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Free-radical polymerizations using mixed initiator systems at two thermally distinct polymerization stages

Assignee: Arkema Inc
•
Filing: 1977-01-06
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Granted: 1978-12-12
•
Expires: 1997-01-06
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Abstract

Abstract A process for the free-radical polymerization of vinyl aromatic monomers in at least two thermally distinct polymerization stages each between the temperatures of about 70° C and 150° C in the presence of at least two free-radical initiators, one of which initiators is particularly effective at the lowest temperature stage and has the formula ##STR1## wherein R is an alkylene, alkynylene or alkenylene diradical, R 1 is alkyl, alkenyl, alkyn or alkoxy and Rhd 2 is lower alkyl and R 3 is hydrogen or a lower alkyl and a second of which initiators has a 10 hour half-life temperature of at least about 80° C which temperature is at least about 15° C above the 10 hour half-life temperature of the compound of the above formula.

Inventors

  • 👤 Vasanth R. Kamath
  • 👤 Gary A. Harpell

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 12:35
CPC Classifications
C; C08; C08F; C08F4/00; C08F4/28; C08F4/32; C08F4/38

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 177 words
A process for the free-radical polymerization of vinyl monomers, including vinyl aromatic monomers, comprises polymerizing said vinyl monomers in at least two thermally distinct polymerization stages, each between the temperatures of about 70° C. and 150° C. in the presence of at least two free-radical initiators, one of which initiators is particularly effective at the lowest temperature stage and has the formula ##STR3## and where R is an alkylene, alkynylene or alkenylene diradical, R 1 is alkyl, alkenyl, alkynl or alkoxy and R 2 is lower alkyl and R 3 is hydrogen or lower alkyl and a second of which initiators have a 10 hour half-life temperature of at least about 80° C., said temperature being at least about 15° C. above the 10 hour half-life temperature of the compound of Formula (I) wherein the same solvent is used for measuring the half-life of all initiators, wherein the initiator of Formula (I) allows completing the polymerization in a shorter time with the resulting polymer having a higher viscosity-average molecular weight than without the initiator of Formula (I).
Claim 2
Dependent Claim 177 words
A process for the free-radical polymerization of vinyl monomers, including vinyl aromatic monomers, comprises polymerizing said vinyl monomers in at least two thermally distinct polymerization stages, each between the temperatures of about 70° C. and 150° C. in the presence of at least two free-radical initiators, one of which initiators is particularly effective at the lowest temperature stage and has the formula ##STR3## and where R is an alkylene, alkynylene or alkenylene diradical, R 1 is alkyl, alkenyl, alkynl or alkoxy and R 2 is lower alkyl and R 3 is hydrogen or lower alkyl and a second of which initiators have a 10 hour half-life temperature of at least about 80° C., said temperature being at least about 15° C. above the 10 hour half-life temperature of the compound of Formula (I) wherein the same solvent is used for measuring the half-life of all initiators, wherein the initiator of Formula (I) allows completing the polymerization in a shorter time with the resulting polymer having a higher viscosity-average molecular weight than without the initiator of Formula (I).
Claim 3
Dependent Claim 14 words
The process of claim 1 wherein the vinyl monomer is a vinyl aromatic monomer.
Claim 4
Dependent Claim 12 words
The process of claim 2 wherein the vinyl aromatic monomer is styrene.
Claim 5
Dependent Claim 13 words
The process of claim 3 wherein the initiator of formula (I) is 2,5-dimethyl-2,5-bis[2-ethylhexanoylperoxy]hexane.
Claim 6
Dependent Claim 11 words
The process of claim 4 wherein said second initiator is 2,5-dimethyl-2,5-bis[benzoylperoxy]hexane.
Claim 7
Dependent Claim 17 words
The process of claim 4 wherein said second initiator is a mixture of 2,5-dimethyl-2,5-bis[benzoylperoxy]hexane and di-t-butyl diperoxycarbonate.
Claim 8
Dependent Claim 18 words
The process of claim 4 wherein said second initiator is a mixture of 1,1-bis(t-butylperoxy)cyclohexane and tertiary butyl perbenzoate.
Claim 9
Dependent Claim 16 words
The process of claim 4 wherein said second initiator is a mixture of 2,5-dimethyl-2,5-bis[benzoylperoxy]hexane and ethyl(3,3-bis(t-butylperoxy)butyrate.
Claim 10
Dependent Claim 15 words
The process of claim 4 wherein said initiators are used in a bulk polymerization technique.
Claim 11
Dependent Claim 15 words
The process of claim 4 wherein said initiators are used in a suspension polymerization technique.
Claim 12
Dependent Claim 19 words
The process of claim 4 wherein the polymerization stages are between the temperatures of 90° C. and 130° C.

References Cited (Backward Citations)

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US2907756A Cited
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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) 1981-12-11 1982-06-12 1982-12-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-12-11 1986-06-12 1986-12-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-12-11 1990-06-12 1990-12-12 $7700.00 Window Closed / Lapsed

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