JP2023109594A - Foamed vinyl chloride resin sheet and manufacturing method thereof - Google Patents

Foamed vinyl chloride resin sheet and manufacturing method thereof Download PDF

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JP2023109594A
JP2023109594A JP2022011186A JP2022011186A JP2023109594A JP 2023109594 A JP2023109594 A JP 2023109594A JP 2022011186 A JP2022011186 A JP 2022011186A JP 2022011186 A JP2022011186 A JP 2022011186A JP 2023109594 A JP2023109594 A JP 2023109594A
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vinyl chloride
chloride resin
foamed
mass
resin
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千典 藤原
Kazunori Fujiwara
誠司 織田
Seiji Oda
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Shin Dai Ichi Vinyl Corp
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Abstract

【課題】発泡特性に優れると共に、引張強度、伸び性などの機械物性に優れた発泡塩化ビニル系樹脂シート、及びその製造方法を提供すること。
【解決手段】塩化ビニル系樹脂と、SP値が7.5~11.0の弾性樹脂と、可塑剤とを含み、前記弾性樹脂が、前記塩化ビニル系樹脂及び弾性樹脂の合計量100質量部に対して0.8~16質量部含まれる発泡塩化ビニル系樹脂シート、及びその製造方法である。
【選択図】なし
An object of the present invention is to provide a foamed vinyl chloride resin sheet having excellent foaming characteristics and mechanical properties such as tensile strength and extensibility, and a method for producing the same.
The elastic resin contains a vinyl chloride resin, an elastic resin having an SP value of 7.5 to 11.0, and a plasticizer, and the elastic resin is 100 parts by mass in total of the vinyl chloride resin and the elastic resin. It is a foamed vinyl chloride resin sheet containing 0.8 to 16 parts by mass per 100 parts, and a method for producing the same.
[Selection figure] None

Description

本発明は、発泡塩化ビニル系樹脂シート及びその製造方法に関する。 TECHNICAL FIELD The present invention relates to a foamed vinyl chloride resin sheet and a method for producing the same.

発泡塩化ビニル系樹脂シートは、壁紙(壁材)、タイルカーペット(床材)等の建築資材や、ブックカバー等の文具といった様々な用途で用いられている。このような発泡塩化ビニル系樹脂シートを備えた壁紙に関して、その機能性向上を目的として種々の提案がなされている(特許文献1~3参照)。 Foamed vinyl chloride resin sheets are used in various applications such as wallpaper (wall material), building materials such as tile carpet (floor material), and stationery such as book covers. Various proposals have been made for wallpaper comprising such a foamed vinyl chloride resin sheet for the purpose of improving its functionality (see Patent Documents 1 to 3).

特開2006-187928号公報Japanese Patent Application Laid-Open No. 2006-187928 特開2003-301385号公報Japanese Patent Application Laid-Open No. 2003-301385 特開2014-109087号公報JP 2014-109087 A

壁紙等の建築資材においては、下地の収縮、ずれ、歪みによって生じるひび割れを防止できるような機械的強度が求められている。また、ブックカバー等の文具においても、優れた機械的強度が求められている。 Building materials such as wallpaper are required to have a mechanical strength that can prevent cracks caused by shrinkage, displacement, and distortion of the substrate. Stationery such as book covers are also required to have excellent mechanical strength.

本発明の課題は、発泡特性に優れると共に、引張強度、伸び性などの機械物性に優れた発泡塩化ビニル系樹脂シート、及びその製造方法を提供することにある。 An object of the present invention is to provide a foamed vinyl chloride resin sheet having excellent foaming characteristics and mechanical properties such as tensile strength and elongation, and a method for producing the same.

本発明者らは、発泡塩化ビニル系樹脂シートの機械的強度を向上させるべく、塩化ビニル系樹脂にフッ素ゴム(FKM)等の弾性樹脂を配合することを試みたが、十分な発泡特性が得られないといった問題や、期待した機械物性が得られないといった問題に直面した。
本発明者らはさらに鋭意研究した結果、塩化ビニル系樹脂に、特定のSP値を有する弾性樹脂を所定の割合で配合することにより、発泡塩化ビニル系樹脂シートの十分な発泡特性を維持しつつ、引張強度、伸び性などの機械物性を向上させることができることを見いだし、本発明を完成するに至った。さらに、本発明者らは、特定のSP値を有する弾性樹脂を所定の割合で配合することにより、発泡塩化ビニル系樹脂シートが優れた応力緩和性を発揮することを見いだした。
In order to improve the mechanical strength of the foamed vinyl chloride resin sheet, the present inventors tried to blend an elastic resin such as fluororubber (FKM) into the vinyl chloride resin, but sufficient foaming characteristics were obtained. We faced problems such as being unable to obtain the expected mechanical properties.
As a result of further intensive research by the present inventors, it was found that by blending an elastic resin having a specific SP value with a vinyl chloride resin at a predetermined ratio, it is possible to maintain sufficient foaming characteristics of the foamed vinyl chloride resin sheet. , tensile strength, elongation and other mechanical properties can be improved, and have completed the present invention. Furthermore, the present inventors have found that a foamed vinyl chloride resin sheet exhibits excellent stress relaxation properties by blending an elastic resin having a specific SP value at a predetermined ratio.

すなわち、本発明は、以下の通りのものである。
[1]塩化ビニル系樹脂と、SP値が7.5~11.0の弾性樹脂と、可塑剤とを含み、前記弾性樹脂が、前記塩化ビニル系樹脂及び弾性樹脂の合計量100質量部に対して0.8~16質量部含まれることを特徴とする発泡塩化ビニル系樹脂シート。
That is, the present invention is as follows.
[1] Contains a vinyl chloride resin, an elastic resin having an SP value of 7.5 to 11.0, and a plasticizer, and the elastic resin is contained in a total amount of 100 parts by mass of the vinyl chloride resin and the elastic resin. A foamed vinyl chloride resin sheet characterized by containing 0.8 to 16 parts by mass.

[2]前記塩化ビニル系樹脂の粘度平均重合度が450~1800であることを特徴とする上記[1]に記載の発泡塩化ビニル系樹脂シート。
[3]前記弾性樹脂が、ブタジエン系ゴム、熱可塑性ポリウレタン、クロロプレンゴム、及び塩素化ポリエチレンから選択される少なくとも一種であることを特徴とする上記[1]又は[2]に記載の発泡塩化ビニル系樹脂シート。
[2] The foamed vinyl chloride resin sheet according to [1] above, wherein the vinyl chloride resin has a viscosity average degree of polymerization of 450 to 1,800.
[3] The foamed vinyl chloride according to [1] or [2] above, wherein the elastic resin is at least one selected from butadiene rubber, thermoplastic polyurethane, chloroprene rubber, and chlorinated polyethylene. based resin sheet.

[4]上記[1]~[3]のいずれか一項に記載の発泡塩化ビニル系樹脂シートを製造する方法であって、塩化ビニル系樹脂と、SP値が7.5~11.0の弾性樹脂と、可塑剤とを混練し、得られた混練物をシート成型した後、得られたシートを発泡させることを特徴とする発泡塩化ビニル系樹脂シートの製造方法。
[5]前記のシート成型が、カレンダー成型であることを特徴とする上記[4]に記載の発泡塩化ビニル系樹脂シートの製造方法。
[4] A method for producing a foamed vinyl chloride resin sheet according to any one of the above [1] to [3], comprising a vinyl chloride resin and an SP value of 7.5 to 11.0 A method for producing a foamed vinyl chloride resin sheet, which comprises kneading an elastic resin and a plasticizer, molding the resulting kneaded product into a sheet, and then foaming the obtained sheet.
[5] The method for producing a foamed vinyl chloride resin sheet according to [4] above, wherein the sheet molding is calendar molding.

本発明の発泡塩化ビニル系樹脂シートは、発泡特性に優れると共に、引張強度、伸び性などの機械物性に優れる。 The foamed vinyl chloride resin sheet of the present invention is excellent in foaming characteristics and mechanical properties such as tensile strength and elongation.

[発泡塩化ビニル系樹脂シート]
本発明の発泡塩化ビニル系樹脂シートは、塩化ビニル系樹脂と、SP値が7.5~11.0である弾性樹脂(以下、単に弾性樹脂という)と、可塑剤とを含み、弾性樹脂が、塩化ビニル系樹脂及び弾性樹脂の合計量100質量部に対して0.8~16質量部含まれる。
[Foamed vinyl chloride resin sheet]
The foamed vinyl chloride resin sheet of the present invention contains a vinyl chloride resin, an elastic resin having an SP value of 7.5 to 11.0 (hereinafter simply referred to as an elastic resin), and a plasticizer. , 0.8 to 16 parts by mass per 100 parts by mass of the total amount of vinyl chloride resin and elastic resin.

本発明の発泡塩化ビニル系樹脂シートは、連続又は不連続の空隙部を有する発泡性シートであり、空隙率が例えば50%以上のものをいい、好ましくは55%以上のものをいう。また、シート厚が、例えば0.1~10.0mm程度のものをいう。 The foamed vinyl chloride resin sheet of the present invention is a foamed sheet having continuous or discontinuous voids, and has a porosity of, for example, 50% or more, preferably 55% or more. Also, the thickness of the sheet is, for example, about 0.1 to 10.0 mm.

本発明の発泡塩化ビニル系樹脂シートは、塩化ビニル系樹脂と相溶性のよい弾性樹脂を含むことから、発泡特性に優れると共に、引張強度、伸び性などの機械物性に優れる。したがって、壁紙や床材等の建築資材や、ブックカバー等の文具において有用である。具体的に、本発明の発泡塩化ビニル系樹脂は、発泡倍率、発泡セル緻密性に優れ、また表面平滑性にも優れる。また、引張強度、伸び性が向上し、表面強度も高いものとなる。さらに、本発明の発泡塩化ビニル系樹脂シートは、応力緩和性に優れる。すなわち、エンボス加工後のエンボス戻りが小さく、優れた形状保持性(柄保持性)を示すため、例えば、壁紙や床材用途に好適である。 The foamed vinyl chloride-based resin sheet of the present invention contains an elastic resin that is highly compatible with vinyl chloride-based resins, so that it has excellent foaming properties and excellent mechanical properties such as tensile strength and extensibility. Therefore, it is useful for building materials such as wallpaper and flooring, and stationery such as book covers. Specifically, the foamed vinyl chloride resin of the present invention is excellent in expansion ratio and foam cell denseness, and is also excellent in surface smoothness. In addition, the tensile strength and elongation are improved, and the surface strength is also increased. Furthermore, the foamed vinyl chloride resin sheet of the present invention is excellent in stress relaxation. That is, since the embossing reversion after embossing is small and excellent shape retention (pattern retention) is exhibited, it is suitable for wallpaper and floor materials, for example.

(塩化ビニル系樹脂)
本発明における塩化ビニル系樹脂としては、サスペンジョン系塩化ビニル系樹脂、ペースト加工用塩化ビニル系樹脂等を挙げることができ、サスペンジョン系塩化ビニル系樹脂が好ましい。これらは、併用してもよい。
(vinyl chloride resin)
Examples of vinyl chloride-based resins in the present invention include suspension-based vinyl chloride-based resins, vinyl chloride-based resins for paste processing, and the like, and suspension-based vinyl chloride-based resins are preferable. These may be used in combination.

(サスペンジョン系塩化ビニル系樹脂)
サスペンジョン系塩化ビニル系樹脂としては、塩化ビニルのホモポリマーの他、塩化ビニルを主体とする共重合体であってもよい。塩化ビニルを主体とするとは、例えば、塩化ビニルが全体の50質量%以上であることをいい、70質量%以上であることが好ましく、90質量%以上であることがより好ましい。
(Suspension vinyl chloride resin)
The suspension vinyl chloride resin may be a homopolymer of vinyl chloride or a copolymer mainly composed of vinyl chloride. Mainly composed of vinyl chloride means, for example, that vinyl chloride accounts for 50% by mass or more of the whole, preferably 70% by mass or more, and more preferably 90% by mass or more.

塩化ビニルと共重合し得る単量体としては、例えば、エチレン、プロピレン等のオレフィン系化合物;酢酸ビニル、プロピオン酸ビニル等のビニルエステル;アクリル酸、メタクリル酸等の不飽和モノカルボン酸;アクリル酸メチル、アクリル酸エチル、アクリル酸-n-ブチル、アクリル酸-2-ヒドロキシエチル、メタクリル酸メチル、メタクリル酸エチル、メタクリル酸-N,N-ジメチルアミノエチル等の不飽和モノカルボン酸エステル;アクリルアミド、メタクリルアミド等の不飽和アミド;アクリロニトリル、メタクリロニトリル等の不飽和ニトリル;マレイン酸、フマル酸等の不飽和ジカルボン酸;これらのエステルおよびこれらの無水物;N-置換マレイミド類;ビニルメチルエーテル、ビニルエチルエーテル等のビニルエーテル;塩化ビニリデン等のビニリデン化合物等を挙げることができる。 Examples of monomers copolymerizable with vinyl chloride include olefin compounds such as ethylene and propylene; vinyl esters such as vinyl acetate and vinyl propionate; unsaturated monocarboxylic acids such as acrylic acid and methacrylic acid; unsaturated monocarboxylic acid esters such as methyl, ethyl acrylate, n-butyl acrylate, 2-hydroxyethyl acrylate, methyl methacrylate, ethyl methacrylate, and -N,N-dimethylaminoethyl methacrylate; acrylamide, Unsaturated amides such as methacrylamide; Unsaturated nitriles such as acrylonitrile and methacrylonitrile; Unsaturated dicarboxylic acids such as maleic acid and fumaric acid; Esters thereof and anhydrides thereof; N-substituted maleimides; vinyl ethers such as vinyl ethyl ether; vinylidene compounds such as vinylidene chloride;

サスペンジョン系塩化ビニル系樹脂は、ペースト加工用塩化ビニル系樹脂よりも粒子径が大きく、通常、平均粒子径(D50)が50~200μmの粒子である。平均粒子径(D50)は、70~180μmであることが好ましく、100~150μmであることがより好ましい。この平均粒子径(D50)は、JIS Z8815(乾式ふるい分け試験法)により、JIS Z8801のふるいを用いた50%通過径として示す。 The suspension vinyl chloride resin has a larger particle size than the vinyl chloride resin for paste processing, and usually has an average particle size (D50) of 50 to 200 μm. The average particle size (D50) is preferably 70-180 μm, more preferably 100-150 μm. This average particle diameter (D50) is indicated as a 50% passing diameter using a JIS Z8801 sieve according to JIS Z8815 (dry sieving test method).

サスペンジョン系塩化ビニル系樹脂の粘度平均重合度は、450~1800であることが好ましく、700~1800であることがより好ましく、800~1500であることがさらに好ましい。この範囲の重合度であることにより、本発明の効果を有効に発揮することができる。
平均重合度は、塩化ビニル樹脂試験法(2003年4月 塩ビ工業・環境協会発行)の測定方法に従い、JIS K7367-2に準拠して測定した還元粘度(K値)を、近似式:K値=20.42×Ln(重合度)-74.93で換算する。
The viscosity-average degree of polymerization of the suspension vinyl chloride resin is preferably 450-1800, more preferably 700-1800, even more preferably 800-1500. By setting the degree of polymerization within this range, the effects of the present invention can be effectively exhibited.
The average degree of polymerization is the reduced viscosity (K value) measured in accordance with JIS K7367-2 according to the vinyl chloride resin test method (published by the PVC Industry and Environment Association, April 2003), and the approximate expression: K value. = 20.42 x Ln (degree of polymerization) - 74.93.

サスペンジョン系塩化ビニル系樹脂は、多孔質であり、そのポロシティ(細孔容積)は、例えば0.05~0.45ml/gであり、0.10~0.40ml/gであることが好ましく、0.15~0.35ml/gであることがより好ましい。
ポロシティは、水銀圧入法(ポロシメーター)により求めることができる。
The suspension vinyl chloride resin is porous, and its porosity (pore volume) is, for example, 0.05 to 0.45 ml/g, preferably 0.10 to 0.40 ml/g, More preferably 0.15 to 0.35 ml/g.
Porosity can be determined by a mercury intrusion method (porosimeter).

本発明のサスペンジョン系塩化ビニル系樹脂は、塩化ビニル単独で、又は塩化ビニルとこれと共重合可能な不飽和単量体とからなる単量体混合物を従来公知の方法で重合することにより得ることができる。例えば、懸濁重合により得ることができる。温度、分散剤の種類や量、撹拌速度等の各種反応条件を適宜設定して、所望の重合度やポロシティの樹脂を得ることができる。 The suspension vinyl chloride resin of the present invention is obtained by polymerizing vinyl chloride alone or a monomer mixture comprising vinyl chloride and an unsaturated monomer copolymerizable therewith by a conventionally known method. can be done. For example, it can be obtained by suspension polymerization. By appropriately setting various reaction conditions such as temperature, type and amount of dispersant, and stirring speed, a resin having a desired degree of polymerization and porosity can be obtained.

(ペースト加工用塩化ビニル系樹脂)
ペースト加工用塩化ビニル系樹脂としては、サスペンジョン系塩化ビニル系樹脂と同様、塩化ビニルのホモポリマーの他、塩化ビニルを主体とする共重合体が含まれる。
(Vinyl chloride resin for paste processing)
Vinyl chloride resins for paste processing include homopolymers of vinyl chloride and copolymers mainly composed of vinyl chloride, as in suspension vinyl chloride resins.

ペースト加工用塩化ビニル系樹脂は、通常、サスペンジョン系塩化ビニル系樹脂よりも粒子径が小さく、一次粒子の平均粒子径(D50)が0.1~10μmの微粒子である。平均粒子径(D50)は、0.1~5.0μmであることが好ましく、0.5~3.0μmであることがより好ましい。
この平均粒子径(D50)は、体積基準で求めた粒度分布の全体積を100%とした累積体積分布曲線において50%となる点の粒子径、すなわち体積基準累積50%径を意味する。粒度分布は、レーザー回折/散乱式粒子径分布測定装置(例えば(株)堀場製作所製LA-960)により求めることができる。
Vinyl chloride resins for paste processing are usually fine particles having a particle size smaller than that of suspension vinyl chloride resins and having an average primary particle size (D50) of 0.1 to 10 μm. The average particle diameter (D50) is preferably 0.1-5.0 μm, more preferably 0.5-3.0 μm.
The average particle size (D50) means the particle size at the 50% point in the cumulative volume distribution curve with the total volume of the particle size distribution determined on a volume basis as 100%, that is, the volume-based cumulative 50% diameter. The particle size distribution can be determined by a laser diffraction/scattering particle size distribution analyzer (eg LA-960 manufactured by Horiba, Ltd.).

ペースト加工用塩化ビニル系樹脂の粘度平均重合度は、450~1800であることが好ましく、700~1800であることがより好ましく、800~1500であることがさらに好ましい。この範囲の重合度であることにより、本発明の効果を有効に発揮することができる。
この粘度平均重合度は、サスペンジョン系塩化ビニル系樹脂の場合と同様に算出する。
The viscosity average degree of polymerization of the vinyl chloride resin for paste processing is preferably 450-1800, more preferably 700-1800, even more preferably 800-1500. By setting the degree of polymerization within this range, the effects of the present invention can be effectively exhibited.
This viscosity-average degree of polymerization is calculated in the same manner as in the case of the suspension vinyl chloride resin.

本発明のペースト加工用塩化ビニル系樹脂は、塩化ビニル単独で、又は塩化ビニルとこれと共重合可能な不飽和単量体とからなる単量体混合物を従来公知の方法で重合することにより得ることができる。例えば、乳化重合(播種乳化重合を含む)により得ることができる。 The vinyl chloride resin for paste processing of the present invention is obtained by polymerizing vinyl chloride alone or a monomer mixture comprising vinyl chloride and an unsaturated monomer copolymerizable therewith by a conventionally known method. be able to. For example, it can be obtained by emulsion polymerization (including seeded emulsion polymerization).

(弾性樹脂)
本発明における弾性樹脂は、上記のように、SP値が7.5~11.0である弾性樹脂である。SP値がこの範囲から外れる弾性樹脂の場合、発泡セルの緻密性、表面平滑性が悪化すると共に、ゴム弾性が発現し、エンボス性が悪化する。すなわち、本発明におけるSP値の弾性樹脂は、塩化ビニル系樹脂と良好に相溶するため、塩化ビニル系樹脂の優れた発泡特性を維持できると共に、弾性樹脂の特徴であるゴム的性質(エンボス戻り性)を抑制して、塩化ビニル系樹脂の優れた応力緩和性を維持することができる。SP値は、8.0~10.5であることが好ましい。
(elastic resin)
The elastic resin in the present invention is an elastic resin having an SP value of 7.5 to 11.0 as described above. In the case of an elastic resin having an SP value outside this range, the density of foamed cells and surface smoothness are deteriorated, rubber elasticity is exhibited, and embossability is deteriorated. That is, since the elastic resin having the SP value in the present invention is well compatible with the vinyl chloride resin, it is possible to maintain the excellent foaming properties of the vinyl chloride resin, and to properties) can be suppressed to maintain the excellent stress relaxation properties of vinyl chloride resins. The SP value is preferably 8.0-10.5.

具体的に、弾性樹脂としては、例えば、アクリルニトリル・ブタジエン系ゴム(NBR)、スチレン・ブタジエン系ゴム(SBR)等のブタジエン系ゴム;熱可塑性ポリウレタン(TPU);ポリエステル系熱可塑性エラストマー(TPC);クロロプレンゴム(CR);アクリルゴム(ACM);クロロスルホン化ポリエチレン(CSM);塩素化ポリエチレン(CPE)が挙げられる。これらの中でも、ブタジエン系ゴム、熱可塑性ポリウレタン、クロロプレンゴム、塩素化ポリエチレンが好ましく、アクリルニトリル・ブタジエン系ゴムが特に好ましい。これらは、2種以上併用してもよい。 Specific examples of elastic resins include butadiene-based rubbers such as acrylonitrile-butadiene-based rubbers (NBR) and styrene-butadiene-based rubbers (SBR); thermoplastic polyurethanes (TPU); polyester-based thermoplastic elastomers (TPC). chloroprene rubber (CR); acrylic rubber (ACM); chlorosulfonated polyethylene (CSM); chlorinated polyethylene (CPE). Among these, butadiene-based rubber, thermoplastic polyurethane, chloroprene rubber, and chlorinated polyethylene are preferred, and acrylonitrile-butadiene-based rubber is particularly preferred. These may be used in combination of two or more.

本発明の発泡塩化ビニル系樹脂シートにおける弾性樹脂は、塩化ビニル系樹脂及び弾性樹脂の合計量100質量部に対して0.8~16質量部含まれる。0.8質量%未満であると、引張強度や伸び性といった機械物性の十分な向上がみられない。一方、16質量%を超えると、発泡特性が悪化すると共に、ゴム的性質が優位となり、応力緩和性が悪くなることにより、エンボス時のエンボス戻りが発生し、エンボス柄の転写性が悪化する。弾性樹脂は、塩化ビニル系樹脂及び弾性樹脂の合計量100質量部に対して1~15質量部含まれることが好ましく、1~10質量部含まれることがより好ましい。 The elastic resin in the foamed vinyl chloride resin sheet of the present invention is contained in an amount of 0.8 to 16 parts by mass per 100 parts by mass of the total amount of the vinyl chloride resin and the elastic resin. If it is less than 0.8% by mass, sufficient improvement in mechanical properties such as tensile strength and elongation is not observed. On the other hand, if it exceeds 16% by mass, the foaming property is deteriorated, the rubber-like property becomes dominant, and the stress relaxation property is deteriorated. The elastic resin is preferably contained in an amount of 1 to 15 parts by mass, more preferably 1 to 10 parts by mass, per 100 parts by mass of the total amount of the vinyl chloride resin and the elastic resin.

(可塑剤)
本発明における可塑剤としては、従来公知の可塑剤を使用することができる。
(Plasticizer)
Conventionally known plasticizers can be used as the plasticizer in the present invention.

本発明においては、例えば、ジブチルフタレート、ジ-(2-エチルヘキシル)フタレート、ジ-n-オクチルフタレート、ジイソブチルフタレート、ジヘプチルフタレート、ジフェニルフタレート、ジイソデシルフタレート、ジウンデシルフタレート、ブチルベンジルフタレート、ジノニルフタレート、ジシクロヘキシルフタレートなどのフタル酸誘導体;ジ-(2-エチルヘキシル)イソフタレート、ジイソオクチルイソフタレート、ジイソノニルフタレートなどのイソフタル酸誘導体;ジ-(2-エチルヘキシル)テトラヒドロフタレート、ジ-n-オクチルテトラヒドロフタレート、ジイソデシルテトラヒドロフタレートなどのテトラヒドロフタル酸誘導体;ジ-n-ブチルアジペート、ジ-(2-エチルヘキシル)アジペート、ジイソデシルアジペート、ジイソノニルアジペートなどのアジピン酸誘導体;ジ-(2-エチルヘキシル)アゼレート、ジイソオクチルアゼレート、ジ-n-ヘキシルアゼレートなどのアゼライン酸誘導体;ジ-n-ブチルセバケート、ジ-(2-エチルヘキシル)セバケートなどのセバシン酸誘導体;ジ-n-ブチルマレエート、ジメチルマレエート、ジエチルマレエート、ジ-(2-エチルヘキシル)マレエートなどのマレイン酸誘導体;ジ-n-ブチルフマレート、ジ-(2-エチルヘキシル)フマレートなどのフマル酸誘導体;トリ-(2-エチルヘキシル)トリメリテート、トリ-n-オクチルトリメリテート、トリイソデシルトリメリテート、トリイソオクチルトリメリテート、トリ-n-ヘキシルトリメリテート、トリイソノニルトリメリテートなどのトリメリット酸誘導体;テトラ-(2-エチルヘキシル)ピロメリテート、テトラ-n-オクチルピロメリテートなどのピロメリット酸誘導体;トリエチルシトレート、トリ-n-ブチルシトレート、アセチルトリエチルシトレート、アセチルトリ-(2-エチルヘキシル)シトレートなどのクエン酸誘導体;モノメチルイタコネート、モノブチルイタコネート、ジメチルイタコネート、ジエチルイタコネート、ジブチルイタコネート、ジ-(2-エチルヘキシル)イタコネートなどのイタコン酸誘導体;ブチルオレエート、グリセリルモノオレエート、ジエチレングリコールモノオレエートなどのオレイン酸誘導体;グリセリルモノリシノレート、ジエチレングリコールモノリシノレートなどのリシノール酸誘導体;グリセリンモノステアレート、ジエチレングリコールジステアレートなどのステアリン酸誘導体;ジエチレングリコールモノラウレート、ジエチレングリコールジペラルゴネート、ペンタエリスリトール脂肪酸エステルなどのその他の脂肪酸誘導体;トリエチルホスフェート、トリブチルホスフェート、トリ-(2-エチルヘキシル)ホスフェート、トリフェニルホスフェート、クレジルジフェニルホスフェート、トリクレジルホスフェート、トリス(クロロエチル)ホスフェートなどのリン酸誘導体;ジエチレングリコールジベンゾエート、ジプロピレングリコールジベンゾエート、トリエチレングリコールジベンゾエート、ジブチルメチレンビスチオグリコレートなどのグリコール誘導体;グリセロールモノアセテート、グリセロールトリアセテート、グリセロールトリブチレートなどのグリセリン誘導体;アジピン酸系ポリエステル、セバシン酸系ポリエステル、フタル酸系ポリエステルなどのポリエステル系可塑剤;あるいは部分水添ターフェニル、接着性可塑剤;さらにはジアリルフタレート、アクリル系モノマーやオリゴマーなどの重合性可塑剤などを用いることができる。これらの可塑剤は2種以上併用してもよい。 In the present invention, for example, dibutyl phthalate, di-(2-ethylhexyl) phthalate, di-n-octyl phthalate, diisobutyl phthalate, diheptyl phthalate, diphenyl phthalate, diisodecyl phthalate, diundecyl phthalate, butylbenzyl phthalate, dinonyl phthalate , dicyclohexyl phthalate and other phthalic acid derivatives; di-(2-ethylhexyl) isophthalate, diisooctyl isophthalate, diisononyl phthalate and other isophthalic acid derivatives; di-(2-ethylhexyl) tetrahydrophthalate, di-n-octyl tetrahydrophthalate , diisodecyltetrahydrophthalate and other tetrahydrophthalic acid derivatives; di-n-butyl adipate, di-(2-ethylhexyl)adipate, diisodecyladipate, diisononyl adipate and other adipic acid derivatives; di-(2-ethylhexyl)azelate, diisooctyl azelaic acid derivatives such as azelate and di-n-hexyl azelate; sebacic acid derivatives such as di-n-butyl sebacate and di-(2-ethylhexyl) sebacate; di-n-butyl maleate, dimethyl maleate and diethyl maleate maleic acid derivatives such as ate, di-(2-ethylhexyl) maleate; fumaric acid derivatives such as di-n-butyl fumarate, di-(2-ethylhexyl) fumarate; tri-(2-ethylhexyl) trimellitate, tri-n - trimellitic acid derivatives such as octyl trimellitate, triisodecyl trimellitate, triisooctyl trimellitate, tri-n-hexyl trimellitate, triisononyl trimellitate; tetra-(2-ethylhexyl) pyromellitate , pyromellitic acid derivatives such as tetra-n-octyl pyromellitate; citric acid derivatives such as triethyl citrate, tri-n-butyl citrate, acetyl triethyl citrate, acetyl tri-(2-ethylhexyl) citrate; monomethyl itaco itaconic acid derivatives such as diethyl itaconate, monobutyl itaconate, dimethyl itaconate, diethyl itaconate, dibutyl itaconate, di-(2-ethylhexyl) itaconate; oleic acid such as butyl oleate, glyceryl monooleate, diethylene glycol monooleate derivatives; ricinoleic acid derivatives such as glyceryl monoricinoleate and diethylene glycol monoricinolate; stearic acid derivatives such as glycerin monostearate and diethylene glycol distearate; Fatty acid derivatives; phosphoric acid derivatives such as triethyl phosphate, tributyl phosphate, tri-(2-ethylhexyl) phosphate, triphenyl phosphate, cresyl diphenyl phosphate, tricresyl phosphate, tris(chloroethyl) phosphate; diethylene glycol dibenzoate, dipropylene glycol Glycol derivatives such as dibenzoate, triethylene glycol dibenzoate, and dibutylmethylene bisthioglycolate; glycerin derivatives such as glycerol monoacetate, glycerol triacetate, and glycerol tributyrate; adipic acid-based polyesters, sebacic acid-based polyesters, phthalic acid-based polyesters or partially hydrogenated terphenyl, adhesive plasticizers; further polymerizable plasticizers such as diallyl phthalate, acrylic monomers and oligomers, and the like. Two or more of these plasticizers may be used in combination.

(その他の成分)
本発明の発泡塩化ビニル系樹脂シートにおいては、塩化ビニル系樹脂、弾性樹脂及び可塑剤に加えて、その他の各種成分を配合してもよい。その他の成分としては、例えば、熱安定剤、充填剤、発泡促進剤、粘度調整剤、接着性付与剤、着色剤、希釈剤、紫外線吸収剤、酸化防止剤、補強剤を挙げることができる。
(other ingredients)
In addition to the vinyl chloride resin, the elastic resin and the plasticizer, the foamed vinyl chloride resin sheet of the present invention may contain other various components. Other components include, for example, heat stabilizers, fillers, foaming accelerators, viscosity modifiers, adhesion imparting agents, colorants, diluents, ultraviolet absorbers, antioxidants, and reinforcing agents.

本発明の発泡塩化ビニル系樹脂シートは、軟質であり、例えば、壁材、床材、ブックカバー、レザー等の発泡樹脂層として用いることができる。 The foamed vinyl chloride resin sheet of the present invention is soft and can be used, for example, as a foamed resin layer for wall materials, floor materials, book covers, leather and the like.

[発泡塩化ビニル系樹脂シートの製造方法]
本発明の発泡塩化ビニル系樹脂シートの製造方法は、塩化ビニル系樹脂と、SP値が7.5~11.0の弾性樹脂と、可塑剤とを混練し、得られた混練物をシート成型した後、得られたシートを発泡させる。本製造方法により、上記本発明の発泡塩化ビニル系樹脂シートを製造することができる。
[Method for producing foamed vinyl chloride resin sheet]
In the method for producing a foamed vinyl chloride resin sheet of the present invention, a vinyl chloride resin, an elastic resin having an SP value of 7.5 to 11.0, and a plasticizer are kneaded, and the resulting kneaded product is molded into a sheet. After that, the obtained sheet is foamed. According to this production method, the foamed vinyl chloride resin sheet of the present invention can be produced.

本発明の製造方法においては、上記のように、少なくとも塩化ビニル系樹脂、弾性樹脂及び可塑剤を混錬した原料塩化ビニル系組成物(コンパウンド又はプラスチゾル)を原料として用いるが、これ以外の成分を配合してもよい。例えば、上記例示したその他の成分の他、発泡剤を用いることが好ましい。 In the production method of the present invention, as described above, a raw vinyl chloride composition (compound or plastisol) obtained by kneading at least a vinyl chloride resin, an elastic resin and a plasticizer is used as a raw material. May be blended. For example, it is preferable to use a foaming agent in addition to the other components exemplified above.

発泡剤としては、例えば、重炭酸ナトリウム、重炭酸アンモニウム、亜硝酸アンモニウム、アミド化合物、ホウ水素化ナトリウム等の無機発泡剤;イソシアネート化合物、アゾ化合物、ヒドラジン誘導体、セミカルバジド化合物、アジ化合物、ニトロソ化合物、トリアゾール化合物等の有機系発泡剤等が挙げられ、2種以上併用してもよい。 Examples of foaming agents include inorganic foaming agents such as sodium bicarbonate, ammonium bicarbonate, ammonium nitrite, amide compounds, and sodium borohydride; isocyanate compounds, azo compounds, hydrazine derivatives, semicarbazide compounds, azide compounds, nitroso compounds, and triazoles. Examples include organic foaming agents such as compounds, and the like, and two or more thereof may be used in combination.

なお、本発明の製造方法においては、必ずしも発泡剤を用いる必要はなく、例えば、マイクロカプセルや、揮発性液体の使用、機械発泡が挙げられる。 In addition, in the production method of the present invention, it is not always necessary to use a foaming agent, and examples thereof include the use of microcapsules, volatile liquids, and mechanical foaming.

シート成型の方法としては、例えば、カレンダー成型法、押出成型法、インフレーション成型法等が挙げられ、効率的にシート成型を行うことができると共に、本発明の効果を有効に発揮させることができることから、カレンダー成型が好ましい。カレンダー成型においては、はじめに塩化ビニル系樹脂及び可塑剤を含む組成物を装置に投入し、シート成型中に弾性樹脂を後から添加することが好ましい。シート成型時の加熱温度としては、原料塩化ビニル系組成物が溶融し、発泡剤が分解発泡しない温度であれば特に制限されるものではなく、例えば、110~230℃であり、140~170℃が好ましい。 Examples of the sheet molding method include calendar molding, extrusion molding, inflation molding, and the like, and the sheet molding can be performed efficiently and the effects of the present invention can be effectively exhibited. , calender molding is preferred. In calender molding, it is preferable to first put a composition containing a vinyl chloride resin and a plasticizer into an apparatus, and then add the elastic resin later during sheet molding. The heating temperature during sheet molding is not particularly limited as long as the starting vinyl chloride composition is melted and the foaming agent is not decomposed and foamed. is preferred.

シート成型後、シートが発泡剤を含む場合は、発泡剤が発泡する温度に加熱して、シートを発泡させる。加熱温度としては、発泡剤が分解する温度であれば特に制限されるものではなく、例えば、110~230℃であり、180~210℃が好ましい。 After molding the sheet, if the sheet contains a foaming agent, the sheet is foamed by heating to a temperature at which the foaming agent foams. The heating temperature is not particularly limited as long as it decomposes the foaming agent, and is, for example, 110 to 230.degree.

以下、実施例および比較例を挙げて本発明を更に詳細に説明するが、本発明はこれらの実施例に限定されるものではない。 EXAMPLES The present invention will be described in more detail below with reference to Examples and Comparative Examples, but the present invention is not limited to these Examples.

[実施例1]
塩化ビニル系樹脂としての粘度平均重合度1020のサスペンジョン系塩化ビニル系樹脂(新第一塩ビ(株)製ZEST 1000Z)99質量部と、可塑剤としてのジ-(2-エチルヘキシル)フタレート((株)ジェイ・プラス製DOP)58質量部と、炭酸カルシウム15質量部と、発泡剤としての(三協化成(株)製セルマイクC-2)2.5質量部と、安定剤としての((株)ADEKA製SC-320)3質量部と、加工助剤としての(三菱ケミカル(株)製メタブレンP-530A)1質量部とを、ヘンシェルミキサー(日本コークス工業(株)製UM2E/I)で3000回転で樹脂温度が120℃に昇温されるまで混合し、塩化ビニル系組成物(コンパウンド)を調製した。
[Example 1]
99 parts by mass of a suspension vinyl chloride resin (ZEST 1000Z manufactured by Shin-Daiichi Vinyl Co., Ltd.) with a viscosity average polymerization degree of 1020 as a vinyl chloride resin, and di-(2-ethylhexyl) phthalate (Ltd. ) DOP manufactured by J Plus) 58 parts by mass, calcium carbonate 15 parts by mass, (Cellmic C-2 manufactured by Sankyo Kasei Co., Ltd.) 2.5 parts by mass as a foaming agent, and (Co., Ltd.) as a stabilizer ) SC-320 manufactured by ADEKA) 3 parts by mass and 1 part by mass of (Metabrene P-530A manufactured by Mitsubishi Chemical Corporation) as a processing aid, Henschel mixer (UM2E / I manufactured by Nippon Coke Industry Co., Ltd.) The mixture was mixed at 3000 rpm until the resin temperature was raised to 120° C. to prepare a vinyl chloride composition (compound).

調製した塩化ビニル系組成物をカレンダー成型装置に投入し、シート成型中に弾性樹脂としてのアクリルニトリル・ブタジエン系ゴム(NBR)1質量部を加え、作製したシートを加熱して発泡させ、実施例1に係る発泡塩化ビニル系樹脂シートを製造した。 The prepared vinyl chloride composition was put into a calendar molding machine, 1 part by mass of acrylonitrile-butadiene rubber (NBR) as an elastic resin was added during sheet molding, and the prepared sheet was heated to foam. A foamed vinyl chloride resin sheet according to 1 was produced.

[実施例2]
実施例1において、塩化ビニル系樹脂の配合量99質量部を95質量部とし、弾性樹脂の配合量1質量を5質量部とした以外は同様にして、実施例2に係る発泡塩化ビニル系樹脂シートを製造した。
[実施例3]
実施例1において、塩化ビニル系樹脂の配合量99質量部を90質量部とし、弾性樹脂の配合量1質量を10質量部とした以外は同様にして、実施例3に係る発泡塩化ビニル系樹脂シートを製造した。
[実施例4]
実施例1において、塩化ビニル系樹脂の配合量99質量部を85質量部とし、弾性樹脂の配合量1質量を15質量部とした以外は同様にして、実施例4に係る発泡塩化ビニル系樹脂シートを製造した。
[Example 2]
The foamed vinyl chloride resin according to Example 2 was prepared in the same manner as in Example 1, except that the compounded amount of the vinyl chloride resin was changed from 99 parts by mass to 95 parts by mass, and the compounded amount of the elastic resin was changed from 1 mass to 5 parts by mass. manufactured the sheet.
[Example 3]
The foamed vinyl chloride resin according to Example 3 was prepared in the same manner as in Example 1, except that the compounded amount of the vinyl chloride resin was changed from 99 parts by mass to 90 parts by mass, and the compounded amount of the elastic resin was changed from 1 mass to 10 parts by mass. manufactured the sheet.
[Example 4]
The foamed vinyl chloride resin according to Example 4 was prepared in the same manner as in Example 1, except that the compounded amount of the vinyl chloride resin was changed from 99 parts by mass to 85 parts by mass, and the compounded amount of the elastic resin was changed from 1 mass to 15 parts by mass. manufactured the sheet.

[比較例1]
実施例1において、塩化ビニル系樹脂の配合量99質量部を100質量部とし、弾性樹脂の配合量1質量を0質量部(無配合)とした以外は同様にして、比較例1に係る発泡塩化ビニル系樹脂シートを製造した。
[比較例2]
実施例1において、塩化ビニル系樹脂の配合量99質量部を80質量部とし、弾性樹脂の配合量1質量を20質量部とした以外は同様にして、比較例2に係る発泡塩化ビニル系樹脂シートを製造した。
[Comparative Example 1]
Foaming according to Comparative Example 1 was performed in the same manner as in Example 1, except that the compounded amount of the vinyl chloride resin was changed from 99 parts by mass to 100 parts by mass, and the compounded amount of the elastic resin was changed from 1 mass to 0 parts by mass (no compounding). A vinyl chloride resin sheet was produced.
[Comparative Example 2]
Foamed vinyl chloride resin according to Comparative Example 2 was prepared in the same manner as in Example 1, except that the compounded amount of the vinyl chloride resin was changed from 99 parts by mass to 80 parts by mass, and the compounded amount of the elastic resin was changed from 1 mass to 20 parts by mass. manufactured the sheet.

[実施例5]
実施例2において、粘度平均重合度1020の塩化ビニル系樹脂を、粘度平均重合度460の塩化ビニル系樹脂に変更した以外は同様にして、実施例5に係る発泡塩化ビニル系樹脂シートを製造した。
[実施例6]
実施例2において、粘度平均重合度1020の塩化ビニル系樹脂を、粘度平均重合度810の塩化ビニル系樹脂に変更した以外は同様にして、実施例6に係る発泡塩化ビニル系樹脂シートを製造した。
[Example 5]
A foamed vinyl chloride resin sheet according to Example 5 was produced in the same manner as in Example 2, except that the vinyl chloride resin having a viscosity average polymerization degree of 1020 was changed to a vinyl chloride resin having a viscosity average polymerization degree of 460. .
[Example 6]
A foamed vinyl chloride resin sheet according to Example 6 was produced in the same manner as in Example 2, except that the vinyl chloride resin having a viscosity average polymerization degree of 1020 was changed to a vinyl chloride resin having a viscosity average polymerization degree of 810. .

[実施例7]
実施例2において、粘度平均重合度1020の塩化ビニル系樹脂を、粘度平均重合度1320の塩化ビニル系樹脂に変更した以外は同様にして、実施例7に係る発泡塩化ビニル系樹脂シートを製造した。
[実施例8]
実施例2において、粘度平均重合度1020の塩化ビニル系樹脂を、粘度平均重合度1740の塩化ビニル系樹脂に変更した以外は同様にして、実施例8に係る発泡塩化ビニル系樹脂シートを製造した。
[Example 7]
A foamed vinyl chloride resin sheet according to Example 7 was produced in the same manner as in Example 2 except that the vinyl chloride resin having a viscosity average polymerization degree of 1020 was changed to a vinyl chloride resin having a viscosity average polymerization degree of 1320. .
[Example 8]
A foamed vinyl chloride resin sheet according to Example 8 was produced in the same manner as in Example 2 except that the vinyl chloride resin having a viscosity average polymerization degree of 1020 was changed to a vinyl chloride resin having a viscosity average polymerization degree of 1740. .

[比較例3]
実施例5において、塩化ビニル系樹脂の配合量95質量部を100質量部とし、弾性樹脂の配合量5質量を0質量部(無配合)とした以外は同様にして、比較例3に係る発泡塩化ビニル系樹脂シートを製造した。
[比較例4]
実施例6において、塩化ビニル系樹脂の配合量95質量部を100質量部とし、弾性樹脂の配合量5質量を0質量部(無配合)とした以外は同様にして、比較例4に係る発泡塩化ビニル系樹脂シートを製造した。
[Comparative Example 3]
Foaming according to Comparative Example 3 was performed in the same manner as in Example 5, except that the compounded amount of the vinyl chloride resin was changed from 95 parts by mass to 100 parts by mass, and the compounded amount of the elastic resin was changed from 5 parts by mass to 0 parts by mass (no compounding). A vinyl chloride resin sheet was produced.
[Comparative Example 4]
Foaming according to Comparative Example 4 was performed in the same manner as in Example 6, except that the blending amount of the vinyl chloride resin was changed from 95 parts by mass to 100 parts by mass, and the blending amount of the elastic resin was changed from 5 parts by mass to 0 parts by mass (no blending). A vinyl chloride resin sheet was produced.

[比較例5]
実施例7において、塩化ビニル系樹脂の配合量95質量部を100質量部とし、弾性樹脂の配合量5質量を0質量部(無配合)とした以外は同様にして、比較例5に係る発泡塩化ビニル系樹脂シートを製造した。
[比較例6]
実施例8において、塩化ビニル系樹脂の配合量95質量部を100質量部とし、弾性樹脂の配合量5質量を0質量部(無配合)とした以外は同様にして、比較例6に係る発泡塩化ビニル系樹脂シートを製造した。
[Comparative Example 5]
Foaming according to Comparative Example 5 was performed in the same manner as in Example 7, except that the blending amount of the vinyl chloride resin was changed from 95 parts by mass to 100 parts by mass, and the blending amount of the elastic resin was changed from 5 parts by mass to 0 parts by mass (no blending). A vinyl chloride resin sheet was produced.
[Comparative Example 6]
Foaming according to Comparative Example 6 was performed in the same manner as in Example 8, except that the blending amount of the vinyl chloride resin was changed from 95 parts by mass to 100 parts by mass, and the blending amount of the elastic resin was changed from 5 parts by mass to 0 parts by mass (no blending). A vinyl chloride resin sheet was produced.

[実施例9]
実施例2において、弾性樹脂であるアクリルニトリル・ブタジエン系ゴム(NBR)を、熱可塑性ポリウレタン(SBR)に変更した以外は同様にして、実施例9に係る発泡塩化ビニル系樹脂シートを製造した。
[実施例10]
実施例2において、弾性樹脂であるアクリルニトリル・ブタジエン系ゴム(NBR)を、弾性樹脂である熱可塑性ポリウレタン(TPU)に変更した以外は同様にして、実施例10に係る発泡塩化ビニル系樹脂シートを製造した。
[実施例11]
実施例2において、弾性樹脂であるアクリルニトリル・ブタジエン系ゴム(NBR)を、弾性樹脂であるクロロプレンゴム(CR)に変更した以外は同様にして、実施例11に係る発泡塩化ビニル系樹脂シートを製造した。
[Example 9]
A foamed vinyl chloride resin sheet according to Example 9 was produced in the same manner as in Example 2, except that acrylonitrile-butadiene rubber (NBR) as the elastic resin was changed to thermoplastic polyurethane (SBR).
[Example 10]
A foamed vinyl chloride resin sheet according to Example 10 was prepared in the same manner as in Example 2, except that acrylonitrile-butadiene rubber (NBR) as the elastic resin was changed to thermoplastic polyurethane (TPU) as the elastic resin. manufactured.
[Example 11]
A foamed vinyl chloride resin sheet according to Example 11 was prepared in the same manner as in Example 2, except that the elastic resin acrylonitrile-butadiene rubber (NBR) was changed to the elastic resin chloroprene rubber (CR). manufactured.

[実施例12]
実施例2において、弾性樹脂であるアクリルニトリル・ブタジエン系ゴム(NBR)を、弾性樹脂であるクロロスルホン化ポリエチレン(CSM)に変更した以外は同様にして、実施例12に係る発泡塩化ビニル系樹脂シートを製造した。
[実施例13]
実施例2において、弾性樹脂であるアクリルニトリル・ブタジエン系ゴム(NBR)を、弾性樹脂であるアクリルゴム(ACM)に変更した以外は同様にして、実施例13に係る発泡塩化ビニル系樹脂シートを製造した。
[実施例14]
実施例2において、弾性樹脂であるアクリルニトリル・ブタジエン系ゴム(NBR)を、弾性樹脂である塩素化ポリエチレン(CPE)に変更した以外は同様にして、実施例14に係る発泡塩化ビニル系樹脂シートを製造した。
[Example 12]
A foamed vinyl chloride resin according to Example 12 was prepared in the same manner as in Example 2, except that the elastic resin acrylonitrile-butadiene rubber (NBR) was changed to the elastic resin chlorosulfonated polyethylene (CSM). manufactured the sheet.
[Example 13]
A foamed vinyl chloride resin sheet according to Example 13 was produced in the same manner as in Example 2, except that acrylonitrile-butadiene rubber (NBR) as the elastic resin was changed to acrylic rubber (ACM) as the elastic resin. manufactured.
[Example 14]
A foamed vinyl chloride resin sheet according to Example 14 was prepared in the same manner as in Example 2, except that the elastic resin acrylonitrile-butadiene rubber (NBR) was changed to the elastic resin chlorinated polyethylene (CPE). manufactured.

[比較例7]
実施例2において、弾性樹脂であるアクリルニトリル・ブタジエン系ゴム(NBR)を、SP値が本発明の範囲から外れる弾性樹脂であるフッ素ゴム(FKM)に変更した以外は同様にして、比較例7に係る発泡塩化ビニル系樹脂シートを製造した。
[Comparative Example 7]
Comparative Example 7 was carried out in the same manner as in Example 2, except that the elastic resin acrylonitrile-butadiene rubber (NBR) was changed to fluororubber (FKM), which is an elastic resin whose SP value is outside the scope of the present invention. A foamed vinyl chloride resin sheet according to was manufactured.

上記実施例1~14及び比較例1~7に係る発泡塩化ビニル系樹脂シートについて、引張伸び率、引張強度、応力残留率、発泡セル緻密性、表面平滑性、発泡倍率を以下の方法で評価した。 The foamed vinyl chloride resin sheets according to Examples 1 to 14 and Comparative Examples 1 to 7 were evaluated for tensile elongation, tensile strength, stress residual rate, foam cell compactness, surface smoothness, and expansion ratio by the following methods. bottom.

(引張試験用サンプル)
発泡塩化ビニル系樹脂シートのカレンダーロール方向(MD)から1号ダンベル型引張り試験片を各10枚ずつ作成し、引張試験用サンプルとした。
(Sample for tensile test)
Ten No. 1 dumbbell-type tensile test pieces were prepared from each of the foamed vinyl chloride resin sheets in the calendar roll direction (MD), and used as samples for the tensile test.

(引張伸び率、引張強度、応力残留率)
引張試験用サンプルをオートグラフ((株)島津製作所製AGS-H)で引張伸び率、引張強度及び応力残留率を測定した。引張試験は、つかみ間距離40mm、試験速度3mm/分で引張試験用サンプルを引張り、発泡塩化ビニル系樹脂シートが破れ始めた時の伸びをつかみ間距離で除した値を伸び率とした。また、発泡塩化ビニル系樹脂シートが破れ始める前の最大応力を引張強度とし、n=5の平均値を求めた。応力残留率は、つかみ間距離が40mmから60mmになるまで試験速度40mm/分で引張り、その直後の応力を初期応力σとし、それから600秒経過後の応力をσとし、応力残留率=(σ/σ)×100とし、n=5の平均値を求めた。
(Tensile elongation, tensile strength, stress residual rate)
Tensile elongation, tensile strength and stress residual rate of the tensile test sample were measured by Autograph (AGS-H manufactured by Shimadzu Corporation). In the tensile test, the tensile test sample was pulled at a grip distance of 40 mm and a test speed of 3 mm/min, and the elongation when the foamed vinyl chloride resin sheet started to break was divided by the grip distance to obtain the elongation rate. Also, the maximum stress before the foamed vinyl chloride resin sheet started to break was taken as the tensile strength, and the average value of n=5 was obtained. The stress retention rate is determined by pulling at a test speed of 40 mm / min until the distance between grips is 40 mm to 60 mm, the stress immediately after that is the initial stress σ 0 , and the stress after 600 seconds is σ t , stress retention = (σ t0 )×100, and the average value of n=5 was obtained.

(発泡セル緻密性の評価)
発泡塩化ビニル系樹脂シートの断面をCCDカメラ50倍で拡大観察を行い、発泡セルの緻密性について以下の基準で評価した。
(Evaluation of foam cell compactness)
The cross section of the foamed vinyl chloride resin sheet was observed with a CCD camera at a magnification of 50 times, and the denseness of the foamed cells was evaluated according to the following criteria.

〇:極めて緻密で均一な発泡セルを有する。
△:やや粗い、もしくは不均一な発泡セルを有する。
×:粗い発泡セルを有する。
◯: It has extremely dense and uniform foam cells.
Δ: Slightly rough or having non-uniform foam cells.
x: It has coarse foam cells.

(表面平滑性)
表面の目視観察、断面の表層部を拡大観察し、以下の基準で評価した。
〇:全体が平滑である
△:大部分が平滑であるが、部分的に凹凸がある
×:全体的に不均一な膨れや凹凸がある
(Surface smoothness)
Visual observation of the surface and magnified observation of the surface layer of the cross section were performed, and evaluation was made according to the following criteria.
○: Overall smooth △: Mostly smooth, but partially uneven ×: Overall uneven swelling and unevenness

(発泡倍率)
上記作製したカレンダー成型シート上の任意の5点で厚みを測定し、その平均値を発泡前の厚みLとした。また、加熱発泡して得られた発泡塩化ビニル系樹脂シートについて、カレンダー成型シートの厚みを測定した同一の5点で厚みを測定し、その平均値を発泡後の厚みLとし、発泡倍率=L/Lとして求めた。
(Expansion ratio)
The thickness was measured at arbitrary 5 points on the calender molded sheet prepared above, and the average value was taken as the thickness L0 before foaming. In addition, for the foamed vinyl chloride resin sheet obtained by heating and foaming, the thickness was measured at the same five points where the thickness of the calendar molded sheet was measured, and the average value was taken as the thickness L after foaming, and the expansion ratio = L. /L 0 .

結果を表1~表3に示す。 The results are shown in Tables 1-3.

表1~表3に示すように、実施例1~14に係る発泡塩化ビニル系樹脂シートは、引張伸び率、引張強度及び応力残留率(応力緩和性)に優れると共に、発泡倍率が高く、発泡セルの緻密性や表面平滑性に優れていた。すなわち、機械物性及び発泡特性に優れた発泡塩化ビニル系樹脂シートが得られた。なお、表2に示すように、一般的に高重合度の塩化ビニル系樹脂を用いると引張伸び率、引張強度は向上する傾向にあるが、弾性樹脂を配合することでこれらがさらに向上する。また、表3に示すように、実施例12(CSM)及び実施例13(ACM)と比較して、その他の弾性樹脂を用いた実施例1(NBR)、実施例9(SBR)、実施例10(TPU)、実施例11(CR)及び実施例14(CPE)の方が、伸び性が良好であった。これは、実施例12(CSM)及び実施例13(ACM)の場合は、樹脂がやや固くなり脆性面が少し発現したことによるものと推測される。 As shown in Tables 1 to 3, the foamed vinyl chloride resin sheets according to Examples 1 to 14 are excellent in tensile elongation rate, tensile strength and stress residual rate (stress relaxation property), and have a high expansion ratio. The denseness and surface smoothness of the cells were excellent. That is, a foamed vinyl chloride resin sheet having excellent mechanical properties and foaming properties was obtained. As shown in Table 2, the tensile elongation and tensile strength generally tend to improve when a vinyl chloride resin with a high degree of polymerization is used, but these properties are further improved by blending an elastic resin. Further, as shown in Table 3, in comparison with Example 12 (CSM) and Example 13 (ACM), Example 1 (NBR), Example 9 (SBR), and Example 1 using other elastic resins 10 (TPU), Example 11 (CR) and Example 14 (CPE) had better elongation properties. This is presumed to be due to the fact that, in the case of Examples 12 (CSM) and 13 (ACM), the resin was slightly hardened and a brittle surface was developed a little.

一方、表1に示すように、比較例2のように、適切な弾性樹脂であっても、その配合量が多すぎると、応力残留率が高くなり、エンボス特性が低下し、また、発泡特性も悪化する。また、表3に示すように、比較例7のようにSP値が本発明の範囲から外れる弾性樹脂では、引張伸び率及び引張強度の向上が見られないにもかかわらず、応力残留率が向上し、また、発泡特性も悪化する。 On the other hand, as shown in Table 1, even if the elastic resin is suitable as in Comparative Example 2, if the amount of the resin is too large, the stress residual rate will increase, the embossing characteristics will deteriorate, and the foaming characteristics will increase. also worsens. In addition, as shown in Table 3, the elastic resin having an SP value outside the range of the present invention as in Comparative Example 7 showed no improvement in tensile elongation and tensile strength, but the stress residual rate improved. and also the foaming properties are deteriorated.

本発明の発泡塩化ビニル系樹脂シートは、壁紙等の発泡樹脂層に用いることができることから、産業上有用である。 The foamed vinyl chloride resin sheet of the present invention is industrially useful because it can be used for a foamed resin layer such as wallpaper.

Claims (5)

塩化ビニル系樹脂と、SP値が7.5~11.0の弾性樹脂と、可塑剤とを含み、
前記弾性樹脂が、前記塩化ビニル系樹脂及び弾性樹脂の合計量100質量部に対して0.8~16質量部含まれることを特徴とする発泡塩化ビニル系樹脂シート。
A vinyl chloride resin, an elastic resin with an SP value of 7.5 to 11.0, and a plasticizer,
A foamed vinyl chloride resin sheet, wherein the elastic resin is contained in an amount of 0.8 to 16 parts by mass based on 100 parts by mass of the total amount of the vinyl chloride resin and the elastic resin.
前記塩化ビニル系樹脂の粘度平均重合度が450~1800であることを特徴とする請求項1に記載の発泡塩化ビニル系樹脂シート。 2. The foamed vinyl chloride resin sheet according to claim 1, wherein the vinyl chloride resin has a viscosity average degree of polymerization of 450 to 1,800. 前記弾性樹脂が、ブタジエン系ゴム、熱可塑性ポリウレタン、クロロプレンゴム、及び塩素化ポリエチレンから選択される少なくとも一種であることを特徴とする請求項1又は2に記載の発泡塩化ビニル系樹脂シート。 3. The foamed vinyl chloride resin sheet according to claim 1, wherein the elastic resin is at least one selected from butadiene rubber, thermoplastic polyurethane, chloroprene rubber, and chlorinated polyethylene. 請求項1~3のいずれか一項に記載の発泡塩化ビニル系樹脂シートを製造する方法であって、
塩化ビニル系樹脂と、SP値が7.5~11.0の弾性樹脂と、可塑剤とを混練し、得られた混練物をシート成型した後、得られたシートを発泡させることを特徴とする発泡塩化ビニル系樹脂シートの製造方法。
A method for producing the foamed vinyl chloride resin sheet according to any one of claims 1 to 3,
A vinyl chloride resin, an elastic resin having an SP value of 7.5 to 11.0, and a plasticizer are kneaded, the resulting kneaded product is formed into a sheet, and the obtained sheet is foamed. A method for producing a foamed vinyl chloride resin sheet.
前記のシート成型が、カレンダー成型であることを特徴とする請求項4に記載の発泡塩化ビニル系樹脂シートの製造方法。

5. The method for producing a foamed vinyl chloride resin sheet according to claim 4, wherein the sheet molding is calendar molding.

JP2022011186A 2022-01-27 2022-01-27 Foamed vinyl chloride resin sheet and manufacturing method thereof Pending JP2023109594A (en)

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