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US3951925A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing improved vinyl chloride polymers

Assignee: JNC Corp
•
Filing: 1973-07-13
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Granted: 1976-04-20
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Expires: 1993-07-13
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Abstract

Abstract Polymer or copolymer of vinyl chloride having superior properties can be produced by suspension-polymerizing vinyl chloride or a mixture thereof with another vinyl monomer, at first, in the presence of an oil-soluble radical initiator, and thereafter, when the percentage of polymerization of the resulting polymer has reached about 15% to about 80%, subjecting the polymer to a further polymerization in the presence of a water-soluble radical initiator. The product thus obtained has both the merits resulting from suspension polymerization and emulsion one. It has an extremely high absorptivity of plasticizer, easy processability, and film made therefrom has substantially no fish eye.

Inventors

  • 👤 Sanetsugu Mishima
  • 👤 Tsutomu Matsubara
  • 👤 Hiroyuki Fujii
  • 👤 Kazumasa Funada
  • 👤 Masataka Torigoe

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 23:10
CPC Classifications
C; C08; C08F; C08F14/00; C08F14/02; C08F14/04; C08F14/06

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 87 words
A process for producing a vinyl chloride-containing polymer having improved properties which consists essentially of: a. subjecting a polymer feed selected from the group consisting of vinyl chloride or at least 80% by weight vinyl chloride and up to 20% by weight of another vinyl monomer copolymerizable therewith selected from the group consisting of vinyl acetate, vinyl stearate, methyl acrylate, ethyl acrylate, dimethyl maleate, dimethyl fumarate, vinyl octyl ether, vinyl cetyl ether, vinylidene chloride, acrylonitrile, ethylene and propylene to a first polymerization step involving aqueous suspension polymerization:
Claim 2
Dependent Claim 87 words
A process for producing a vinyl chloride-containing polymer having improved properties which consists essentially of: a. subjecting a polymer feed selected from the group consisting of vinyl chloride or at least 80% by weight vinyl chloride and up to 20% by weight of another vinyl monomer copolymerizable therewith selected from the group consisting of vinyl acetate, vinyl stearate, methyl acrylate, ethyl acrylate, dimethyl maleate, dimethyl fumarate, vinyl octyl ether, vinyl cetyl ether, vinylidene chloride, acrylonitrile, ethylene and propylene to a first polymerization step involving aqueous suspension polymerization:
Claim 3
Dependent Claim 138 words
which uses 100 to 400 parts by weight of water based upon 100 parts by weight of said polymer feed, 2. at a temperature of 30° to 70° C., 3. in the presence of an oil-soluble radical initiator in an amount of 0.005% to 0.2% by weight based upon the weight of said polymer feed, said oil-soluble radical initiator consisting of at least one member selected from the group consisting of dilauroyl peroxide, dibenzoyl peroxide, di-2-ethylhexyl peroxide, 3,5,5-trimethylhexanoyl peroxide, 2,4-dichlorobenzoyl peroxide, azobisisobutyronitrile, 2,2'-azobis-2,4-dimethylvaleronitrile, 2,2'-azobis-4-methoxy-2,4-dimethylvaleronitrile, isopropyl peroxydicarbonate, disecondary butyl peroxydicarbonate, t-butyl peroxypivalate and acetyl cyclohexylsulfonyl peroxide, b. deactivating said oil-soluble radical initiator when the polymerization in said first step reaches 15% to 80% completion, said deactivation being carried out by the addition of an alkaline substance, c. continuing the polymerization of said polymer feed in a second polymerization step
Claim 4
Dependent Claim 138 words
which uses 100 to 400 parts by weight of water based upon 100 parts by weight of said polymer feed, 2. at a temperature of 30° to 70° C., 3. in the presence of an oil-soluble radical initiator in an amount of 0.005% to 0.2% by weight based upon the weight of said polymer feed, said oil-soluble radical initiator consisting of at least one member selected from the group consisting of dilauroyl peroxide, dibenzoyl peroxide, di-2-ethylhexyl peroxide, 3,5,5-trimethylhexanoyl peroxide, 2,4-dichlorobenzoyl peroxide, azobisisobutyronitrile, 2,2'-azobis-2,4-dimethylvaleronitrile, 2,2'-azobis-4-methoxy-2,4-dimethylvaleronitrile, isopropyl peroxydicarbonate, disecondary butyl peroxydicarbonate, t-butyl peroxypivalate and acetyl cyclohexylsulfonyl peroxide, b. deactivating said oil-soluble radical initiator when the polymerization in said first step reaches 15% to 80% completion, said deactivation being carried out by the addition of an alkaline substance, c. continuing the polymerization of said polymer feed in a second polymerization step
Claim 5
Dependent Claim 62 words
at a temperature of 30° to 70°C., 2. in the presence of a water-soluble radical initiator which is present in an amount of from 0.02 to 0.2% by weight based upon the total weight of the polymerization system, said water-soluble radical initiator being at least one member selected from the group consisting of potassium persulfate, ammonium persulfate, hydrogen peroxide, and 2,2'-azobis(2-amidino-propane hydrochloride).
Claim 6
Dependent Claim 62 words
at a temperature of 30° to 70°C., 2. in the presence of a water-soluble radical initiator which is present in an amount of from 0.02 to 0.2% by weight based upon the total weight of the polymerization system, said water-soluble radical initiator being at least one member selected from the group consisting of potassium persulfate, ammonium persulfate, hydrogen peroxide, and 2,2'-azobis(2-amidino-propane hydrochloride).
Claim 7
Dependent Claim 57 words
A process for producing a vinyl chloride-containing polymer having improved properties which consists essentially of: a. subjecting a polymer feed selected from the group consisting of vinyl chloride or at least 80% by weight vinyl chloride and up to 20% by weight of another vinyl monomer copolymerizable therewith to a first polymerization step involving aqueous suspension polymerization:
Claim 8
Dependent Claim 57 words
A process for producing a vinyl chloride-containing polymer having improved properties which consists essentially of: a. subjecting a polymer feed selected from the group consisting of vinyl chloride or at least 80% by weight vinyl chloride and up to 20% by weight of another vinyl monomer copolymerizable therewith to a first polymerization step involving aqueous suspension polymerization:
Claim 9
Dependent Claim 106 words
at a temperature of 30° to 70°C., 3. in the presence of an oil-soluble radical initiator in an amount of 0.003% to 0.5% by weight based upon the weight of said polymer feed, b. deactivating said oil-soluble radical initiator when the polymerization in said fist step reaches 15% to 80% completion, c. continuing the polymerization of said polymer feed in a second polymerization step 1. at a temperature of 30° to 70°C., 2. in the presence of a water-soluble radical initiator which is present in an amount of more than 0.01% and up to 0.3% by weight based upon the total weight of the polymerization system.
Claim 10
Dependent Claim 106 words
at a temperature of 30° to 70°C., 3. in the presence of an oil-soluble radical initiator in an amount of 0.003% to 0.5% by weight based upon the weight of said polymer feed, b. deactivating said oil-soluble radical initiator when the polymerization in said fist step reaches 15% to 80% completion, c. continuing the polymerization of said polymer feed in a second polymerization step 1. at a temperature of 30° to 70°C., 2. in the presence of a water-soluble radical initiator which is present in an amount of more than 0.01% and up to 0.3% by weight based upon the total weight of the polymerization system.
Claim 11
Dependent Claim 15 words
A process according to claim 2, wherein said deactivating is carried out by elevating temperature.
Claim 12
Dependent Claim 22 words
A process according to claim 3, wherein said deactivating is carried out by addition of an alkaline substance or a reducible substance.
Claim 13
Dependent Claim 87 words
A process for producing a vinyl chloride-containing polymer having improved properties which consists essentially of: a. subjecting a polymer feed selected from the group consisting of vinyl chloride or at least 80% by weight vinyl chloride and up to 20% by weight of another vinyl monomer copolymerizable therewith selected from the group consisting of vinyl acetate, vinyl stearate, methyl acrylate, ethyl acrylate, dimethyl maleate, dimethyl fumarate, vinyl octyl ether, vinyl cetyl ether, vinylidene chloride, acrylonitrile, ethylene and propylene to a first polymerization step involving aqueous suspension polymerization:
Claim 14
Dependent Claim 87 words
A process for producing a vinyl chloride-containing polymer having improved properties which consists essentially of: a. subjecting a polymer feed selected from the group consisting of vinyl chloride or at least 80% by weight vinyl chloride and up to 20% by weight of another vinyl monomer copolymerizable therewith selected from the group consisting of vinyl acetate, vinyl stearate, methyl acrylate, ethyl acrylate, dimethyl maleate, dimethyl fumarate, vinyl octyl ether, vinyl cetyl ether, vinylidene chloride, acrylonitrile, ethylene and propylene to a first polymerization step involving aqueous suspension polymerization:
Claim 15
Dependent Claim 192 words
which uses 100 to 400 parts by weight of water based upon 100 parts by weight of said polymer feed, 2. at a temperature of 30° to 70°C., 3. in the presence of an oil-soluble radical initiator in an amount of .005% to .2% by weight based upon the weight of said polymer feed, said oil-soluble radical initiator consisting of at least one member selected from the group consisting of dilauroyl peroxide, dibenzoyl peroxide, di-2-ethylhexyl peroxide, 3,5,5-trimethylhexanoyl peroxide, 2,4-dichlorobenzoyl peroxide, azobisisobutyronitrile, 2,2'-azobis-2,4-dimethylvaleronitrile, 2,2'-azobis-4-methoxy-2,4-dimethylvaleronitrile, isopropyl peroxydicarbonate, disecondary butyl peroxydicarbonate, t-butyl peroxypivalate and acetyl cyclohexylsulfonyl peroxide, and, when said first polymerization step has reached a percentage of completion within the range of 15 - 80%., and then b. continuing the polymerization of said polymer feed in a second polymerization step 1. at a temperature of 30° to 70°C., 2. in the presence of a water-soluble radical initiator which is present in an amount of from 0.02 to 0.2% by weight based upon the total weight of the polymerization system, said water-soluble radical initiator being at least one member selected from the group consisting of potassium persulfate, ammonium persulfate, hydrogen peroxide, and 2,2'-azobis (2-amidino-propane hydrochloride).
Claim 16
Dependent Claim 192 words
which uses 100 to 400 parts by weight of water based upon 100 parts by weight of said polymer feed, 2. at a temperature of 30° to 70°C., 3. in the presence of an oil-soluble radical initiator in an amount of .005% to .2% by weight based upon the weight of said polymer feed, said oil-soluble radical initiator consisting of at least one member selected from the group consisting of dilauroyl peroxide, dibenzoyl peroxide, di-2-ethylhexyl peroxide, 3,5,5-trimethylhexanoyl peroxide, 2,4-dichlorobenzoyl peroxide, azobisisobutyronitrile, 2,2'-azobis-2,4-dimethylvaleronitrile, 2,2'-azobis-4-methoxy-2,4-dimethylvaleronitrile, isopropyl peroxydicarbonate, disecondary butyl peroxydicarbonate, t-butyl peroxypivalate and acetyl cyclohexylsulfonyl peroxide, and, when said first polymerization step has reached a percentage of completion within the range of 15 - 80%., and then b. continuing the polymerization of said polymer feed in a second polymerization step 1. at a temperature of 30° to 70°C., 2. in the presence of a water-soluble radical initiator which is present in an amount of from 0.02 to 0.2% by weight based upon the total weight of the polymerization system, said water-soluble radical initiator being at least one member selected from the group consisting of potassium persulfate, ammonium persulfate, hydrogen peroxide, and 2,2'-azobis (2-amidino-propane hydrochloride).
Claim 17
Dependent Claim 86 words
A process for producing a vinyl chloride-containing polymer having improved properties which consists essentially of: a. subjecting a polymer feed selected from the group consisting of vinyl chloride or at least 80% by weight vinyl chloride and up to 20% by weight of another vinyl monomer copolymerizable therewith to a first polymerization step involving aqueous suspension polymerization: 1. which uses 100 to 400 parts by weight of water based upon 100 parts by weight of said polymer feed, 2. at a temperature of 30° to 70°C.,
Claim 18
Dependent Claim 86 words
A process for producing a vinyl chloride-containing polymer having improved properties which consists essentially of: a. subjecting a polymer feed selected from the group consisting of vinyl chloride or at least 80% by weight vinyl chloride and up to 20% by weight of another vinyl monomer copolymerizable therewith to a first polymerization step involving aqueous suspension polymerization: 1. which uses 100 to 400 parts by weight of water based upon 100 parts by weight of said polymer feed, 2. at a temperature of 30° to 70°C.,
Claim 19
Dependent Claim 100 words
in the presence of an oil-soluble radical initiator in an amount of 0.003% to 0.5% by based upon the weight of said polymer feed, and, when said first polymerization step has reached a percentage of completion within the range of 15 - 80%., and then b. continuing the polymerization of said polymer feed in a second polymerization step 1. at a temperature of 30° to 70°C., 2. in the presence of a water-soluble radical initiator which is present in an amount of more than 0.01% and up to 0.3% by weight based upon the total weight of the polymerization system.
Claim 20
Dependent Claim 100 words
in the presence of an oil-soluble radical initiator in an amount of 0.003% to 0.5% by based upon the weight of said polymer feed, and, when said first polymerization step has reached a percentage of completion within the range of 15 - 80%., and then b. continuing the polymerization of said polymer feed in a second polymerization step 1. at a temperature of 30° to 70°C., 2. in the presence of a water-soluble radical initiator which is present in an amount of more than 0.01% and up to 0.3% by weight based upon the total weight of the polymerization system.

References Cited (Backward Citations)

US2652392A Cited
US3558584A Cited
US3687917A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-04-20 1979-10-20 1980-04-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-04-20 1983-10-20 1984-04-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-04-20 1987-10-20 1988-04-20 $7700.00 Window Closed / Lapsed

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