US4346193A
Expired / Lapsed
US
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Continuous process for making star-block copolymers
Assignee: Lyondell Chemical Technology LP
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Filing: 1981-05-04
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Granted: 1982-08-24
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Expires: 2001-05-04
Abstract
Abstract A continuous anionic solution process for preparing star-block copolymers of monovinylaromatic compounds and conjugated dienes having either monomodal or bimodal arm structure is described. The process utilizes a continuous tubular reactor made up of a sequence of four static mixer zones followed by a pressure control valve.
Inventors
- 👤 David R. Warfel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 12:40
CPC Classifications
C; C08; C08F; C08F297/00; C08F297/02; C08F297/04; C08F297/044; C08G; C08G81/00; C08G81/02; C08G81/021; C08G81/022
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
250 words
A continuous anionic solution polymerization process for producing star-block copolymers in a continuous tubular reactor having internal zones defined by a sequence of four static mixers, each of which is maintained at a temperature of from 65° to 85° C. and each has a means for introducing new matter at the inlet of the mixer, and the tubular reactor having a pressure control valve mounted after the last mixer to maintain the reactor in a liquid full mode at all times, said process consisting essentially of the steps of (a) continuously feeding to a first static mixer a solution of vinyl aromatic compound in an inert solvent and a solution of hydrocarbyllithium initiator in an inert solvent at a rate such that the time of flow of the solutions through the first mixer is between 6 and 15 minutes; (b) continuously feeding to a second static mixer a conjugated diene monomer, at sufficient pressure to ensure the diene is in the liquid state, at a rate such that the time of flow through the second mixer is between 25 and 55 minutes; (c) continuously feeding to a third static mixer a multifunctional coupling agent at a rate such that the time of flow through the third mixer is between 25 and 55 minutes; (d) continuously feeding to a fourth static mixer a terminating agent; (e) continuously removing the reaction product from the tubular reactor through the pressure control valve; and (f) separating the resulting star-block copolymer from the inert solvent.
Claim 2
Dependent Claim
250 words
A continuous anionic solution polymerization process for producing star-block copolymers in a continuous tubular reactor having internal zones defined by a sequence of four static mixers, each of which is maintained at a temperature of from 65° to 85° C. and each has a means for introducing new matter at the inlet of the mixer, and the tubular reactor having a pressure control valve mounted after the last mixer to maintain the reactor in a liquid full mode at all times, said process consisting essentially of the steps of (a) continuously feeding to a first static mixer a solution of vinyl aromatic compound in an inert solvent and a solution of hydrocarbyllithium initiator in an inert solvent at a rate such that the time of flow of the solutions through the first mixer is between 6 and 15 minutes; (b) continuously feeding to a second static mixer a conjugated diene monomer, at sufficient pressure to ensure the diene is in the liquid state, at a rate such that the time of flow through the second mixer is between 25 and 55 minutes; (c) continuously feeding to a third static mixer a multifunctional coupling agent at a rate such that the time of flow through the third mixer is between 25 and 55 minutes; (d) continuously feeding to a fourth static mixer a terminating agent; (e) continuously removing the reaction product from the tubular reactor through the pressure control valve; and (f) separating the resulting star-block copolymer from the inert solvent.
Claim 3
Dependent Claim
21 words
The process of claim 1 wherein the weight ratio of monovinyl aromatic compound to conjugated diene is from 25/75 to 55/45.
Claim 4
Dependent Claim
31 words
The process of claim 1 wherein the monovinyl aromatic compound is styrene, the conjugated diene is butadiene and the polyfunctional coupling agent is selected from o-divinylbenzene, m-divinylbenzene, p-divinylbenzene and mixtures thereof.
Claim 5
Dependent Claim
38 words
The process of claim 1 wherein a solution of hydrocarbyllithium initiator in an inert solvent is fed to the second static mixer along with the conjugated diene monomer, whereby a star-block copolymer having bimodal arm structure is produced.
References Cited (Backward Citations)
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US3637554A
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US3985830A
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US3985830B1
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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) | 1985-08-23 | 1986-02-22 | 1986-08-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-08-23 | 1990-02-22 | 1990-08-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-08-23 | 1994-02-22 | 1994-08-24 | $7700.00 | Window Closed / Lapsed |