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US4039500A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for controlling molecular weight distribution of latex polymers

Assignee: Union Carbide Corp
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Filing: 1975-10-22
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Granted: 1977-08-02
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Expires: 1995-10-22
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Abstract

Abstract Particle morphology and molecular weight distribution of latex polymers is controlled by a process wherein a primary polymerizable feed composition, (a) a crosslinker and (b) a chain transfer agent during at least a portion of the period of addition of said composition to the polymerization zone, is fed into a polymerization zone while simultaneously feeding a secondary polymerizable feed composition containing chain transfer agent to the primary polymerizable feed composition and thus continually varying the compositional content of the primary polymerizable feed composition.

Inventors

  • 👤 David Robinson Bassett
  • 👤 Kenneth Look Hoy

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 02:25
CPC Classifications
C; C08; C08F; C08F2/00; C08F2/12; C08F2/16; C08F2/22

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 228 words
A process for controlling the particle morphology and molecular weight distribution of emulsion polymerized latex polymers, said process comprising introducing at least one primary polymerizable ethylenically unsaturated monomers feed composition containing from 0 to 5 weight percent of a chain transfer agent and from 0 to 5 weight percent of at least one crosslinking agent from at least one primary feed source to a polymerization zone, said primary polymerizable ethylenically unsaturated monomers feed composition continually varying in compositional content by the simultaneous addition thereto during its introduction to the polymerization zone, from at least one secondary feed source, of at least one secondary polymerizable ethylenically unsaturated monomers feed composition containing from 0 to 5 weight percent of a chain transfer agent and from 0 to 5 weight percent of at least one crosslinking agent so as to continually change the compositional content of the primary polymerizable ethylenically unsaturated monomers feed composition in said primary feed source during the addition thereto of said secondary polymerizable ethylenically unsaturated monomers feed composition, and simultaneously polymerizing the primary polymerizable ethylenically unsaturated monomers feed composition introduced to the polymerization zone whereby emulsion polymerized latex polymer of broadened molecular weight distribution is produced; with the proviso that there be a positive amount of said chain transfer agent in at least one of said feed compositions during at least a portion of the polymerization period.
Claim 2
Dependent Claim 228 words
A process for controlling the particle morphology and molecular weight distribution of emulsion polymerized latex polymers, said process comprising introducing at least one primary polymerizable ethylenically unsaturated monomers feed composition containing from 0 to 5 weight percent of a chain transfer agent and from 0 to 5 weight percent of at least one crosslinking agent from at least one primary feed source to a polymerization zone, said primary polymerizable ethylenically unsaturated monomers feed composition continually varying in compositional content by the simultaneous addition thereto during its introduction to the polymerization zone, from at least one secondary feed source, of at least one secondary polymerizable ethylenically unsaturated monomers feed composition containing from 0 to 5 weight percent of a chain transfer agent and from 0 to 5 weight percent of at least one crosslinking agent so as to continually change the compositional content of the primary polymerizable ethylenically unsaturated monomers feed composition in said primary feed source during the addition thereto of said secondary polymerizable ethylenically unsaturated monomers feed composition, and simultaneously polymerizing the primary polymerizable ethylenically unsaturated monomers feed composition introduced to the polymerization zone whereby emulsion polymerized latex polymer of broadened molecular weight distribution is produced; with the proviso that there be a positive amount of said chain transfer agent in at least one of said feed compositions during at least a portion of the polymerization period.
Claim 3
Dependent Claim 21 words
A process as claimed in claim 1, wherein the concentration of chain transfer agent is from 0.05 to 1 weight percent.
Claim 4
Dependent Claim 21 words
A process as claimed in claim 1, wherein the concentration of chain transfer agent is from 0.1 to 0.5 weight percent.
Claim 5
Dependent Claim 20 words
A process as claimed in claim 1, wherein the concentration of crosslinking agent is from 0.05 to 1 weight percent.
Claim 6
Dependent Claim 25 words
A process as claimed in claim 1, wherein the chain transfer agent is originally present solely in the secondary polymerizable ethylenically unsaturated monomers feed composition.
Claim 7
Dependent Claim 23 words
A process as claimed in claim 1, wherein the crosslinking agent is originally present in the primary polymerizable ethylenically unsaturated monomers feed composition.
Claim 8
Dependent Claim 51 words
A process as claimed in claim 1, wherein the chain transfer agent is present in the secondary polymerizable ethylenically unsaturated monomers feed composition for a period of time less than the entire period of time required to add said feed composition to the primary feed source from the secondary feed source.
Claim 9
Dependent Claim 16 words
A process as claimed in claim 1, wherein the chain transfer agent is an organic mercaptan.
Claim 10
Dependent Claim 15 words
A process as claimed in claim 1, wherein the chain transfer agent is butyl mercaptan.
Claim 11
Dependent Claim 14 words
A process as claimed in claim 1, wherein the chain transfer agent is dodecylmercaptan.
Claim 12
Dependent Claim 9 words
A polymer produced by the process of claim 1.

References Cited (Backward Citations)

US3562240A Cited
US3562235A Cited
US3804881A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-08-01 1981-01-31 1981-08-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-08-01 1985-01-31 1985-08-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-08-01 1989-01-31 1989-08-02 $7700.00 Window Closed / Lapsed

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