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US5997781A Expired / Lapsed US ⏱️ 0.0 years remaining

Injection-expansion molded, thermoplastic resin product and production process thereof

Assignee: Mitsui Chemicals Inc
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Filing: 1997-03-31
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Granted: 1999-12-07
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Expires: 2017-03-31
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Abstract

Abstract Disclosed is a process for the production of an injection-expansion molded, thermoplastic resin product. The process comprises a gas dissolving step, a cooling step, a metering and injection step, and an expansion controlling step. Specifically, a thermoplastic resin is molten in a continuous plasticator (1), supercritical carbon dioxide and/or nitrogen is added as a blowing agent, and the blowing agent and the thermoplastic resin are formed into a mutually-dissolved state. The resultant molten resin composition is cooled within the plasticator while maintaining a pressure equal to or higher than a critical pressure of the blowing agent. The thus-cooled molten resin composition is metered by an injector (7) and is filled in a mold (8). An internal pressure of the mold is lowered beyond the critical pressure of the blowing agent to produce cell nuclei, whereby the cell diameter is controlled. The blowing agent is maintained in a supercritical state up to the metering and injection step.

Inventors

  • 👤 Shigeo Nishikawa
  • 👤 Kaoru Yorita
  • 👤 Kouzo Ichikawa
  • 👤 Haruo Inoue
  • 👤 Michio Eriguchi
  • 👤 Takanori Sueda
  • 👤 Hideo Amemiya

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 18:21
CPC Classifications
B; B29; B29C; B29C44/00; B29C44/34; B29C44/3469; B29C44/348; C; C08; C08J; C08J9/00; C08J9/04; B29C44/02; B29C44/04; B29C44/0415; B29C44/36; B29C44/38; B29C44/42; B29C44/421; C08J9/12; C08J9/122; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/54; Y10; Y10S; Y10S264/00; Y10S264/13

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 317 words
A process for the production of the injection-expansion molded, thermoplastic resin product comprising an expanded portion as an inner layer and an unexpanded portion as a surface layer, said expanded portion having an average cell diameter of from 0.01 to 50 μm and an average cell population of from 10 8 to 10 16 cells/cm 3 , and said unexpanded portion having a thickness of from 10 to 1,000 μm and integrated with said expanded portion, said process comprising: (I) as a gas dissolving step, melting 100 parts by weight of a thermoplastic resin at 100 to 450° C. in a continuous plasticator equipped with a feed line for a blowing agent, adding supercritical carbon dioxide and/or nitrogen in a proportion of 0.1 to 30 parts by weight per 100 parts by weight of said thermoplastic resin, and forming a molten resin composition in which said thermoplastic resin and said supercritical carbon dioxide and/or nitrogen are in mutually-dissolved state; (II) as a cooling step, cooling, within said continuous plasticator, said molten resin composition to a temperature of from 50 to 300° C. while maintaining a pressure equal to or higher than a critical pressure of said carbon dioxide and/or nitrogen; (III) as a metering and injection step, metering the thus-cooled molten resin composition by an injector, which is connected to said continuous plasticator and equipped with an injection plunger, and filling the same in a mold; and (IV) as an expansion controlling step, lowering an internal pressure of said mold to a pressure lower than said critical pressure of said carbon dioxide and/or nitrogen to produce cell nuclei, whereby said cell diameter is controlled; wherein said carbon dioxide and/or nitrogen are maintained in a supercritical state up to said metering and injection step, and said gas dissolving step and cooling step by said continuous plasticator and said metering and injection step by said injector are conducted independently.
Claim 2
Dependent Claim 317 words
A process for the production of the injection-expansion molded, thermoplastic resin product comprising an expanded portion as an inner layer and an unexpanded portion as a surface layer, said expanded portion having an average cell diameter of from 0.01 to 50 μm and an average cell population of from 10 8 to 10 16 cells/cm 3 , and said unexpanded portion having a thickness of from 10 to 1,000 μm and integrated with said expanded portion, said process comprising: (I) as a gas dissolving step, melting 100 parts by weight of a thermoplastic resin at 100 to 450° C. in a continuous plasticator equipped with a feed line for a blowing agent, adding supercritical carbon dioxide and/or nitrogen in a proportion of 0.1 to 30 parts by weight per 100 parts by weight of said thermoplastic resin, and forming a molten resin composition in which said thermoplastic resin and said supercritical carbon dioxide and/or nitrogen are in mutually-dissolved state; (II) as a cooling step, cooling, within said continuous plasticator, said molten resin composition to a temperature of from 50 to 300° C. while maintaining a pressure equal to or higher than a critical pressure of said carbon dioxide and/or nitrogen; (III) as a metering and injection step, metering the thus-cooled molten resin composition by an injector, which is connected to said continuous plasticator and equipped with an injection plunger, and filling the same in a mold; and (IV) as an expansion controlling step, lowering an internal pressure of said mold to a pressure lower than said critical pressure of said carbon dioxide and/or nitrogen to produce cell nuclei, whereby said cell diameter is controlled; wherein said carbon dioxide and/or nitrogen are maintained in a supercritical state up to said metering and injection step, and said gas dissolving step and cooling step by said continuous plasticator and said metering and injection step by said injector are conducted independently.
Claim 3
Dependent Claim 62 words
The process of claim 1, wherein between said continuous plasticator equipped with said feed line for said blowing agent and said injector equipped with said injection plunger, an adapter having a mixing portion is arranged so that said adapter is connected to a delivery path of said continuous plasticator, said delivery path being selectively connected to said injector via an on-off valve.
Claim 4
Dependent Claim 19 words
The process of claim 1, wherein said process produces an expanded product of 0.5 to 50 mm in thickness.
Claim 5
Dependent Claim 19 words
The process of claim 1, wherein said process produces an expanded product of 10 to 50 mm in thickness.
Claim 6
Dependent Claim 47 words
The process of claim 1, wherein said expansion control step is conducted by removing a high-pressure gas, which has been filled in said mold subsequent to the injection of said molten resin composition, and/or causing at least a portion of a core of said mold to retreat.
Claim 7
Dependent Claim 27 words
The process of claim 1, wherein a foam stabilizer is added further in a proportion of form 0.1 to 10 parts by weight to said thermoplastic resin.
Claim 8
Dependent Claim 51 words
The process of claim 1, wherein between said continuous plasticator equipped with said feed line for said blowing agent and said injector equipped with said injection plunger, a resin accumulator equipped with a plunger is arranged so that said resin accumulator is selectively connected to said injector via an on-off valve.
Claim 9
Dependent Claim 45 words
The process of claim 7, wherein between an adapter having a mixing portion and said injector equipped with said injection plunger, said resin accumulator equipped with said plunger is arranged so that said resin accumulator is selectively connected to said injector via said on-off valve.
Claim 10
Dependent Claim 35 words
The process of claim 1 wherein said expanded portion has an average cell diameter ranging from 0.01 to 20 μm and an average cell population ranging from 10 8 to 10 14 cells/cm 3 .

References Cited (Backward Citations)

US4473665A Cited
DE3436361A1 Cited
US4761256A Cited
US5075162A Cited
US5158986A Cited
JPH0811190A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 2002-12-06 2003-06-07 2003-12-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2006-12-06 2007-06-07 2007-12-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2010-12-06 2011-06-07 2011-12-07 $7700.00 Window Closed / Lapsed

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