US4480075A
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Block copolymers of Ziegler-Natta polymerized and anionically polymerized monomers
Assignee: Shell USA Inc
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Filing: 1983-06-24
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Granted: 1984-10-30
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Expires: 2003-06-24
Abstract
Abstract Block copolymers are prepared by using two successive and different catalytic processes, a Ziegler-Natta type polymerization followed by a conventional anionic polymerization.
Inventors
- 👤 Carl L. Willis
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 16:10
CPC Classifications
C; C08; C08F; C08F297/00; C08F295/00
Claims Analysis
Total Claims: 36
Claim 1
Independent Claim
101 words
A process for preparing living multi-block copolymers comprising; (a) combining under polymerization conditions one or more alpha olefin monomers in a suitable diluent in the presence of a Ziegler-Natta catalyst system and a transmetallation reagent selected from the group consisting of dialkyl zinc, dialkyl cadmium, tetralkyl lead, and their salts, (b) contacting the resulting polymer with an anionic transfer reagent generating an anionic polymerization initiator thereby forming living polymer chains, (c) contacting the resulting living polymer chains sequentially with one or more monomers selected from the group consisting of conjugated dienes, and monoalkenylarenes and activated mono olefins; (d) recovering multi-block copolymers.
Claim 2
Dependent Claim
101 words
A process for preparing living multi-block copolymers comprising; (a) combining under polymerization conditions one or more alpha olefin monomers in a suitable diluent in the presence of a Ziegler-Natta catalyst system and a transmetallation reagent selected from the group consisting of dialkyl zinc, dialkyl cadmium, tetralkyl lead, and their salts, (b) contacting the resulting polymer with an anionic transfer reagent generating an anionic polymerization initiator thereby forming living polymer chains, (c) contacting the resulting living polymer chains sequentially with one or more monomers selected from the group consisting of conjugated dienes, and monoalkenylarenes and activated mono olefins; (d) recovering multi-block copolymers.
Claim 3
Dependent Claim
115 words
A process for preparing block copolymers comprising: (a) combining under polymerization conditions one or more alpha-olefin, monomers, a Ziegler-Natta catalyst, a transmetallation reagent in a suitable diluent; (b) contacting the resulting polymer with an anionic polymerization transfer reagent selected from the group consisting of MeOLi, EtOLi, PrOLi, BuOLi, hexyl and octyl alkoxides of lithium, thereby forming living polymer chains; (c) contacting the resulting living polymer chains sequentially with one or more monomers selected from the groups consisting conjugated dienes monoalkenylarenes and activated monoolefins thereby forming living multi block copolymers; (d) contacting the resulting living multi block copolymers with a coupling agent having a functionality of two or more; and (e) recovering the resulting block copolymer.
Claim 4
Dependent Claim
115 words
A process for preparing block copolymers comprising: (a) combining under polymerization conditions one or more alpha-olefin, monomers, a Ziegler-Natta catalyst, a transmetallation reagent in a suitable diluent; (b) contacting the resulting polymer with an anionic polymerization transfer reagent selected from the group consisting of MeOLi, EtOLi, PrOLi, BuOLi, hexyl and octyl alkoxides of lithium, thereby forming living polymer chains; (c) contacting the resulting living polymer chains sequentially with one or more monomers selected from the groups consisting conjugated dienes monoalkenylarenes and activated monoolefins thereby forming living multi block copolymers; (d) contacting the resulting living multi block copolymers with a coupling agent having a functionality of two or more; and (e) recovering the resulting block copolymer.
Claim 5
Dependent Claim
17 words
The process according to claim 1 wherein said alpha-olefin monomer is ethylene, propylene, 1-butene or a mixture.
Claim 6
Dependent Claim
27 words
The process according to claim 1 wherein said hydrocarbon diluent is n-hexane, n-heptane, cyclohexane, cyclopentane, benzene, toluene, one or more xylenes, 2,2,4-trimethylpentane, or mixture, or monomers themselves.
Claim 7
Dependent Claim
14 words
The process of claim 1 wherein the Ziegler-Natta catalyst is an organo-aluminum/TiCl 3 catlayst.
Claim 8
Dependent Claim
13 words
The process of claim 1 wherein the Ziegler-Natta catalyst is triethylaluminum/TiCl 3 .
Claim 9
Dependent Claim
14 words
The process of claim 1 wherein the Ziegler-Natta catalyst is diethylaluminum chloride/TiCl 3 .
Claim 10
Dependent Claim
22 words
The process of claim 1 wherein the Ziegler-Natta catalyst is present at between 0.3 and 30 millimoles per hundred grams of monomer.
Claim 11
Dependent Claim
12 words
The process of claim 1 wherein the transmetallation reagent is diethyl zinc.
Claim 12
Dependent Claim
40 words
The process of claim 1 wherein the Ziegler-Natta polymerization takes place at a temperature between about 30° C. and about 80° C., a pressure sufficient to maintain the mixture substantially liquid and continues for between 15 minutes and 8 hours.
Claim 13
Dependent Claim
24 words
The process according to claim 1 wherein said transfer agent is n-butyllithium, sec-butyllithium, n-decyllithium, phenyllithium, 1-naphthyllithium, p-tolyllithium, cyclohexllithium, eicosyllithium or their alkoxides or mixture.
Claim 14
Dependent Claim
20 words
The process according to claim 1 wherein said conjugated diene is 1,3-butadiene, isoprene, 2,3-dimethyl-1,3-butadiene, 2-methyl-1,3-pentadiene, 2,3-dimethyl-1,3-pentadiene, 2-methyl-3-ethyl-1,3-pentadiene, 2-methyl-1,3-butadiene or mixture.
Claim 15
Dependent Claim
12 words
The process of claim 1 wherein the monoalkylarene is styrene or alkylstyrene.
Claim 16
Dependent Claim
25 words
The process of claim 1 wherein the anionic polymerization takes place at between 20° C. and 120° C. for between 2 minutes and 8 hours.
Claim 17
Dependent Claim
26 words
The process according to claim 1 wherein said polymerization admixture, after polymerization of said conjugated diene monomer is treated with a lower alcohol, acid, or water.
Claim 18
Dependent Claim
17 words
The process according to claim 2 wherein said alpha-olefin monomer is ethylene, propylene, 1-butene or a mixture.
Claim 19
Dependent Claim
26 words
The process according to claim 2 wherein said hydrocarbon diluent is n-hexane, n-heptane, cyclohexane, cyclopentane, benzene, toluene, one or more xylenes, 2,2,4-trimethylpentane, or mixture or monomer.
Claim 20
Dependent Claim
14 words
The process of claim 2 wherein the Ziegler-Natta catalyst is an organo-aluminum/TiCl 3 catlayst.
Claim 21
Dependent Claim
13 words
The process of claim 2 wherein the Ziegler-Natta catalyst is triethylaluminum/TiCl 3 .
Claim 22
Dependent Claim
16 words
The process according to claim 2 wherein said hydrocarbon diluent is Et 2 AlCl/TiCl 3 .
Claim 23
Dependent Claim
22 words
The process of claim 2 wherein the Ziegler-Natta catalyst is present at between 0.3 and 30 millimoles per hundred grams of monomer.
Claim 24
Dependent Claim
12 words
The process of claim 2 wherein the transmetallation reagent is diethyl zinc.
Claim 25
Dependent Claim
40 words
The process of claim 2 wherein the Ziegler-Natta polymerization takes place at a temperature between about 30° C. and about 80° C., a pressure sufficient to maintain the mixture substantially slurry and continues for between 15 minutes and 8 hours.
Claim 26
Dependent Claim
23 words
The process according to claim 2 wherein said initiator is n-butyllithium, sec-butyllithium, n-decyllithium, phenyllithium, 1-naphthyllithium, p-tolyllithium, cyclohexllithium, eicosyllithium or their alkoxides or mixture.
Claim 27
Dependent Claim
20 words
The process according to claim 2 wherein said conjugated diene is 1,3-butadiene, isopresne, 2,3-dimethyl-1,3-butadiene, 2-methyl-1,3-pentadiene, 2,3-dimethyl-1,3-pentadiene, 2-methyl-3-ethyl-1,3-pentadiene, 2-methyl-1,3-butadiene or mixture.
Claim 28
Dependent Claim
12 words
The process of claim 2 wherein the monoalkylarene is styrene or alklystyrene.
Claim 29
Dependent Claim
25 words
The process of claim 2 wherein the anionic polymerization takes place at between 30° C. and 120° C. for between 2 minutes and 8 hours.
Claim 30
Dependent Claim
30 words
The process according to claim 2 wherein said coupling agent is present in the range of about 0.5 to 10 equivalents per equivalent of lithium, thereby preparing a coupled polymer.
Claim 31
Dependent Claim
36 words
The process according to claim 2 wherein said coupling agent is a polyepoxide, polyisocyanate, polyamine, polyaldehyde, polyketone, polyanhydride, polyester, polyhalide, polyvinyl aromatic, carbon dioxide, or monoester, wherein the functionality of said agent is at least 2.
Claim 32
Dependent Claim
36 words
The process according to claim 2 employing 1-butene as said alpha-olefin monomer, heptane as said diluent, n-butyllithium as said hydrocarbon monolithium initiator, 1,3-butadiene as said conjugated diene; and wherein coupling is by treatment with silicon tetrahalide.
Claim 33
Dependent Claim
13 words
The process according to claim 2 employing silicon tetrachloride as said silicon tetrahalide.
Claim 34
Dependent Claim
11 words
The block copolymer product produced by the process of claim 1.
Claim 35
Dependent Claim
11 words
The block copolymer product produced by the process of claim 2.
Claim 36
Dependent Claim
12 words
The end-capped block copolymer product produced by the process of claim 1.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-10-30 | 1988-04-30 | 1988-10-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-10-30 | 1992-04-30 | 1992-10-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-10-30 | 1996-04-30 | 1996-10-30 | $7700.00 | Window Closed / Lapsed |