein R¹ to R¹⁰ each represent the same or different atoms or groups and stand for a hydrogen atom or an alkyl group with or without R⁵ being bonded to R⁶ or R¹⁰ via an alkylene group having 1 to 3 carbon atoms,

(b) said random copolymer being obtained by copolymerizing ethylene with a feed monomer material comprising a 5-aryl-bicyclo [2.2.1] hept-2-ene compound represented by the formula of;

##STR9## wherein R¹ to R¹⁰ are the same as above, (c) said random copolymer containing 50 to 90 mol % of ethylene,

(d) said random copolymer having an intrinsic viscosity [η

] of 0.3 to 10 dl/g measured in decahydronophthalene at 30°

C., and

(e) said random copolymer having a glass transition temperature (Tg) of 80°

to 220°

C. measured by a thermomechanical analyzer.

2. The random copolymer according to claim 1 wherein said 5-aryl-bicyclo [2. 2. 1] hept-2-ene compound is selected from the group consisting of 5-phenyl-bicyclo [2. 2. 1] hept-2-ene, 5-o-tolyl-bicyclo [2. 2. 1] hept-2-ene, 5-m-tolyl-bicyclo [2. 2. 1] hept-2-ene, 5-p-tolyl-bicyclo [2. 2. 1] hept-2-ene, 5-o-ethylphenyl-bicyclo [2. 2. 1] hept-2-ene, 5-m-ethylphenyl-bicyclo [2. 2. 1] hept-2-ene, 5-p-ethylphenyl-bicyclo [2. 2. 1] hept-2-ene, 5-p-isopropylphenyl-bicyclo [2. 2. 1] hept-2-ene, 1, 4-methano-1, 4, 4a, 9a-tetrahydrofluorene and mixtures thereof.

3. The random copolymer according to claim 1 further comprising not more than 10 mol %, based on mole of the 5-aryl-bicyclo [2. 2. 1] hept-2-ene compound, of a comonomer selected from the group consisting of α

-olefins having not less than 3 carbon atoms, aromatic olefins, bicycloheptenes and mixtures thereof.

4. The random copolymer according to claim 3 wherein said comonomer is selected from the group consisting of propylene, 1-butene, 3-methyl-1-butene, 1-pentene, 1-hexene, 1-decene, styrene, α

-methylstyrene, bicycloheptene, methylbicycloheptane, ethylbicycloheptane, 2, 3, 3a, 4, 7, 7a-hexahydro-4, 7-methano-1H-indene, 5-ethylidenebicyclo [2. 2. 1] hept-2-ene, and mixtures thereof.

5. The random copolymer according to claim 1 having a degree of crystallinity measured by X rays of not more than 5% and exhibiting no melting point measured by a differential scanning calorimeter.

6. A method for preparing a random copolymer comprising copolymerizing ethylene and a 5-aryl-bicyclo [2. 2. 1] hept-2-ene compound represented by the formula of;

##STR10## wherein R¹ to R¹⁰ each represent the same or different atoms or groups and stand for a hydrogen atom or an alkyl group with or without R⁵ being bonded to R⁶ or R¹⁰ via an alkylene group having 1 to 3 carbon atoms, in a hydrocarbon solvent and in the presence of a catalyst containing an organoaluminum compound and a vanadium compound soluble in the hydrocarbon solvent.

7. The method according to claim 6 wherein said vanadium compound is selected from the group consisting of VCl₄, VBr₄, VOCl₃, VOBr₃ and VO(OR)₃, R indicating a hydrocarbon group having 1 to 20 carbon atoms, VO(OR)_n X_3-n, R indicating a hydrocarbon group having 1 to 20 carbon atoms, X indicating a halogen and 0≦

n<

3, and mixtures thereof.

8. The method according to claim 6 wherein said organoaluminum compound has the formula of R'"'"'_m AlX'"'"'_3-m, R'"'"' indicating an aliphatic or alicyclic hydrocarbon residue having 1 to 20 carbon atoms, X'"'"' indicating a halogen and 0<

m≦

3.

9. The method according to claim 8 wherein said organoaluminum compound is selected from the group consisting of trimethyl aluminum, triethyl aluminum, triisobutyl aluminum, tricyclohexyl aluminum, diethyl aluminum chloride, diethyl aluminum bromide, diethyl aluminum iodide, ethyl aluminum dichloride, ethyl aluminum dibromide, ethyl aluminum diiodide, ethyl aluminum sesquichloride, ethyl aluminum sesquibromide, ethyl aluminum sesquiiodide and mixtures thereof.

10. The method according to claim 6 wherein the molar ratio of the organoaluminum compound to the vanadium compound is in the range of 1:

2 to 30.

11. The method according to claim 6 wherein the concentration of said vanadium compound in the hydrocarbon solvent ranges from 0.1 to 20 millimol/liter.

12. The method according to claim 6 wherein the concentration of said 5-aryl-bicyclo [2. 2. 1] hept-2-ene compound in the hydrocarbon solvent ranges from 0.05 to 4 mol/liter.

13. The method according to claim 12 wherein the concentration of ethylene is 0.01 to 1 time that of the 5-aryl-bicyclo [2. 2. 1] hept-2-ene compound.

14. The method according to claim 6 wherein said hydrocarbon solvent is selected from the group consisting of hexane, heptane, octane, cyclohexane, benzene, toluene, xylene and mixtures thereof.

15. The method according to claim 6 wherein the copolymerization is carried out at a temperature of -30°

C. to 80°

C. and under a pressure of 0.1 to 50 kg/cm² in terms of absolute pressure.