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Process for the production of extra soft polyvinyl chloride foam plastics

Assignee: Lonza AG
•
Filing: 1975-10-06
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Granted: 1978-03-14
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Expires: 1995-10-06
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Abstract

Abstract The process for the production of closed-cell, extra soft polyvinylchloride foam plastics having improved volume stability at elevated temperatures. The process includes heating a plastisol or plastigel comprised of a plasticizer and foaming agent containing polyvinyl chloride or vinyl chloride copolymerizate in a pressure mold at a pressure of up to 300 atm. to a temperature of 150° to 180° C. for 1 to 2 hours. The plastigel or plastisol is cooled, at an unchanged closing force of the press of said pressure mold, to a temperature of 20° to 70° C. The plastigel or plastisol is removed from the pressure mold, a crude foam plastic forming. The crude foam plastic is heated under a gas pressure of 2 to 10 atm. to a temperature of 140° to 170° C. The crude foam plastic is cooled at said pressure of 2 to 10 atm. to a temperature of 100° to 130° C. The pressure is lowered to atmospheric pressure, the foam plastic simultaneous expanding. The resultant foam plastic will not shrink or expand more than 5 percent after storage for one week at 60° C.

Inventors

  • 👤 Emil Brunner
  • 👤 Alfred Huber

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 15:43
CPC Classifications
C; C08; C08J; C08J9/00; C08J9/04; C08J9/06; C08J2327/00; C08J2327/02; C08J2327/04; C08J2327/06; Y; Y10; Y10S; Y10S264/00; Y10S264/60

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 216 words
The process for the production of a closed-cell, extra soft polyvinylchloride foam plastic product having improved volume stability at elevated temperatures which comprises (a) heating a plastisol or plastigel comprised of a plasticizer- and a foaming agent-containing polyvinyl chloride or vinylchloride copolymerizate in a pressure mold at a pressure of up to 300 atm. to a temperature of 150° to 180° C., (b) cooling said plastigel or plastisol, at an unchanged closing force of the press or said pressure mold, to a temperature of 20° to 70° C., (c) removing said cooled plastigel or plastisol from said pressure mold as a crude foam plastic preform, (d) heating said crude foam plastic preform under a gas pressure of 2 to 10 atm. to a temperature of 140° to 170° C., (e) cooling said crude foam plastic preform at said pressure of 2 to 10 atm. to a temperature of 100° to 130° C., and (f) lowering said pressure to atmospheric pressure, said foam plastic preform simultaneously expanding to form said closed-cell extra soft polyvinyl chloride product, step (a) achieving gelation and the decomposition of the foaming agent, step (d) imparting said extra softness and said improved volume stability at elevated temperatures to said polyvinylchloride foam plastic preform and steps (c) and (f) achieving expansion under light pressure.
Claim 2
Dependent Claim 216 words
The process for the production of a closed-cell, extra soft polyvinylchloride foam plastic product having improved volume stability at elevated temperatures which comprises (a) heating a plastisol or plastigel comprised of a plasticizer- and a foaming agent-containing polyvinyl chloride or vinylchloride copolymerizate in a pressure mold at a pressure of up to 300 atm. to a temperature of 150° to 180° C., (b) cooling said plastigel or plastisol, at an unchanged closing force of the press or said pressure mold, to a temperature of 20° to 70° C., (c) removing said cooled plastigel or plastisol from said pressure mold as a crude foam plastic preform, (d) heating said crude foam plastic preform under a gas pressure of 2 to 10 atm. to a temperature of 140° to 170° C., (e) cooling said crude foam plastic preform at said pressure of 2 to 10 atm. to a temperature of 100° to 130° C., and (f) lowering said pressure to atmospheric pressure, said foam plastic preform simultaneously expanding to form said closed-cell extra soft polyvinyl chloride product, step (a) achieving gelation and the decomposition of the foaming agent, step (d) imparting said extra softness and said improved volume stability at elevated temperatures to said polyvinylchloride foam plastic preform and steps (c) and (f) achieving expansion under light pressure.
Claim 3
Dependent Claim 41 words
The process of claim 1 wherein the copolymerizable monomer forming said copolymerizate with said vinyl chloride or said polyvinyl chloride is a vinyl ester, an acrylic acid ester, a methacrylic ester, an olefin or a chlorinated monomer other than vinyl chloride.
Claim 4
Dependent Claim 12 words
The process of claim 1 wherein the starting material is a plastisol.
Claim 5
Dependent Claim 20 words
The process of claim 1 wherein said heating of step (a) is to a temperature of 160° to 170° C.
Claim 6
Dependent Claim 23 words
The process of claim 1 wherein, after heating step (a) is effected, said temperature and pressure being maintained for 1 to 2 hours.
Claim 7
Dependent Claim 18 words
The process of claim 1 wherein a pressure of 100° to 200° C. is achieved in step (a).
Claim 8
Dependent Claim 20 words
The process of claim 1 wherein said cooling of step (b) is to a temperature of 30° to 50° C.
Claim 9
Dependent Claim 20 words
The process of claim 1 wherein said heating of step (d) is to a temperature of 150° to 160° C.
Claim 10
Dependent Claim 21 words
The process of claim 1 wherein after heating step (d) is effected, said temperature being maintained for 0.5 to 1 hour.
Claim 11
Dependent Claim 28 words
The process of claim 1 wherein said pressure in step (d) is achieved by means of air and wherein said step (d) is achieved in a pressure vessel.
Claim 12
Dependent Claim 23 words
The process of claim 10 wherein steam is introduced into said pressure vessel to obtain a relative humidity of 10 to 40 percent.
Claim 13
Dependent Claim 30 words
The process of claim 1 wherein, in step (a), said plastisol is filled into said pressure mold in the form of a heavy foam, obtained by mechanical beating in air.
Claim 14
Dependent Claim 28 words
The process of claim 1 wherein said crude foam plastic preform obtained from step (c) is split and said split pieces are subjected to steps (d) to (f).
Claim 15
Dependent Claim 25 words
The process of claim 1 wherein, in step (a), said pressure mold is completely filled with said plastisol or plastigel before said heating is started.
Claim 16
Dependent Claim 15 words
The process of claim 1 wherein more than one of said pressure molds are used.

References Cited (Backward Citations)

US2768407A Cited
US2590156A Cited
US2525965A Cited
US2525880A Cited
US2498074A Cited
US2751627A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-03-13 1981-09-12 1982-03-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-03-13 1985-09-12 1986-03-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-03-13 1989-09-12 1990-03-14 $7700.00 Window Closed / Lapsed

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