US4710554A
Expired / Lapsed
US
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Polybutadiene and process for preparing the same
Assignee: Sumitomo Chemical Co Ltd
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Filing: 1986-02-14
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Granted: 1987-12-01
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Expires: 2006-02-14
Abstract
Abstract A polybutadiene having an average 1,2-bond content of 18 to 32% by mole, a branched polymer chain content of 60% by weight or more and a Mooney viscosity at 100 DEG C. of 40 to 90, the viscosity of a 5% by weight concentration solution of this polybutadiene in styrene at 25 DEG C. being 60 to 90 cps, and a process for preparing the polybutadiene comprising starting the polymerization of 1,3-butadiene in an inert hydrocarbon solvent in the presence of a Lewis basic compound and an organolithium compound, the latter compound being in an amount of 0.5 to 3 millimoles per 100 g of 1,3-butadiene, at a temperature selected from the range of 30 DEG to 80 DEG C., carrying out the polymerization by controlling the temperature so that the temperature at the end of polymerization may be 5 DEG to 40 DEG higher than the temperature at the start of polymerization, and adding to the resulting polymer solution a polyfunctional halogen compound in an amount of 0.6 to 1 equivalent per equivalent of the organolithium compound to further react the polymer with the polyfunctional halogen compound.
Inventors
- 👤 Akio Imai
- 👤 Yasushi Okamoto
- 👤 Masatoshi Saito
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 04:12
CPC Classifications
C; C08; C08F; C08F136/00; C08F136/02; C08F136/04; C08F136/06
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
181 words
A process for producing a polybutadiene having branched polymer chains, said polybutadiene having an average 1,2-bond content of 18 to 32% by mole, a branched polymer chain content of 60% by weight or more and a Mooney viscosity at 100° C. of 40 to 90, the viscosity of a 5% by weight concentration solution of the polybutadiene in styrene at 25° C. being 60 to 90 cps, said process comprising starting the polymerization of 1,3-butadiene in an inert hydrocarbon solvent in the presence of a Lewis basic compound and an organomonolithium compound in an amount of 0.5 to 3 millimoles per 100 g of 1,3-butadiene at a temperature selected from the range of 30° to 40° C., conducting the polymerization while controlling the temperature so that the temperature at the end of the polymerization may be 20° to 40° C. higher than the temperature at the start of the polymerization, and adding to the resulting polymer solution of a polyfunctional halogen compound in an amount of 0.6 to 1 equivalent per equivalent of the organomonolithium compound to effect further reaction thereof.
Claim 2
Dependent Claim
181 words
A process for producing a polybutadiene having branched polymer chains, said polybutadiene having an average 1,2-bond content of 18 to 32% by mole, a branched polymer chain content of 60% by weight or more and a Mooney viscosity at 100° C. of 40 to 90, the viscosity of a 5% by weight concentration solution of the polybutadiene in styrene at 25° C. being 60 to 90 cps, said process comprising starting the polymerization of 1,3-butadiene in an inert hydrocarbon solvent in the presence of a Lewis basic compound and an organomonolithium compound in an amount of 0.5 to 3 millimoles per 100 g of 1,3-butadiene at a temperature selected from the range of 30° to 40° C., conducting the polymerization while controlling the temperature so that the temperature at the end of the polymerization may be 20° to 40° C. higher than the temperature at the start of the polymerization, and adding to the resulting polymer solution of a polyfunctional halogen compound in an amount of 0.6 to 1 equivalent per equivalent of the organomonolithium compound to effect further reaction thereof.
Claim 3
Dependent Claim
56 words
A process according to claim 1, wherein the Lewis basic compound is an ether selected from the group consisting of diethyl ether, dibutyl ether, tetrahydrofuran, ethylene glycol dimethyl ether, ethylene glycol dibutyl ether, diethylene glycol dimethyl ether and diethylene glycol dibutyl ether and a tertiary amine selected from the group consisting of triethylamine, tributylamine and N,N,N',N'-tetramethylethylenediamine.
Claim 4
Dependent Claim
16 words
A process according to claim 2, wherein the Lewis basic compound is diethylene glycol dimethyl ether.
Claim 5
Dependent Claim
29 words
A process according to claim 1, wherein the organomonolithium compound is a hydrocarbon compound containing lithium selected from the group consisting of n-propyl-lithium, isopropyllithium, n-butyllithium, sec-butyllithium, t-butyllithium, and n-pentyllithium.
Claim 6
Dependent Claim
29 words
A process according to claim 2, wherein the organomonolithium compound is a hydrocarbon compound containing lithium selected from the group consisting of n-propyl-lithium, isopropyllithium, n-butyllithium, sec-butyllithium, t-butyllithium, and n-pentyllithium.
Claim 7
Dependent Claim
12 words
A process according to claim 4, wherein the organomonolithium compound is n-butyllithium.
Claim 8
Dependent Claim
12 words
A process according to claim 5, wherein the organomonolithium compound is n-butyllithium.
Claim 9
Dependent Claim
29 words
A process according to claim 1, wherein the polyfunctional halogen compound is selected from the group consisting of dimethylsilicon dichloride, monomethylsilicon trichloride, silicon tetrachloride, tin tetrachloride and germanium tetrachloride.
Claim 10
Dependent Claim
30 words
A process according to claim 2, wherein the polyfunctional halogen compound is selected from the group consisting of dimethylsilicon dichloride , monomethylsilicon trichloride, silicon tetrachloride, tin tetrachloride and germanium tetrachloride.
Claim 11
Dependent Claim
14 words
A process according to claim 8, wherein the polyfunctional halogen compound is tin tetrachloride.
Claim 12
Dependent Claim
14 words
A process according to claim 9, wherein the polyfunctional halogen compound is tin tetrachloride.
Claim 13
Dependent Claim
29 words
A process according to claim 4, wherein the polyfunctional halogen compound is selected from the group consisting of dimethylsilicon dichloride, monomethylsilicon trichloride, silicon tetrachloride, tin tetrachloride and germanium tetrachloride.
Claim 14
Dependent Claim
29 words
A process according to claim 5, wherein the polyfunctional halogen compound is selected from the group consisting of dimethylsilicon dichloride, monomethylsilicon trichloride, silicon tetrachloride, tin tetrachloride and germanium tetrachloride.
Claim 15
Dependent Claim
14 words
A process according to claim 12, wherein the polyfunctional halogen compound is tin tetrachloride.
Claim 16
Dependent Claim
14 words
A process according to claim 13, wherein the polyfunctional halogen compound is tin tetrachloride.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-11-30 | 1991-06-01 | 1991-12-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-11-30 | 1995-06-01 | 1995-12-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-11-30 | 1999-06-01 | 1999-12-01 | $7700.00 | Window Closed / Lapsed |