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US3725520A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for preparing a porous synthetic thermoplastic film or sheet

Assignee: Sanyo Kokusaku Pulp Co Ltd
•
Filing: 1970-04-24
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Granted: 1973-04-03
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Expires: 1990-04-24
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Abstract

Abstract A method for preparing a porous film or sheet, which comprises admixing together 100 parts by volume of at least one thermoplastic resin, 5 - 150 parts by volume of a solvent, and 20-50 parts by volume of a filler, uniformly dispersing the solvent and the filler in said resin to thereby form a stock, molding a film or sheet from the resulting stock, biaxially stretching the film or sheet at a suitable temperature between the glass transition temperature of the resin and the flow temperature of the resin, and substantially removing the solvent from the film or sheet during the period between the molding and the end of the stretching without foaming.

Inventors

  • 👤 S Suzuki
  • 👤 K Nakamura

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 10:05
CPC Classifications
B; B29; B29C; B29C55/00; B29C55/02; B29C55/10; B29C55/12; B29C67/00; B29C67/20; B29C67/202; C; C08; C08J; C08J9/00; C08J9/28; D; D01; D01F; D01F1/00; D01F1/02; D01F1/10; C08J2201/00; C08J2201/04; C08J2201/05; C08J2201/0502; Y; Y10; Y10S; Y10S264/00; Y10S264/13; Y10S264/17; Y10S264/62; Y10S428/00; Y10S428/91

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 204 words
A method for preparing a porous film or sheet, whIch comprises: A. admixing together: 100 parts by volume of at least one thermoplastic resin, 5-150 parts by volume of a solvent, and 20-50 parts by volume of a filler, B. uniformly dispersing the solvent and the filler in said resin to thereby form a stock, C. molding a film or sheet from the resulting stock, D. biaxially stretching the film or sheet at a suitable temperature between the glass transition temperature of the resin and the flow temperature of the resin, and E. substantially entirely removing the solvent from the film or sheet during the period between the molding and the end of the stretching without foaming, the aforesaid steps being further characterized by the facts that: a. said at least one thermoplastic resin is selected from the group consisting of polyolefins, polyvinyls, polyamides, and polyesters, b. said solvent has a boiling point between 100* and 230*C., c. said solvent is incapable of completely dissolving the resin of (a) at the temperature of molding step (C), but capable of partially swelling the resin, d. said filler is inert to the resin of (a), and e. said filler is stable at the temperature of molding.
Claim 2
Dependent Claim 52 words
a solvent mixture containing at least 60 percent by volume of xylene with the balance being a solvent selected from the group consisting of chlorobenzene, dichlorobenzene, ethylbenzene, diethyl-benzene, decalin, tetralin, terpene oil, chlorinated hydrocarbons having a boiling point of 100* - 230*C and a mixture of at least two of these solvents,
Claim 3
Dependent Claim 98 words
A method according to claim 2 wherein said thermoplastic resin is a polyolefin and said solvent is selected from the group consisting of (a) petroleum- and coal- naphtha containing at least 50 percent by volume of aromatic components and having a boiling point of 160*-230*C and (b) a solvent mixture containing at least 60 percent by volume of xylene, with the balance being a solvent selected from the group consisting of chlorobenzene, dichlorobenzene, ethylbenzene, diethylbenzene, decalin, tetralin, terpene oil, chlorinated hydrocarbons having a boiling point of 100* -230*C and a mixture of at least two of these solvents.
Claim 4
Dependent Claim 62 words
a solvent mixture containing at least 70 percent by volume of a solvent from the group of petroleum naphtha, coal naphtha having a boiling point of 150*-230*C., xylene and a mixture of these two solvents with the balance being a solvent selected from the group consisting of cyclohexanone, nitrobenzene, diacetone alcohol and a mixture of at least two of these compounds and
Claim 5
Dependent Claim 93 words
water, c. said solvent is incapable of completely dissolving the resin of (a) at the temperature of molding step (C), but capable of partially swelling the resin, d. said filler is inert to the resin of (a) and stable at the temperature of molding and comprises at least one member selected from the group consisting of calcium carbonate, magnesium carbonate, barium sulfate, powdered silica, mica, kaolin, clay, diatomaceous earth, talc, gypsum, asbestos, rock wool, alumina, aluminum hydroxide, powdered glass, glass fiber, white carbon, titanium dioxide, pulp floc,wood sawdust, and synthetic polymer short fibers.
Claim 6
Dependent Claim 84 words
A method according to claim 2 wherein said thermoplastic resin is a polyvinyl resin and said solvent is selected from mixtures containing at least 70 percent by volume of a solvent selected from the group consisting of petroleum-and coal-naphtha having a boiling point of 150* - 230*C, xylene and a mixture of at least two of these solvents, with the remainder being a solvent selected from the group consisting of cyclohexanone, nitrobenzene, diacetone alcohol and a mixture of at least two of these compounds.
Claim 7
Dependent Claim 35 words
A method according to claim 2 wherein said thermoplastic resin is polystrene and said solvent is selected from the group consisting of petroleum- and coal- solvent naphtha having a boiling point of 130* - 230*C.
Claim 8
Dependent Claim 58 words
A method according to claim 2, wherein the filler is at least one member selected from the group consisting of calcium carbonate, magnesium carbonate, barium sulfate, powdered silica, mica, kaolin, clay, diatomaceous earth, talc, gypsum, asbestos, rock wool, alumina, aluminum hydroxide, powdered glass, glass fiber, white carbon, titanium dioxide, pulp floc, wood sawdust, and synthetic polymer short fibers.
Claim 9
Dependent Claim 43 words
A method according to claim 2 wherein the biaxially stretched air-permeable film or sheet is thereafter coated with a final thermoplastic polymeric resin having a higher Young''s modulus than that of the thermoplastic polymeric resin that was used to form the stretched film.
Claim 10
Dependent Claim 14 words
A method according to claim 7 wherein said final thermoplastic polymeric resin is polystyrene.
Claim 11
Dependent Claim 15 words
A method according to claim 7 wherein said final thermoplastic polymeric resin is polyvinyl alcohol.
Claim 12
Dependent Claim 18 words
A method according to claim 6 wherein said final thermoplastic polymeric resin is admixed with an antistatic agent.
Claim 13
Dependent Claim 14 words
A method according to claim 10 wherein said antistatic agent is an anionic surfactant.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-04-02 1976-10-02 1977-04-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-04-02 1980-10-02 1981-04-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-04-02 1984-10-02 1985-04-03 $7700.00 Window Closed / Lapsed

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