US4075138A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Polymerization process and vinylidene chloride microspheres produced thereby
Assignee: Casco Adhesives AB
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Filing: 1977-05-03
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Granted: 1978-02-21
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Expires: 1997-05-03
Abstract
Abstract Vinylidene chloride microspheres are polymerized in relatively large vessels with a relatively reduced peak exotherm employing a small quantity of a comonomer such as methacrylonitrile, methylmethacrylate, sytrene or butadiene which has a higher copolymerization reactivity with respect to acrylonitrile and a lower propagation rate constant.
Inventors
- 👤 Joseph L. Garner
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 14:57
CPC Classifications
B; B01; B01J; B01J13/00; B01J13/02; B01J13/06; B01J13/14; B01J13/18; B01J13/185; C; C08; C08F; C08F214/00; C08F214/02; C08F214/04; C08F214/08; Y; Y10; Y10T; Y10T428/00; Y10T428/29; Y10T428/2982
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
232 words
In a method for the preparation of synthetic resinous thermoplastic microspheres employing from 60 to 90 parts by weight of vinylidene chloride and from 40 to 10 parts by weight of acrylonitrile, the steps of the method comprising preparing an oil phase containing the polymerizable component and a liquid blowing agent which volatilizes at a temperature below the heat softening point of the polymer prepared from the monomer mixture, dispersing the oil phase in the water phase, the water phase containing a dispersion stabilizer, the oil phase being dispersed as a plurality of droplets having diameters from about 1 to about 50 microns, initiating polymerization of the monomer in the droplets to form a plurality of hollow polymer particles having symmetrically encapsulated therein a volatile fluid foaming agent, the improvement which comprises employing from about 3 to 12 parts by weight of a copolymerizable monomer having a propagation constant of from about 2 to about 15,000 liters per mole second and (r 1 /r 2 ) >1 wherein r 1 is the reactivity ratio for the copolymerizable monomer and r 2 is the reactivity ratio for acrylonitrile, with the further limitation that the vinylidene chloride/acrylonitrile/volatile fluid foaming agent and the copolymerizable monomer are mutually soluble at a temperature between about 20° to 90° C and the copolymerizable monomer being selected from the group consisting of methacrylonitrile, methylmethacrylate, styrene, 1,3-butadiene and mixtures thereof.
Claim 2
Dependent Claim
232 words
In a method for the preparation of synthetic resinous thermoplastic microspheres employing from 60 to 90 parts by weight of vinylidene chloride and from 40 to 10 parts by weight of acrylonitrile, the steps of the method comprising preparing an oil phase containing the polymerizable component and a liquid blowing agent which volatilizes at a temperature below the heat softening point of the polymer prepared from the monomer mixture, dispersing the oil phase in the water phase, the water phase containing a dispersion stabilizer, the oil phase being dispersed as a plurality of droplets having diameters from about 1 to about 50 microns, initiating polymerization of the monomer in the droplets to form a plurality of hollow polymer particles having symmetrically encapsulated therein a volatile fluid foaming agent, the improvement which comprises employing from about 3 to 12 parts by weight of a copolymerizable monomer having a propagation constant of from about 2 to about 15,000 liters per mole second and (r 1 /r 2 ) >1 wherein r 1 is the reactivity ratio for the copolymerizable monomer and r 2 is the reactivity ratio for acrylonitrile, with the further limitation that the vinylidene chloride/acrylonitrile/volatile fluid foaming agent and the copolymerizable monomer are mutually soluble at a temperature between about 20° to 90° C and the copolymerizable monomer being selected from the group consisting of methacrylonitrile, methylmethacrylate, styrene, 1,3-butadiene and mixtures thereof.
Claim 3
Dependent Claim
11 words
The method of claim 1 wherein the copolymerizable monomer is methacrylonitrile.
Claim 4
Dependent Claim
165 words
An improved synthetic resinous thermoplastic microsphere having polymerized in the polymer shell from about 60 to 90 parts by weight of vinylidene chloride, from about 40 to 10 parts by weight of acrylonitrile and from about 3 to 12 parts by weight of a copolymerizable monomer having a propagation constant of from about 2 to about 15,000 liters per mole second and (r 1 /r 2 ) >1 wherein r 1 is the reactivity ratio for the copolymerizable monomer and r 2 is the reactivity ratio for acrylonitrile, the copolymerizable monomer being selected from the group consisting of methacrylonitrile, methylmethacrylate, styrene, 1,3-butadiene and mixtures thereof with the further limitation that the vinylidene chloride/acrylonitrile/volatile fluid foaming agent and the copolymerizable monomer are mutually soluble at a temperature between about 20° to 90° C, having generally symmetrically encapsulated therein a volatile liquid blowing agent which volatilizes at a temperature below the heat softening point of the polymer, the blowing agent being a distinct and separate liquid phase.
Claim 5
Dependent Claim
165 words
An improved synthetic resinous thermoplastic microsphere having polymerized in the polymer shell from about 60 to 90 parts by weight of vinylidene chloride, from about 40 to 10 parts by weight of acrylonitrile and from about 3 to 12 parts by weight of a copolymerizable monomer having a propagation constant of from about 2 to about 15,000 liters per mole second and (r 1 /r 2 ) >1 wherein r 1 is the reactivity ratio for the copolymerizable monomer and r 2 is the reactivity ratio for acrylonitrile, the copolymerizable monomer being selected from the group consisting of methacrylonitrile, methylmethacrylate, styrene, 1,3-butadiene and mixtures thereof with the further limitation that the vinylidene chloride/acrylonitrile/volatile fluid foaming agent and the copolymerizable monomer are mutually soluble at a temperature between about 20° to 90° C, having generally symmetrically encapsulated therein a volatile liquid blowing agent which volatilizes at a temperature below the heat softening point of the polymer, the blowing agent being a distinct and separate liquid phase.
Claim 6
Dependent Claim
11 words
The microsphere of claim 3 wherein the copolymerizable monomer is methacrylonitrile.
Claim 7
Dependent Claim
180 words
In a method for the preparation of synthetic resinous thermoplastic microspheres employing from 60 to 90 parts by weight of vinylidene chloride and from 40 to 10 parts by weight of acrylonitrile, the steps of the method comprising preparing an oil phase containing the polymerizable component and a liquid blowing agent which volatilizes at a temperature below the heat softening point of the polymer prepared from the monomer mixture, dispersing the oil phase in the water phase, the water phase containing a dispersion stabilizer, the oil phase being dispersed as a plurality of droplets having diameters from about 1 to about 50 microns, initiating polymerization of the monomer in the droplets to form a plurality of hollow polymer particles having symmetrically encapsulated therein a volatile fluid foaming agent, the improvement which comprises employing as the copolymerizable monomer from about 3 to 12 parts by weight of methacrylonitrile, methylmethacrylate, styrene, 1,3-butadiene and mixtures thereof, with the further limitation that the vinylidene chloride/acrylonitrile/volatile fluid foaming agent and the copolymerizable monomer are mutually soluble at a temperature between about 20° to 90° C.
Claim 8
Dependent Claim
180 words
In a method for the preparation of synthetic resinous thermoplastic microspheres employing from 60 to 90 parts by weight of vinylidene chloride and from 40 to 10 parts by weight of acrylonitrile, the steps of the method comprising preparing an oil phase containing the polymerizable component and a liquid blowing agent which volatilizes at a temperature below the heat softening point of the polymer prepared from the monomer mixture, dispersing the oil phase in the water phase, the water phase containing a dispersion stabilizer, the oil phase being dispersed as a plurality of droplets having diameters from about 1 to about 50 microns, initiating polymerization of the monomer in the droplets to form a plurality of hollow polymer particles having symmetrically encapsulated therein a volatile fluid foaming agent, the improvement which comprises employing as the copolymerizable monomer from about 3 to 12 parts by weight of methacrylonitrile, methylmethacrylate, styrene, 1,3-butadiene and mixtures thereof, with the further limitation that the vinylidene chloride/acrylonitrile/volatile fluid foaming agent and the copolymerizable monomer are mutually soluble at a temperature between about 20° to 90° C.
Claim 9
Dependent Claim
116 words
An improved synthetic resinous thermoplastic microsphere having polymerized in the polymer shell from about 60 to 90 parts by weight vinylidene chloride, from about 40 to 10 parts by weight acrylonitrile and from about 3 to 12 parts by weight of a monomer selected from the group consisting of methacrylonitrile, methylmethacrylate, styrene, 1,3-butadiene and mixtures thereof, with the further limitation that the vinylidene chloride/acrylonitrile/volatile fluid foaming agent and the copolymerizable monomer are mutually soluble at a temperature between about 20° to 90° C, having generally symmetrically encapsulated therein a volatile liquid blowing agent which volatilizes at a temperature below the heat softening point of the polymer, the blowing agent being a distinct and separate liquid phase.
Claim 10
Dependent Claim
116 words
An improved synthetic resinous thermoplastic microsphere having polymerized in the polymer shell from about 60 to 90 parts by weight vinylidene chloride, from about 40 to 10 parts by weight acrylonitrile and from about 3 to 12 parts by weight of a monomer selected from the group consisting of methacrylonitrile, methylmethacrylate, styrene, 1,3-butadiene and mixtures thereof, with the further limitation that the vinylidene chloride/acrylonitrile/volatile fluid foaming agent and the copolymerizable monomer are mutually soluble at a temperature between about 20° to 90° C, having generally symmetrically encapsulated therein a volatile liquid blowing agent which volatilizes at a temperature below the heat softening point of the polymer, the blowing agent being a distinct and separate liquid phase.
References Cited (Backward Citations)
US3615972A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-02-20 | 1981-08-22 | 1982-02-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-02-20 | 1985-08-22 | 1986-02-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-02-20 | 1989-08-22 | 1990-02-21 | $7700.00 | Window Closed / Lapsed |