Claims
- 1. A polymer having terminal halogen atoms, which polymer is produced by cationically polymerizing an olefinic monomer in the presence of an initiator system comprising a halogen-containing Lewis acid and a dihydrofuran derivative selected from the group consisting of a 2,2,5,5-tetramethyldihydrofuran, 2,2,5,5-tetraethyldihydrofuran and mixtures thereof.
- 2. A polymer as defined in claim 1, wherein the halogen-containing Lewis acid is a halide of boron, tin, aluminum, titanium, antimony or iron.
- 3. A polymer as defined in claim 1, wherein boron trichloride is used as the halogen-containing Lewis acid.
- 4. A polymer as defined in claim 1, wherein the cationic polymerization is carried out at a temperature of from -130.degree. C. to 30.degree. C.
- 5. A polymer as defined in claim 1, wherein the concentration of said dihydrofuran derivative present in the process is from 10.sup.-8 to 10.sup.-1 mole per mole of the monomer used, and the Lewis acid is present in a molar ratio of from 1:1 to 200:1 based on said dihydrofuran derivative.
- 6. A polymer as defined in claim 1, wherein isobutene is used as the cationically polymerizable monomer.
- 7. A process for preparing a polymer having terminal halogen atoms which comprises: cationically polymerizing a monomer in the presence of an initiator system which includes a halogen-containing Lewis acid and a dihydrofuran derivative selected from the group consisting of 2,2,5,5-tetramethyldihydrofuran, 2,2,5,5-tetraethyldihydrofuran and mixtures thereof.
- 8. The process of claim 7, wherein the halogen-containing Lewis acid is a halide of boron, tin, aluminum, titanium, antimony or iron.
- 9. The process of claim 7, wherein boron trichloride is used as the halogen-containing Lewis acid.
- 10. The process of claim 7, wherein the polymerization is carried out at a temperature of from -130.degree. C. to +30.degree. C.
- 11. The process of claim 7, wherein said dihydrofuran derivative is present during the polymerization in a concentration of from 10.sup.-6 to 10.sup.-1 mole per mole of the monomer used, and the Lewis acid is present in a molar ratio of from 1:1 to 200:1 based on said dihydrofuran derivative.
- 12. The process of claim 7, wherein isobutene is used as the cationically polymerizable monomer.
Priority Claims (1)
Number |
Date |
Country |
Kind |
3833818 |
Oct 1988 |
DEX |
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Parent Case Info
This application is a continuation of application Ser. No. 409,583, filed on Sep. 19, 1989 now abandoned.
US Referenced Citations (3)
Foreign Referenced Citations (3)
Number |
Date |
Country |
0206756 |
Dec 1986 |
EPX |
0265053 |
Apr 1988 |
EPX |
0083241 |
Jul 1971 |
DDX |
Non-Patent Literature Citations (1)
Entry |
Polymer Bulletin 17, 7-13 (1987), Living Carbocationic Polymerization Kennedy et al. |
Continuations (1)
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Number |
Date |
Country |
Parent |
409583 |
Sep 1989 |
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