US4704433A
Expired / Lapsed
US
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Block copolymer containing a methacrylate ester block
Assignee: Tonen General Sekiyu KK
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Filing: 1985-05-24
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Granted: 1987-11-03
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Expires: 2005-05-24
Abstract
Abstract A novel block copolymer is disclosed which includes a random ethylene-propylene copolymer segment (A) and a methacrylate segment (B). The block copolymer has a number-average molecular weight of about 1,000 to about 600,000 and a ratio of (A) to (B) of 15/85 to 97/3 by weight.
Inventors
- 👤 Satoshi Ueki
- 👤 Chihiro Imai
- 👤 Tokuo Makishima, deceased
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 21:27
CPC Classifications
C; C08; C08F; C08F297/00; C08F297/06
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
376 words
A process for producing a block copolymer having a number-average molecular weight of about 1,000 to about 600,000 in which a random copolymer segment (A) is bonded to a polymer segment (B), with the ratio of (A) to (B) being 15/85 to 97/3 by weight, said random copolymer segment (A) being composed of the constitutional units represented by the formulas I and II below ##STR6## wherein the amount of I in said segment (A) is from 30 to 80 wt% and the amount of II in said segment (A) is from 70 to 20 wt%, and said polymer segment (B) being composed of the constitutional units represented by the formula ##STR7## wherein R is hydrocarbyl of from 1 to 20 carbon atoms, said process comprising the steps of: (a) performing living polymerization of ethylene and propylene at a temperature of less than -50° C. in the presence of a catalyst comprising (i) a beta-diketone vanadium chelate of the formula ##STR8## wherein R 1 and R 2 are the same or different and are each alkyl or aryl, and (ii) an organoaluminum compound of the formula R 2 AlX, wherein R is an alkyl group of 1 to 8 carbon atoms and X is a halogen atom, to provide a living ethylene-propylene random copolymer having an ethylene-to-propylene ratio of from 30/70 to 80/20 by weight, said vanadium chelate being used in an amount of from 1×10 -4 to 0.01 mol per 1 mol of said ethylene and propylene, said organoaluminum compound being used in an amount of from about 1×10 -3 to 0.1 mol per 1 mol of said ethylene and propylene, and said organoaluminum compound being used in an amount of from 5 to 25 mol per 1 mol of said vanadium chelate; (b) reacting said ethylene-propylene copolymer with a halogen selected from the chlorine, bromine and iodine to provide an ethylene-propylene random copolymer having halogenated terminal groups, said halogen being employed in an amount of from 2 to 5 moles per mole of said organoaluminum compound; (c) contacting said halogenated copolymer produced in step (b) with metallic magnesium; and (d) polymerizing the product of step (c) with a methacrylate ester of the formula ##STR9## wherein R is as defined above, to form said block copolymer.
Claim 2
Dependent Claim
376 words
A process for producing a block copolymer having a number-average molecular weight of about 1,000 to about 600,000 in which a random copolymer segment (A) is bonded to a polymer segment (B), with the ratio of (A) to (B) being 15/85 to 97/3 by weight, said random copolymer segment (A) being composed of the constitutional units represented by the formulas I and II below ##STR6## wherein the amount of I in said segment (A) is from 30 to 80 wt% and the amount of II in said segment (A) is from 70 to 20 wt%, and said polymer segment (B) being composed of the constitutional units represented by the formula ##STR7## wherein R is hydrocarbyl of from 1 to 20 carbon atoms, said process comprising the steps of: (a) performing living polymerization of ethylene and propylene at a temperature of less than -50° C. in the presence of a catalyst comprising (i) a beta-diketone vanadium chelate of the formula ##STR8## wherein R 1 and R 2 are the same or different and are each alkyl or aryl, and (ii) an organoaluminum compound of the formula R 2 AlX, wherein R is an alkyl group of 1 to 8 carbon atoms and X is a halogen atom, to provide a living ethylene-propylene random copolymer having an ethylene-to-propylene ratio of from 30/70 to 80/20 by weight, said vanadium chelate being used in an amount of from 1×10 -4 to 0.01 mol per 1 mol of said ethylene and propylene, said organoaluminum compound being used in an amount of from about 1×10 -3 to 0.1 mol per 1 mol of said ethylene and propylene, and said organoaluminum compound being used in an amount of from 5 to 25 mol per 1 mol of said vanadium chelate; (b) reacting said ethylene-propylene copolymer with a halogen selected from the chlorine, bromine and iodine to provide an ethylene-propylene random copolymer having halogenated terminal groups, said halogen being employed in an amount of from 2 to 5 moles per mole of said organoaluminum compound; (c) contacting said halogenated copolymer produced in step (b) with metallic magnesium; and (d) polymerizing the product of step (c) with a methacrylate ester of the formula ##STR9## wherein R is as defined above, to form said block copolymer.
Claim 3
Dependent Claim
28 words
The process of claim 1 wherein said vanadium chelate comprises a member selected from the group consisting of V(acetylacetonate) 3 , V(benzoylacetylacetonate) 3 , and V(dibenzoylmethanate) 3 .
Claim 4
Dependent Claim
27 words
The process of claim 1 wherein said organoaluminum compound comprises a member selected from the group consisting of dimethylaluminum chloride, diethylaluminum chloride, diethylaluminum bromide, and diisobutylaluminum chloride.
Claim 5
Dependent Claim
18 words
The process according to claim 1 wherein said step (a) polymerization temperature is at -65° C. or below.
Claim 6
Dependent Claim
54 words
The process of claim 1 wherein said halogenated copolymer and said metallic magnesium are contacted in the presence of tetrahydrofuran or diethylether solvent under reflux for 1 to 10 hours and wherein from about 0.001 to 0.1 part by weight of said metallic magnesium is employed per part by weight of said halogenated copolymer.
Claim 7
Dependent Claim
22 words
The process according to claim 5 wherein said polymerization step (d) is performed at a temperature of from -50° to -100° C.
References Cited (Backward Citations)
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| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
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| 3.5 Years (Year 4) | 1990-11-02 | 1991-05-04 | 1991-11-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-11-02 | 1995-05-04 | 1995-11-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-11-02 | 1999-05-04 | 1999-11-03 | $7700.00 | Window Closed / Lapsed |