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US4184027A Expired / Lapsed US ⏱️ 0.0 years remaining

Recycle control system for continuous polymerization

Assignee: Bayer Antwerpen NV
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Filing: 1974-03-18
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Granted: 1980-01-15
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Expires: 1994-03-18
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Abstract

Abstract A system for controlling the percent of polymer in a reactor in a process in which the reactor effluent, comprising a mixture of polymer, unreacted materials and, possibly, by-products, goes through a separator to remove from such effluent unreacted materials and by-products. The system is especially useful with variable fillage, horizontal continuous stirred tank reactors.

Inventors

  • 👤 Byrd Hopkins

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 15:33
CPC Classifications
B; B01; B01J; B01J19/00; B01J19/24; B01J19/2455; B01J19/2465; B01J19/0006; B01J2219/00; B01J2219/18; B01J2219/182

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 293 words
A method for controlling material balance and weight fraction of polymer in a continuous polymerization reaction producing a mixture of unreacted material and polymer having (a) a variable fillage horizontal continuously stirred and reflux cooled reaction zone wherein monomer is polymerized to polymer, (b) a separation zone in which unreacted material is separated from polymer, and (c) a flow regulating means therebetween, the feed rate of monomer to said reaction zone being maintained at a prechosen constant value, and the effluent rate from said reaction zone being regulated to control the flow rate of unreacted material from said separation zone at a prechosen constant value, so that the total weight of unreacted material and polymer in said reaction zone automatically tends toward a steady value at which the weight fraction of polymer in said reaction zone will be determined by the following relationship: ##EQU2## said method comprising the steps of: (A) feeding continuously and at a constant prechosen rate monomers to said reaction zone, (B) removing through said flow regulating means a mixture of unreacted material and polymer from said polymerization zone and feeding such mixture to said separation zone, (C) separating in said separation zone at least a predetermined weight percentage of said unreacted material from said polymer, (D) measuring the flow rate of unreacted material so separated in said separation zone and generating a signal representative of said flow rate, (E) comparing said flow rate signal with a prechosen set signal to produce a control signal, and (F) feeding said control signal to said flow regulating means to regulate the flow rate of said mixture so removed from said reaction zone, thereby to achieve the desired control of said material balance and said weight fraction of polymer in said reaction zone.
Claim 2
Independent Claim 293 words
A method for controlling material balance and weight fraction of polymer in a continuous polymerization reaction producing a mixture of unreacted material and polymer having (a) a variable fillage horizontal continuously stirred and reflux cooled reaction zone wherein monomer is polymerized to polymer, (b) a separation zone in which unreacted material is separated from polymer, and (c) a flow regulating means therebetween, the feed rate of monomer to said reaction zone being maintained at a prechosen constant value, and the effluent rate from said reaction zone being regulated to control the flow rate of unreacted material from said separation zone at a prechosen constant value, so that the total weight of unreacted material and polymer in said reaction zone automatically tends toward a steady value at which the weight fraction of polymer in said reaction zone will be determined by the following relationship: ##EQU2## said method comprising the steps of: (A) feeding continuously and at a constant prechosen rate monomers to said reaction zone, (B) removing through said flow regulating means a mixture of unreacted material and polymer from said polymerization zone and feeding such mixture to said separation zone, (C) separating in said separation zone at least a predetermined weight percentage of said unreacted material from said polymer, (D) measuring the flow rate of unreacted material so separated in said separation zone and generating a signal representative of said flow rate, (E) comparing said flow rate signal with a prechosen set signal to produce a control signal, and (F) feeding said control signal to said flow regulating means to regulate the flow rate of said mixture so removed from said reaction zone, thereby to achieve the desired control of said material balance and said weight fraction of polymer in said reaction zone.
Claim 3
Dependent Claim 23 words
The method of claim 1 wherein at least a portion of the said unreacted material so separated is returned to said reaction zone.
Claim 4
Dependent Claim 25 words
The method of claim 1 wherein the reaction is a continuous polymerization of styrene, the monomer comprises styrene and the unreacted material comprises styrene monomer.

References Cited (Backward Citations)

US2556851A Cited
US2634257A Cited
US2989517A Cited
US3130187A Cited
US3341622A Cited
US3794471A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-01-14 1983-07-16 1984-01-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-01-14 1987-07-16 1988-01-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-01-14 1991-07-16 1992-01-15 $7700.00 Window Closed / Lapsed

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