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US4016347A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of polymers having a broad molecular weight distribution

Assignee: Huels AG
•
Filing: 1975-08-08
•
Granted: 1977-04-05
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Expires: 1995-08-08
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Abstract

Abstract 1,3-Butadiene is polymerized to polymers having broad molecular weight distribution in a continuous-adiabatic organolithium catalyzed polymerization in a flow pipe reactor by varying in a periodic manner the ratio of catalyst to 1,3-butadiene being charged to the reactor and mixing the polymers thus produced.

Inventors

  • 👤 Neithart Sommer
  • 👤 Gerhard Cuntze
  • 👤 Wolfgang Boehmer

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 10:56
CPC Classifications
C; C08; C08F; C08F136/00; C08F136/02; C08F136/04; C08F136/06

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 186 words
A process for the production of polymers having a broad molecular weight distribution by the continuous-adiabatic polymerization of 1,3-butadiene alone or in admixture with a comonomer in a diluent and in the presence of an organolithium catalyst which comprises feeding a stream of 1,3-butadiene and diluent at a constant flow rate of at least 1.10.sup. -3 liters/sec./cm 2 to an elongate reaction zone and feeding a stream of the catalyst to the inlet zone at a rate which is periodically increased and decreased with a cycle time of at least 1 sec., said flow rate and rate of change of catalyst flow rate being such that segments of reaction product along the length of the initial portion of the elongate reaction zone contain polymer having an average molecular weight which differs from the average molecular weight of the polymer in preceding and following like segments of reaction product adjacent thereto, and said reaction zone has a length to diameter ratio from about 5:1 to about 200:1 and is sufficiently elongate that said adjacent segments become remixed before the reaction product is discharged from said reaction zone.
Claim 2
Dependent Claim 186 words
A process for the production of polymers having a broad molecular weight distribution by the continuous-adiabatic polymerization of 1,3-butadiene alone or in admixture with a comonomer in a diluent and in the presence of an organolithium catalyst which comprises feeding a stream of 1,3-butadiene and diluent at a constant flow rate of at least 1.10.sup. -3 liters/sec./cm 2 to an elongate reaction zone and feeding a stream of the catalyst to the inlet zone at a rate which is periodically increased and decreased with a cycle time of at least 1 sec., said flow rate and rate of change of catalyst flow rate being such that segments of reaction product along the length of the initial portion of the elongate reaction zone contain polymer having an average molecular weight which differs from the average molecular weight of the polymer in preceding and following like segments of reaction product adjacent thereto, and said reaction zone has a length to diameter ratio from about 5:1 to about 200:1 and is sufficiently elongate that said adjacent segments become remixed before the reaction product is discharged from said reaction zone.
Claim 3
Dependent Claim 27 words
A process according to claim 1 wherein the elongate reaction zone is tubular with a ratio of length to diameter of from about 5:1 to about 200:1.
Claim 4
Dependent Claim 11 words
A process according to claim 1 wherein 1,3-butadiene only is homopolymerized.
Claim 5
Dependent Claim 16 words
A process according to claim 1 wherein the cycle time is about 1 to 30 seconds.

References Cited (Backward Citations)

US3402160A Cited
US3812088A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-04-04 1980-10-04 1981-04-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-04-04 1984-10-04 1985-04-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-04-04 1988-10-04 1989-04-05 $7700.00 Window Closed / Lapsed

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