TW201213426A - Foam and foaming composition - Google Patents

Foam and foaming composition Download PDF

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Publication number
TW201213426A
TW201213426A TW100130015A TW100130015A TW201213426A TW 201213426 A TW201213426 A TW 201213426A TW 100130015 A TW100130015 A TW 100130015A TW 100130015 A TW100130015 A TW 100130015A TW 201213426 A TW201213426 A TW 201213426A
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mass
foam
parts
block copolymer
component
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TW100130015A
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Chinese (zh)
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TWI441861B (en
Inventor
Susumu Hoshi
Kazuo Morito
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Asahi Kasei Chemicals Corp
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Priority claimed from JP2010186369A external-priority patent/JP5597478B2/en
Priority claimed from JP2010186441A external-priority patent/JP5597479B2/en
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Publication of TW201213426A publication Critical patent/TW201213426A/en
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/0061Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof characterized by the use of several polymeric components
    • AHUMAN NECESSITIES
    • A43FOOTWEAR
    • A43BCHARACTERISTIC FEATURES OF FOOTWEAR; PARTS OF FOOTWEAR
    • A43B13/00Soles; Sole-and-heel integral units
    • A43B13/02Soles; Sole-and-heel integral units characterised by the material
    • A43B13/04Plastics, rubber or vulcanised fibre
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/0066Use of inorganic compounding ingredients
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L53/00Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L53/02Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L9/00Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/04N2 releasing, ex azodicarbonamide or nitroso compound
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2353/00Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
    • C08J2353/02Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers of vinyl aromatic monomers and conjugated dienes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2409/00Characterised by the use of homopolymers or copolymers of conjugated diene hydrocarbons

Abstract

To obtain a foam having excellent hardness, dimensional stability, thermal moldability, and mechanical strength; the foam being suitable for the midsole, inner sole, or outer sole of a shoe. Provided is a foam that has a specific gravity of 0.1-0.98 g/cc and is obtained by crosslinking a foaming composition containing: (a) a block copolymer containing 65-95 mass% of a vinyl aromatic hydrocarbon and 5-35 mass% of a conjugated diene, the block ratio of the vinyl aromatic hydrocarbon polymer being 40-98 mass%, the storage modulus (E') at 30 DEG C in dynamic viscoelastic measurement being 3 108 to 2.35 109 Pa, and one or more peak temperatures existing in the range of 85 to 125 DEG C for the tand function of a dynamic viscoelastic measurement; (b) isoprene rubber and/or diene rubber; (c) a filler; and (d) a blowing agent; the mass ratio of component (a)/component (b) being 1-30/70-99, and the content of components (c) and (d) being 1-100 mass parts and 0.1-30 mass parts, respectively, relative to a total of 100 mass parts of components (a) and (b).

Description

201213426 六、發明說明: 【發明所屬之技術領域】 本發明係關於適合於鞋用中底、㈣或外底用材料 泡體及發泡體用組合物。 發 【先前技術】 運動鞋等所使用之發泡體材料要求緩衝性或衝擊緩衝 性、輕量等特性m種特性的素材先前以來—直使 用:以乙烯-乙酸乙烯醋共聚物(EVA)為主成分之發泡體或 以聚胺基甲酸_(PU)為主成分之發泡體❹基材橡膠令調 配有二氧化梦、碳黑等填充劑之橡膠組合物中含有氣泡的 鞋用交聯發泡體。上述氣泡可藉由發泡劑之發泡、微小中 空球之調配等而含有’於該鞋用交聯發泡體中,正在研究 進一步之輕量化。 先刖,提出如後述之各種發泡體材料。 例如,專利文獻1中揭示含有間規12-聚丁二稀之材料作 為耐磨耗性優異、輕量、且不滑之發泡橡膠鞋底。 專利文獻2巾揭*有旨在輕量、且f有緩衝性通氣性、 隔音性等之嵌段共聚物系交聯發泡體。 ^利文獻3中,揭示有包含含有苯乙稀含量為嫩。以下 之苯乙烯-丁二烯嵌段共聚物之材料的發泡體,作為即便 於高溫、低溫環境下硬度變化亦較小,緩衝性、衝擊緩衝 性優異之發泡體。 專利文獻4中, 熱塑性彈性體及 揭示有含有輻射型熱塑性彈性體與線型 [,2-聚丁二烯之組合物’作為成形性優 5 157712.doc 201213426 異、且柔軟性、成型性外觀優異之成型組合物。 專利文獻5中揭示有用以製造撕裂強度、耐壓縮永久變 形性、低回彈彈性、耐磨性優異之發泡體的氫化嵌段共聚 物0 先前技術文獻 專利文獻 專利文獻1 :曰本專利特開昭63_2〇〇7〇2號公報 專利文獻2:曰本專利特開昭63_225638號公報 專利文獻3 :日本專利特開2〇〇1_34〇1〇5號公報 專利文獻4 :日本專利特開2〇〇4_217846號公報 專利文獻5:國際公開第2007/094216號 【發明内容】 發明所欲解決之問題 然而,如上所述之先前揭示之各種發泡體材料於硬度、 尺寸穩定性、熱成型性及機械強度方面均仍有改善餘地, 作為鞋用發泡體(鞋底),並不具有充分之特性。 因此’本發明之目的係提供硬度、尺寸穩定性、熱成型 性及機械強度優異之特別適合於鞋用中底、鞋塾及外底之 發泡體。 解決問題之技術手段 本發明者等人為了解決如上所述之關於發泡體之先前技 術的課題而反覆銳意研究’結果發現,以特定比率包含具 有特定黏彈性行為之含有乙烯基芳香族烴與共軛二烯之嵌 段共聚物、特定橡膠成分、填充劑、及發泡劑之發泡體, 157712.doc 201213426 或包含含有乙料芳香族煙與共_二烯之嵌段共聚物 疋橡膠成π ί真充劑 '發泡劑且於特定㈣之比重中呈有 特定硬度之發泡體,可这士、l ·+. 、 J建成上述目的,從而完成了本 明。 即,本發明為如下所述。 [1] -種發泡體,其係、使包含下述成分之發泡體用組合物交 聯而成:⑷嵌段共聚物,其含有至少2個乙烯基芳香族煙 聚合物嵌段、以及至少!個包含共軛二烯與乙烯基芳香族 烴之共聚物嵌段,且 乙稀基芳香族煙之含量為65〜95質量%、共辆二婦之含 量為5〜35質量%, 嵌段共聚物所含有之乙烯基芳香族烴聚合物之嵌段率為 40〜98質量%, 動態黏彈性測定中30°C下之儲存彈性模數(E,)為3χ1〇8 Pa以上2.35Χ109 pa以下,且動態黏彈性測定之函數以⑽之 峰值溫度於85°C以上125°C以下存在至少!個; (b) 異戊二烯系橡膠及/或二烯系橡膠; (c) 填充劑; (d) 發泡劑; 上述(a)嵌段共聚物與上述(b)異戊二烯系橡膠及/或二稀 系橡膠之質量比為1〜30/70〜99 ; 使相對於上述(a)嵌段共聚物與上述(b)異戊二烯系橡膠 及/或二烯系橡膠之合計量1〇〇質量份,而含有上述(c)填充 157712.doc 201213426 劑1〜100貝量份、上述(句發泡劑〇丨〜3〇質量份且該發泡 體比重為0.1〜0.98 g/cc。 [2] 如上述[1]之發泡體’其中上述⑷嵌段共聚物係動態黏 彈性測定之函數ΐαηδ之峰值溫度於9(rc以上125„c以下存 在至少1個。 [3] 如上述[1]或[2]之發泡體,其中上述⑷欲段共聚物含有 至少1個包含乙烯基芳香族烴含量為7〇質量%以上未達1 〇〇 質量。/。之乙烯基芳香族烴與共軛二烯之無規共聚物嵌段。 [4] 如上述[1]至[3]中任-項之發泡體,上述⑷嵌段共聚物 含有至少1個包含乙烯基芳香族烴含量為75質量%以上% 質量%以下之乙烯基芳香族烴與共軛二烯之無規共聚物嵌 段。 [5] 如上述[1]至[4]中任一項之發泡體’其中相對於上述 嵌段共聚物、與上述(b)異戊二烯系橡膠及/或二烯系橡膠 之合計量100質量份,而含有: 上述(c)填充劑2〜90質量份、 上述(d)發泡劑0.5〜20質量份。 [6] 如上述[1]至[5]中任一項之發泡體,其中相對於上述(&) 嵌段共聚物、與上述(b)異戊二烯系橡膠及/或二烯系橡膠 157712.doc -6 - 201213426 之合計量100質量份,而進而含有: (e)熱塑性彈性體及/或熱塑性樹脂1〜i 〇〇質量份。 [7] 如上述[1]至[6]中任一項之發泡體,其中比重為〇1〜〇7 g/cc、或比重為 〇.8〜〇 98 g/cc。 [8] 一種鞋底,其係將如上述[丨]至[7]中任一項之發泡體成 型而成。 [9] -種發泡體用組合物,其包含:⑷嵌段共聚物,其含有 至少2個乙烯基芳香族烴聚合物嵌段、以及至少1個包含共 軛二烯與乙烯基芳香族烴之共聚物嵌段,且 乙烯基芳香族煙之含量為65〜95f量%、共輛二烯之含 $為5〜35質量%, 嵌段共聚物所含有之乙烯基芳香族烴聚合物之欲段率為 40〜98質量%, 動U彈&測定中3G°C下之儲存彈性模數(ε,)為3x1〇8201213426 VI. Description of the Invention: [Technical Field of the Invention] The present invention relates to a composition for a material for a shoe midsole, a (four) or an outsole, and a composition for a foam. [Prior Art] Foam materials used in sports shoes, etc. require materials such as cushioning, impact cushioning, and lightweight properties. Previously, the material used was: ethylene-vinyl acetate copolymer (EVA) A foam of a main component or a foamed base rubber having a polyaminocarbamic acid (PU) as a main component, and a rubber composition containing a filler such as a dioxide dream or a carbon black Foamed body. The above-mentioned air bubbles can be contained in the crosslinked foamed body for foaming by foaming of a foaming agent, blending of fine hollow spheres, etc., and further weight reduction is being studied. First, various foam materials as described later are proposed. For example, Patent Document 1 discloses a material containing syndiotactic 12-polybutylene dilute as a foamed rubber sole which is excellent in abrasion resistance, lightweight, and non-slip. Patent Document 2 discloses a block copolymer-based crosslinked foam which is intended to be lightweight, has a cushioning air permeability, and has sound insulating properties. In Lie 3, it is revealed that the content containing styrene is tender. The foam of the material of the styrene-butadiene block copolymer is a foam which is small in hardness change even in a high-temperature and low-temperature environment, and is excellent in cushioning property and impact cushioning property. In Patent Document 4, a thermoplastic elastomer and a composition containing a radiation-type thermoplastic elastomer and a linear [2-mertene-butadiene] are disclosed as excellent moldability, and excellent in flexibility and moldability. Molding composition. Patent Document 5 discloses a hydrogenated block copolymer useful for producing a foam having excellent tear strength, compression set resistance, low rebound resilience, and abrasion resistance. PRIOR ART DOCUMENT Patent Document Patent Document 1: Patent Japanese Laid-Open Patent Publication No. JP-A-63-225638 Patent Document 3: Japanese Patent Laid-Open Publication No. Hei No. Hei. Patent Document 5: International Publication No. 2007/094216 SUMMARY OF THE INVENTION Problems to be Solved by the Invention However, various foam materials previously disclosed as described above are in hardness, dimensional stability, thermoforming There is still room for improvement in terms of properties and mechanical strength, and as a foam for shoes (sole), it does not have sufficient characteristics. Therefore, the object of the present invention is to provide a foam which is particularly suitable for a shoe midsole, a shoe last and an outsole which is excellent in hardness, dimensional stability, thermoformability and mechanical strength. Means for Solving the Problems The inventors of the present invention have repeatedly studied in order to solve the problems of the prior art regarding foams as described above, and found that the inclusion of vinyl aromatic hydrocarbons having specific viscoelastic behavior at a specific ratio and A block copolymer of a conjugated diene, a specific rubber component, a filler, and a foam of a foaming agent, 157712.doc 201213426 or a block copolymer containing a blend of aromatic aromatic and co-diene The foam is formed into a foam having a specific hardness in the specific gravity of the specific (4), and the above purpose can be achieved by this, l·+., J, thereby completing the present invention. That is, the present invention is as follows. [1] A foam obtained by crosslinking a composition for a foam comprising the following components: (4) a block copolymer containing at least two vinyl aromatic tobacco polymer blocks, And at least one copolymer block comprising a conjugated diene and a vinyl aromatic hydrocarbon, and the content of the ethylene-based aromatic tobacco is 65 to 95% by mass, and the content of the total two women is 5 to 35% by mass. The block ratio of the vinyl aromatic hydrocarbon polymer contained in the block copolymer is 40 to 98% by mass, and the storage elastic modulus (E,) at 30 ° C in the dynamic viscoelasticity measurement is 3χ1〇8 Pa or more and 2.35. Χ109 pa or less, and the dynamic viscoelasticity measurement function has a peak temperature of (10) of at least 85 ° C and above 125 ° C below! (b) isoprene-based rubber and/or diene-based rubber; (c) filler; (d) foaming agent; (a) block copolymer and (b) isoprene The mass ratio of the rubber and/or the dilute rubber is from 1 to 30/70 to 99; and is relative to the above (a) block copolymer and the above (b) isoprene rubber and/or diene rubber. 1 part by mass of the total amount, and containing the above (c) filling 157712.doc 201213426 agent 1 to 100 parts by weight, the above (sentence foaming agent 〇丨~3 〇 parts by mass and the specific gravity of the foam is 0.1 to 0.98 [2] The foam of the above [1] wherein the peak temperature of the function (4) of the above-mentioned (4) block copolymer dynamic viscous measurement ΐαηδ is at least one of 9 (rc or more and 125 cp or less). [3] The foam of the above [1] or [2], wherein the (4) segment copolymer contains at least one vinyl aromatic hydrocarbon content of 7 〇 mass% or more and less than 1 〇〇 mass. The random copolymer block of the vinyl aromatic hydrocarbon and the conjugated diene. [4] The foam of any one of the above [1] to [3], wherein the (4) block copolymer contains at least one of Vinyl aroma The random copolymer block of a vinyl aromatic hydrocarbon and a conjugated diene having a hydrocarbon content of 75% by mass or more and more by mass%. [5] The foaming according to any one of the above [1] to [4] The body of the above-mentioned (c) filler is 2 to 90 parts by mass with respect to 100 parts by mass of the total of the block copolymer and the (b) isoprene-based rubber and/or the diene-based rubber. The foaming agent according to any one of the above [1] to [5], wherein the above (&) block copolymer, and the above (b) 100 parts by mass of the isoprene-based rubber and/or the diene rubber 157712.doc -6 - 201213426, and further contains: (e) a thermoplastic elastomer and/or a thermoplastic resin 1 to i 〇〇 [7] The foam according to any one of the above [1] to [6] wherein the specific gravity is 〇1 to 〇7 g/cc, or the specific gravity is 〇.8 to 〇98 g/cc. And a composition for foaming, comprising: (4) a block copolymer, wherein the foam is formed by the foam of any one of the above [丨] to [7]. It contains at least 2 vinyl aromatic hydrocarbons a block of the copolymer and at least one copolymer block comprising a conjugated diene and a vinyl aromatic hydrocarbon, and the content of the vinyl aromatic smoke is 65 to 95% by volume, and the total of the total amount of the diene is 5 to 5 The mass fraction of the vinyl aromatic hydrocarbon polymer contained in the block copolymer is 40 to 98% by mass, and the storage elastic modulus (ε,) at 3 G ° C in the measurement is 3x1〇8

PaU上235x10 PaW下’且動態黏彈性測定之函數之 峰值溫度於8 5 °C以上12 5 °Γ以it f 上以下存在至少1個; (b) 異戊二稀系橡膠及/或二埽系橡膠; (c) 填充劑; (d) 發泡劑; V ()甘入1又共承物與上述(b)異戍二稀系橡膠及/或二烯 糸橡膠之質量比為1〜30/70〜99 ;PaU on 235x10 PaW' and the peak temperature of the function of dynamic viscoelasticity measurement is above 8 5 °C and above 12 5 °Γ at least 1 below it f; (b) Isoprene rubber and/or diterpenoid (c) filler; (d) foaming agent; V () mass ratio 1 and the mass ratio of the above (b) isodecane rubber and/or diene rubber is 1~ 30/70~99;

S 157712.doc 一 201213426 相對於上述⑷嵌段共聚物與上述(b)異戊二稀系橡膠及/ 或二烯系橡膠之合計量1〇〇質量份,而含有上述⑷填充劑 1〜100質量份、上述(d)發泡劑0.1〜3 0質量份。 [10] 一種發泡體,其包含:(a’)嵌段共聚物,其含有至少2個 乙烯基芳香族烴聚合物嵌段、以及至少丨個包含共軛二烯 與乙烯基芳香族烴之共聚物嵌段,且 乙烯基芳香族烴之含量為65〜95質量%、共軛二烯之含 量為5〜35質量。/。, 嵌段共聚物所含有之乙稀基芳香族煙聚合物之嵌段率為 40〜98質量% ; (b)異戊二稀系橡膠及/或二烯系橡膝; Ο)填充劑; (d)發泡劑; 比重為0.1〜0.7 g/cc時,藉由型號c測定之硬度為 45-98 ; 比重為0.8〜〇·98 g/“時,藉由型號a測定之硬度為 6 0 〜9 8。 發明之效果 •根據本㉝明,可獲得硬度、尺寸穩定性、熱成型性及機 械強度優異之主要適合於鞋用中底、鞋墊或外底等之發泡 體。 【實施方式】 以下,對用以實旆土义 只知本發明之形態(以下稱為「本實施形 157712.doc 201213426 態」)進行說明。再者,本發明並不限定於以下之記載 於其要旨之範圍内可進行各種變形而實施。 [發泡體j [第1實施形態之發泡體] 、本實施形態之發泡體中之第1實施形態之發泡體含有下 述成分(a)〜成分(d)。 (:)嵌段共聚物,其含有至少2個乙婦基芳香族烴聚合物嵌 奴、以及至少1個包含共軛二烯與乙烯基芳香族烴之共聚 物嵌段,且 一 乙烯基芳香族烴之含量為65〜95質量%、共軛二稀之含 罝為5〜35質量%, 甘入^又/、聚物所含有之乙稀基芳香族烴聚合物之嵌段率為 40〜98質量%, 動態黏彈性測定中3(rc下之儲存彈性模數(E,)為3χΐ〇8 Pa以上2.35xlG9 pa以下’且動態黏彈性測定之函數㈤之 峰值溫度於85 °C以上125°C以下存在至少1個。 (b)異戊一烯系橡膠及/或二烯系橡膠。 0)填充劑。 (d)發泡劑。 又,本實施形態之發泡體中,係使上述(a)嵌段共聚物與 上述(b)異戊二烯系橡膠及/或二烯系橡膠之質量比為 1〜30/70〜99,進而相對於上述(a)嵌段共聚物與上述(^異 戍二烯系橡膠及/或二烯系橡膠之合計量1〇〇質量份,而含 有上述(c)填充劑1〜1〇〇質量份、上述(d)發泡劑〇丨〜3〇質量 157712.doc 201213426 份之發泡體用組合物交聯而成者比重為〇 H^/cc。 以下對成分(a)〜成分(d)進行說明。 (成分(a):嵌段共聚物) 成分⑷係如上所述般含有乙烯基芳香族烴與共耗二稀之 嵌段共聚物。 成分(a)中之乙稀基芳香族烴之含量為65〜95質量%,較 佳為68〜93質量%,更佳為70〜90質量%。 ^分⑷中之共心^含量為5〜35質量%,較佳為㈣ 質量% ’更佳為1 0〜30質量〇/〇。 人:乙婦基芳香族煙之含量為65〜95質量%、共輛二稀之 3置為5〜35質量%之範圍,則成為發泡體之硬度盘伸長率 及熱成型性之平衡優異者,成為適合於㈣之發泡體。 二分⑷中之乙稀基芳香族烴之含量'及共輪二稀之含 使用紫外線分光光度計,測定對特定波長之光 的及收光度而求得。 40成98^)所含有之乙職芳香族㈣合物之嵌段率為 若乙煤^ A,較佳為5〇〜95質量%,更佳為6〇〜90質量%。 :芳香族烴聚合物之嵌段率為4〇,質量%之範 二=寸穩定性與熱成型性優異者,適合作為鞋用 =基芳香族煙聚合物之嵌段率可藉由成分⑷中之包含 族烴與共耗二烯之無規共聚物鏈 基方香族烴之含量(質量%)來調整。 里及烯 構成成分⑷嵌段共聚物之無規共聚物鏈中所佔有之乙稀 157712.doc 201213426 芳香知*工量越多’則乙稀基芳香族烴聚合物之後段率降 低’越少則嵌段率變高。 至於乙婦基芳香族煙聚合物之錢率,係應用將四氧化 鐵作為觸媒藉由過氧化第三丁醇將成分⑽段共聚物氧化 刀解之方法(氧化分解法·· j M k〇lth〇ff,αL Polym. Sci. 1,429 (1946)所記載之方法),將乙稀基芳香族 烴:合物嵌段鏈成分(其中平均聚合度為約30以下之乙烯 基方香族烴聚合物成分除外)分離,測定該乙稀基芳香族 烴聚合物嵌段鏈之重量,根據下述式而求得。 嵌段率(質量%)=(嵌段共聚物中之乙烯基料族煙聚合 物钱段聚合鏈之重量續段共聚物中之乙縣芳香族煙之 總重量100 再者’「喪段共聚物中之乙烯基芳香族煙之總重量」係 根據聚合時之投入比率或藉由NMR等之分析而长得。 成分(a)含有至少2個乙烯基芳香族烴聚合物嵌段、以及 至少1個包含共軛二烯與乙烯基芳香族烴之共聚物嵌段。 成分(a)之聚合物結構並無特別限制,例如可使用下述通 式所示之線狀嵌段共聚物或輻射狀嵌段共聚物、或咳等聚 合物結構之任意的混合物。又’下述通式所示之輕射狀嵌 段共聚物中,進而至少一個敌段A及/或嵌段鍵結於; X。 (Α-Β)η+1 ' Α-(Β-Α)η ' Β-(Α-Β)η+ι、 [(A-B)k]m+i-X、[(A-B)k_A]m+1-X、 [(B-A)ic]m+i-X、[(B-A)k-B]m+1-X、 § 157712.doc 201213426 上述各通式中,嵌段A由乙烯基芳香族烴聚合物構成, 嵌段B由包含共輛二稀與乙縣芳㈣烴之共聚物構成。 上述通式中,X例如表示四氯化矽、四氯化錫、丨,3雙 (N,N-縮水甘油基胺基甲基)環己烷 '環氧化大豆油等偶合 劑之殘基、或多官能有機鋰化合物等起始劑之殘基。 n、k及m分別為i以上之整數,通常為卜5之整數。又, 複數個鍵結之聚合物鏈之結構可相同亦可不同。 構成發泡體所含有之上述成分⑷:嵌段共聚物之嵌段B 中乙稀基芳香族煙與共輥二烯之共聚物中之乙稀基芳香族 烴可均句地分佈,亦可成楔形(漸減)狀分佈。 又’該共聚物中可於嵌段巾分別共存複數個乙稀基芳香 族烴均句分佈之部分及/或成楔形狀分佈之部分。 成刀(a)瓜奴共聚物較佳為含有至少丨個無規共聚物嵌 段,其包含乙烯基芳香族烴含量為7〇質量%未達_質量 幸乂 k為75質量%以上98質量%以下之乙稀基芳香族煙 與共輛二稀。 藉此可獲得硬度與尺寸穩定性良好之發泡體。 <成分(a)嵌段共聚物之製造方法> 成分⑷係可藉由於烴溶劑中將有機經化合物作為起始負 將乙稀基芳香族烴及共_二稀聚合而獲得。 為婦基芳香族您,例如有:苯乙烯、鄰甲基苯乙 烯、對甲基苯乙烯、對第三丁基苯乙烯、1,3-二甲基苯乙 婦af基苯乙歸、乙稀基蔡、乙婦基葱、^卜二苯基乙 稀N,N-—子基_對胺基乙基苯乙婦、n>n_二n㈣| 157712.doc ⑤ •12· 201213426 乙基苯乙料,特別是作為普通者,可列舉苯乙烯。該等 可單獨使用1種,亦可混合2種以上而使用。 為/、軛—烯,為具有丨對共軛雙鍵之二烯烴,例如為 ’3 丁—烯、2_甲基-1,3-丁二烯(異戊二烯)、2,3-二甲基_ 1,3-丁二煤、丨1七_ ,-戊—烯、丨,3_己二烯等,特別是作為普通 者,可列舉丁二稀、異戊二稀等。該等可單獨使们 種,亦可混合2種以上而使用。 正作為溶劑,例如可使用:正丁烷、異丁烷、正戊烷、 、烷正庚烷、正辛烷等脂肪族烴類,環戊烷、甲基環 戊f己烧、甲基環己烧、環庚燒、甲基環庚燒等脂環 式㈣’又苯、甲苯、二甲苯、乙苯等芳香族烴等。該等 可單獨使用1種,亦可併用2種以上。 作為進行成分(a)之聚合時的聚合起始劑通常可使用: 十;八輛一稀及乙稀基芳香族化合物具有陰離子聚合 活性之脂肪族烴驗金屬化合物、芳香族烴鹼金屬化合物、 有機胺基驗金屬化合物等。 土作為構成該等之驗金屬,可列舉經、鈉、鉀等,作為較 :圭之有機鹼金屬化合物,可列舉:為碳數卜2〇之脂肪族及 芳香奴烴鋰化合物,且丨分子中具有丨個鋰之化合物或1分 子中具有複數個鋰之二鋰化合物、三鋰化合物 '四鋰化合 物0 具體可列舉:正丙基鋰、正丁基鋰、第二丁基鋰、第三 丁基鋰、六亞甲基二鋰、丁二烯基二鋰、異戊二烯基二 鋰 '二異丙烯基苯與.第二丁基鋰之反應產物、進而二乙烯 157712.doc 5 •13· 201213426 基苯與第二丁基心及少量1,3·Τ二狀反應產物等。 進而亦可使用美國專利第5,,㈣號說明書、英國專 利第2」241,239號說明書、美國專利第5,527,753號說明書等 斤揭丁之有機驗金屬化合物。該等可單獨使们種,亦可 併用2種以上。 衣以成刀(a)時的聚合溫度通常為〗〇。匚〜15〇它、較佳 40°C 〜120。(:。 聚。所需要之時間根據條件而不同,通常為ι〇小時以 内’特佳為0.5〜5小時。 又’聚合體系之環境氣體較佳為以氮氣等惰性氣 行置換。 聚合壓力只要於對在上述聚合溫度範圍㈣單體及溶劑 維持為液層而充分之壓力的範圍即可,並無特別限制。 進而較佳為加以留意而使將觸媒及活性聚合物惰性化之 雜質例如水、氧氣、二氧化碳等不混人至聚合體系内。 成分(a):嵌段共聚物係含有至少2個乙烯基芳香族烴聚 合物嵌段、以及至少丨個包含共軛二烯與乙烯基芳香族烴 之共聚物嵌段的嵌段共聚物。 為了製成此種構成,而於成分(a”嵌段共聚物之聚合步 驟中,控制投入成為原料之單體的乙烯基芳香族化合物^ 共輕二烯化合物之時序即可β 成分(a):嵌段共聚物中乙烯基芳香族烴之含量為65 質量°/。、共軛二烯之含量為5〜35質量%。 為了製成此種構成,只要於成分(a):嵌段共聚物之聚合 157712.doc -14- 201213426 步驟中,調整成為原料之單體的乙烯基芳香族化合物、丘 軛二烯化合物之投入量即可。 八 又,成分(a):嵌段纟聚物含有至少1個包含乙稀基芳香 • 族煙含量為7〇質量。/〇以上未達⑽質量% '較佳為75質量% 卩上98質量%以下之乙烯基芳香族烴與共軛二烯之無規共 為了製成此種構成,只要於成分(a)··嵌段共聚物之製造 步驟中’於無規嵌段之聚合㈣中,冑整成為原料之單體 之投入量即可。 <成分(a):嵌段共聚物之物性> 如上所述,成分(a).嵌段共聚物中,動態黏彈性測定中 3〇°C下之儲存彈性模數(E,)為3x1〇8 pa以上2 35χΐ〇9 &以 下,且動態黏彈性測定之函數tan§之峰值溫度於85它以上 125°C以下存在至少1個。 較佳為,動態黏彈性測定中30t下之儲存彈性模數(ε·) 為5xl08 Pa以上2.33xlG9 Pa以下,且動態黏彈性測定之函 數taM之峰值溫度於9(rc以上125。〇以下存在至少^固。 表示上述tan5之峰值之溫度係指tan§之值相對於溫度之 變化量的第1次微分值為零的溫度。 在成分(a).嵌段共聚物之動態黏彈性測定中3〇艺下之健 存彈性模數(E')為3xl08 Pa以上2‘35xl09 Pa以下,且動態 黏彈性測定之函數tanS之峰值溫度於85°c以上I25〇c以下 存在至少1個時,本實施形態之發泡體成為硬度與伸長率 及熱成型性之平衡優異者,並且適合於鞋底。 1577I2.doc -15· 201213426 成分(a)之動態黏彈性測定中儲存彈性模數(£,)與^以可 藉由後述實施例中所記載之方法而測定。 例如可藉由Rheology(股)製造之黏彈性測定解析裝置 DVE-V4、或 TOYO Baldwin公司製造之Rhe〇vibr〇n DDV3 型等而測疋’具體而言’可於振盪頻率為35 Hz、升溫速 度3°C/min之條件下,使用厚度為〇 5〜2 mm之試驗片而測 定。 上述動態黏彈性測定中30°C下之儲存彈性模數(E,)可藉 由以下方式而提高,即,於構成上述成分⑷之包含乙稀基 芳香族烴聚合物之嵌段A、與包含含有共輛二烯與乙稀基 芳香族烴之共聚物之嵌段B之比率中,增加嵌段即, 藉由適當調整構成成分(a)之嵌段A與嵌段B之比率,而可 將3〇°C下之儲存彈性模數(E,)控制為3χ1〇8 pa以上2 35χΐ〇9 Pa以下之數值範圍。 成分(a)之動態黏彈性測定之函數tanS之峰值溫度可藉由 以下方式而控制在較高程度,例如增加成分⑷之乙稀基芳 香族煙含ϊ ’增大成分(a)之分子量,將構成成分⑷之包 含乙烯基料㈣與共^狀無規共聚㈣段巾的乙稀 基芳香族烴之比率設為70質量%以上未達1〇〇質量%、較佳 為75貝里/。以上%質量%以下之範圍,於該範圍内增大乙 稀基芳香族烴之比率;反之,藉由以下方式控制在較低程 度將構成成分(a)之包含乙稀基芳香族煙與共輛二稀之無 規聚物攸中的乙烯基芳香族烴之比率設為川質量%以 上未達1〇〇質量%、較佳為75質4%以上%質量%以下之範 157712.doc -16· 201213426 圍,於該範圍内減少乙埽基芳香族煙之比率,並且增加該 無規共聚物嵌段相對於乙烯基芳香族烴均聚物嵌段之比 率。 即,藉由進行上述各種調整,而可將成分(a)之動態黏彈 性測定之函數tan6之峰值溫度控制為85。〇以上125t以 下。 成分(a)之分子量並無特別限定,藉由凝膠滲透層析法 (GPC法)中之聚苯乙烯換算之數量平均分子量,較佳為 30,000〜1,〇〇〇,〇〇〇,更佳為 40 000〜5〇〇 〇〇〇,尤佳為 5〇 〇〇〇〜 300,000 〇 藉由將成分(a)之分子量設定為上述範圍,而可獲得流動 性、加工性優異之發泡體用組合物。 (成分(b):異戊二烯系橡膠及/或二烯系橡膠) 所δ胃異戊一烯系橡膠,係天然橡膠及異戊二烯橡膠,所 謂二烯系橡膠,係笨乙烯•丁二烯共聚合橡膠、聚丁二烯 橡膠、丙烯腈•丁二烯共聚合橡膠、乙烯•丙烯•二烯共 聚合橡膠等’作為構成本實施形態之發泡體之成分(b),可 單獨使用該等’亦可併用2種以上。 成分(b)可含有:石蠟油、環烷油、芳香油等油,或鄰 苯二甲酸二辛酯、鄰笨二曱酸二丁酯、癸二酸二辛酯、己 二酸二辛酯等各種塑化劑。 作為上述石環油’可列舉:出光興產公司製造之DianaS 157712.doc A 201213426 The above (4) block copolymer is contained in combination with the above (b) isoprene rubber and/or diene rubber in an amount of 1 part by mass, and the above (4) filler 1 to 100 is contained. The mass part and the above (d) foaming agent are 0.1 to 30 parts by mass. [10] A foam comprising: (a') a block copolymer comprising at least two vinyl aromatic hydrocarbon polymer blocks, and at least one of which comprises a conjugated diene and a vinyl aromatic hydrocarbon The copolymer block has a vinyl aromatic hydrocarbon content of 65 to 95% by mass and a conjugated diene content of 5 to 35 mass. /. The block ratio of the ethylene-based aromatic tobacco polymer contained in the block copolymer is 40 to 98% by mass; (b) the isoprene-based rubber and/or the diene-based rubber knee; Ο) filler; (d) a foaming agent; when the specific gravity is 0.1 to 0.7 g/cc, the hardness measured by the model c is 45-98; and when the specific gravity is 0.8 to 〇 98 g/", the hardness measured by the model a is 6 0 to 9 8. Effects of the Invention According to the present invention, a foam which is excellent in hardness, dimensional stability, thermoformability and mechanical strength and which is mainly suitable for a midsole, an insole or an outsole for shoes can be obtained. MODES OF THE INVENTION The following is a description of the form of the present invention (hereinafter referred to as "the present embodiment 157712.doc 201213426 state"). It is to be understood that the invention is not limited thereto, and various modifications may be made without departing from the scope of the invention. [Foam j] [Foam of the first embodiment] The foam of the first embodiment of the foam of the present embodiment contains the following components (a) to (d). a (:) block copolymer comprising at least two ethylenic aromatic hydrocarbon polymer inclusions, and at least one copolymer block comprising a conjugated diene and a vinyl aromatic hydrocarbon, and a vinyl aromatic The content of the hydrocarbon is 65 to 95% by mass, the cerium content of the conjugated dilute is 5 to 35% by mass, and the block ratio of the ethylene-based aromatic hydrocarbon polymer contained in the monomer is 40. ~98% by mass, in the dynamic viscoelasticity measurement 3 (the storage elastic modulus (E,) under rc is 3χΐ〇8 Pa or more and 2.35xlG9pa or less' and the peak value of the dynamic viscoelasticity measurement (5) is above 85 °C There is at least one at 125 ° C. (b) Isoprene-based rubber and/or diene-based rubber. 0) Filler. (d) a blowing agent. Further, in the foam of the present embodiment, the mass ratio of the (a) block copolymer to the (b) isoprene-based rubber and/or the diene-based rubber is from 1 to 30/70 to 99. Further, the above (a) block copolymer and the above (^ isocene-based rubber and/or diene-based rubber are contained in a total amount of 1 part by mass, and the above (c) filler 1 to 1 is contained. 〇 mass part, the above (d) foaming agent 〇丨 〇 3 〇 mass 157712.doc 201213426 parts of the foam composition cross-linked to a specific gravity of 〇 H ^ / cc. The following components (a) ~ ingredients (d) (Component (a): Block copolymer) Component (4) contains a block copolymer of a vinyl aromatic hydrocarbon and a divalently dilute as described above. The ethylene group in the component (a) The content of the aromatic hydrocarbon is 65 to 95% by mass, preferably 68 to 93% by mass, more preferably 70 to 90% by mass. The concentric content in the fraction (4) is 5 to 35% by mass, preferably (4). The mass % 'better is 1 0 to 30 mass 〇 / 〇. Person: the content of the ethyl spheroidal aromatic smoke is 65 to 95% by mass, and the total amount of the second diluted glass is set to 5 to 35% by mass. Foaming The hardness of the disk is excellent in the balance between the elongation of the disk and the thermoformability, and is suitable for the foam of (4). The content of the ethylene-based aromatic hydrocarbon in the two-part (4) and the ultraviolet-based spectrophotometer are used in the mixture of the two-wheel mixture. The measurement is carried out for the light of a specific wavelength and the light-receiving degree. The block ratio of the aromatic (tetra) compound contained in 40% of 98%) is preferably 5% to 95% by mass. More preferably 6〇~90% by mass. : The block ratio of the aromatic hydrocarbon polymer is 4 〇, the mass % is 2 = the stability of the inch and the thermoformability are excellent, and the block ratio suitable as the shoe-based aromatic smog polymer can be obtained by the component (4) The content (% by mass) of the random copolymer chain-based aromatic hydrocarbon containing the hydrocarbon and the diene is adjusted. Ethylene and olefin constituents (4) The ethylene copolymer occupied by the random copolymer chain of the block copolymer 157712.doc 201213426 The more the aromatics * the amount of work, the lower the rate of the ethylene-based aromatic hydrocarbon polymer is less. Then the block rate becomes high. As for the money rate of the ethylene-based aromatic-smoke polymer, the method of oxidizing and pulverizing the component (10) copolymer by using peroxidized tert-butyl alcohol as a catalyst is used (oxidative decomposition method··j M k 〇lth〇ff, αL Polym. Sci. 1, 429 (1946), which comprises a vinyl chain aromatic component: a block chain component (having an average degree of polymerization of about 30 or less) The mixture of the hydrocarbon polymer components was separated, and the weight of the ethylene-based aromatic hydrocarbon polymer block chain was measured and found according to the following formula. Block ratio (% by mass) = (the weight of the vinyl group in the block copolymer, the weight of the polymer chain, the weight of the polymer chain, the total weight of the aromatic fluoride in the sequent copolymer in the sequent copolymer of 100) The total weight of the vinyl aromatic fumes in the product is obtained according to the input ratio at the time of polymerization or by analysis by NMR, etc. The component (a) contains at least two vinyl aromatic hydrocarbon polymer blocks, and at least A copolymer block comprising a conjugated diene and a vinyl aromatic hydrocarbon. The polymer structure of the component (a) is not particularly limited, and for example, a linear block copolymer or radiation represented by the following formula may be used. a block copolymer, or a mixture of any polymer structure such as cough. Further, in the light-emitting block copolymer represented by the following formula, at least one enemy A and/or block is bonded to; X. (Α-Β)η+1 ' Α-(Β-Α)η ' Β-(Α-Β)η+ι, [(AB)k]m+iX, [(AB)k_A]m+1 -X, [(BA)ic]m+iX, [(BA)kB]m+1-X, § 157712.doc 201213426 In the above formulas, block A is composed of a vinyl aromatic hydrocarbon polymer, embedded Section B consists of a total of two dilute and B (a) hydrocarbons In the above formula, X represents, for example, a coupling agent such as antimony tetrachloride, tin tetrachloride, antimony or tris(N,N-glycidylaminomethyl)cyclohexane'epoxidized soybean oil. a residue of a starting agent such as a residue or a polyfunctional organolithium compound. n, k and m are each an integer of i or more, and are usually an integer of 5. Further, the structure of a plurality of bonded polymer chains may be The same component may be different. The above-mentioned component (4) constituting the foam: the ethylene-based aromatic hydrocarbon in the copolymer of the ethylene-based aromatic cigarette and the co-rolled diene in the block B of the block copolymer The distribution of the ground may also be in the form of a wedge-shaped (decreasing) shape. In the copolymer, the portion of the plurality of ethylene-based aromatic hydrocarbons and the distribution of the wedge-shaped distribution may be coexisted in the block towel. The knife (a) melon copolymer preferably contains at least one random copolymer block containing a vinyl aromatic hydrocarbon content of 7 〇 mass% and less than _ mass 乂 k is 75% by mass or more and 98% by mass. The following ethylene-based aromatic cigarettes and a total of two dilute, which can achieve good hardness and dimensional stability Froth. <Production method of component (a) block copolymer> The component (4) can be obtained by polymerizing an ethylene-based aromatic hydrocarbon and a co-diazole by using an organic compound as a starting negative in a hydrocarbon solvent. Obtained. For your cation-based aromatics, for example: styrene, o-methyl styrene, p-methyl styrene, p-tert-butyl styrene, 1,3-dimethyl phenyl ethene , Ethyl group, Ethyl onion, ^ diphenylethylene N, N--subunit _ p-aminoethyl benzene, n > n_ two n (four) | 157712.doc 5 •12· 201213426 Ethyl styrene, particularly as an ordinary one, may be styrene. These may be used alone or in combination of two or more. a / yoke-ene, a diene having a fluorene pair conjugated double bond, such as '3 butyl-ene, 2-methyl-1,3-butadiene (isoprene), 2,3- Dimethyl _ 1,3-butane coal, ruthenium sulphate, pentane-ene, fluorene, 3-hexadiene, etc., particularly as ordinary ones, may include dibutyl sulphate and isoprene. These may be used alone or in combination of two or more. As the solvent, for example, an aliphatic hydrocarbon such as n-butane, isobutane, n-pentane, an alkyl-n-heptane or n-octane, cyclopentane, methylcyclopentane, or a methyl ring can be used. Alicyclic, cycloheptane, methylcycloheptane and other alicyclic (four) '-benzene, toluene, xylene, ethylbenzene and other aromatic hydrocarbons. These may be used alone or in combination of two or more. As the polymerization initiator for carrying out the polymerization of the component (a), generally: ten; eight aliphatic and ethylenic aromatic compounds having an anionic polymerization activity, an aliphatic hydrocarbon metal compound, an aromatic hydrocarbon alkali metal compound, An organic amine based metal compound or the like. As the organic metal constituting the above-mentioned materials, examples include a solution of sodium, potassium, etc., and as an organic alkali metal compound of the formula: an aliphatic and aromatic lithium compound which is a carbon number and a samarium compound A compound having one lithium or a lithium compound having a plurality of lithium in one molecule, and a tetralithium compound 'tetralithium compound 0 can be specifically exemplified by n-propyl lithium, n-butyl lithium, second butyl lithium, and third butyl. Reaction product of lithium, hexamethylene dilithium, butadienyl dilithium, isoprenyl dilithium 'diisopropenylbenzene and second butyl lithium, and further diethylene 157712.doc 5 •13 · 201213426 Base benzene and second butyl core and a small amount of 1,3·Τ dimorphic reaction products. Further, it is also possible to use an organic metal test compound which is disclosed in U.S. Patent No. 5, (4), British Patent No. 2, No. 2,241,239, and U.S. Patent No. 5,527,753. These may be used alone or in combination of two or more. The polymerization temperature at the time of forming the knife (a) is usually 〇.匚~15〇 It is preferably 40°C~120. (:. Poly. The time required varies depending on the conditions, usually within ι〇 hours, particularly preferably 0.5 to 5 hours. Further, the ambient gas of the polymerization system is preferably replaced by an inert gas such as nitrogen. The range in which the monomer and the solvent are maintained in the liquid layer in the polymerization temperature range (4) is not particularly limited. Further, it is preferable to note impurities such as inerting the catalyst and the living polymer. Water, oxygen, carbon dioxide, etc. are not mixed into the polymerization system. Component (a): The block copolymer contains at least 2 vinyl aromatic hydrocarbon polymer blocks, and at least one of the conjugated diene and vinyl groups. a block copolymer of a copolymer block of an aromatic hydrocarbon. In order to obtain such a composition, in the polymerization step of the component (a" block copolymer, a vinyl aromatic compound which is a monomer which is a raw material is controlled. The timing of the common light diene compound can be β component (a): the content of the vinyl aromatic hydrocarbon in the block copolymer is 65 mass%, and the content of the conjugated diene is 5 to 35 mass%. Such composition In the step of the polymerization of the component (a): block copolymer 157712.doc -14-201213426, the amount of the vinyl aromatic compound or the yoke conjugated compound which is a monomer of the raw material may be adjusted. , component (a): block bismuth polymer containing at least one aromatic group containing a group of aromatics; mass content of 7 〇 mass. / 〇 or more up to (10) mass% 'preferably 7 mass% 卩 98% by mass or less of ethylene In order to obtain such a configuration, the aromatic hydrocarbon and the conjugated diene are formed in a random manner in the polymerization step (four) of the component (a)·block copolymer. The amount of the monomer of the raw material may be. <Component (a): Physical properties of the block copolymer> As described above, in the component (a). Block copolymer, the dynamic viscoelasticity measurement is 3 〇 ° C The storage elastic modulus (E,) is 3x1 〇 8 pa or more and 2 35 χΐ〇 9 & below, and the peak temperature of the function of the dynamic viscoelasticity measurement tan § is at least one of 85 or more and 125 ° C or less. Therefore, the storage elastic modulus (ε·) at 30t in the dynamic viscoelasticity measurement is 5xl08 Pa or more 2.33xlG9 P a is below, and the peak temperature of the function of the dynamic viscoelasticity measurement taM is 9 (rc or more 125. There is at least a solid below the 。. The temperature indicating the peak of the above tan 5 is the first change in the value of tan § with respect to temperature. The temperature at which the sub-differential value is zero. In the dynamic viscoelasticity measurement of the component (a). The block copolymer has a storage modulus (E') of 3xl08 Pa or more and 2'35xl09 Pa or less, and dynamic When the peak temperature of the function of the viscoelasticity measurement is at least one of 85 ° C or more and I25 ° C or less, the foam of the present embodiment is excellent in the balance of hardness, elongation, and thermoformability, and is suitable for the sole. 1577I2.doc -15·201213426 The storage elastic modulus (£, ) and ^ in the dynamic viscoelasticity measurement of the component (a) can be measured by the method described in the examples below. For example, it can be measured by the viscoelasticity measuring and analyzing device DVE-V4 manufactured by Rheology, or the Rhe〇vibr〇n DDV3 type manufactured by TOYO Baldwin Co., Ltd., etc., specifically, the oscillation frequency is 35 Hz, and the temperature is raised. The test piece having a thickness of 〇5 to 2 mm was measured under the conditions of a speed of 3 ° C/min. The storage elastic modulus (E,) at 30 ° C in the above dynamic viscoelasticity measurement can be improved by, for example, the block A containing the ethylene-based aromatic hydrocarbon polymer constituting the above component (4), and In the ratio of the block B containing the copolymer of the common diene and the ethylene aromatic hydrocarbon, the block is increased, that is, by appropriately adjusting the ratio of the block A to the block B of the component (a), The storage elastic modulus (E,) at 3 ° C can be controlled to a value range of 3 χ 1 〇 8 Pa or more and 2 35 χΐ〇 9 Pa or less. The peak temperature of the function of dynamic viscoelasticity of the component (a) can be controlled to a high degree by, for example, increasing the molecular weight of the ethylenic aromatic smoulder of the component (4) to increase the component (a). The ratio of the vinyl-containing (4) component of the component (4) to the ethylene-based aromatic hydrocarbon of the copolymerized (four) segmented towel is 70% by mass or more and less than 1% by mass, preferably 75 Å/y. . The range of the above % by mass or less, in which the ratio of the ethylene-based aromatic hydrocarbon is increased; on the contrary, the ethylene-containing aromatic smoke of the constituent (a) is controlled to a lower degree by the following means. The ratio of the vinyl aromatic hydrocarbon in the divalent random polymer enthalpy is not more than 1% by mass, more preferably 75% by mass or more, and 5% by mass or less. 16·201213426, in which the ratio of the ethyl ketone aromatic smoke is reduced, and the ratio of the random copolymer block to the vinyl aromatic hydrocarbon homopolymer block is increased. That is, by performing the above various adjustments, the peak temperature of the function tan6 of the dynamic viscoelasticity measurement of the component (a) can be controlled to 85. 〇 Above 125t. The molecular weight of the component (a) is not particularly limited, and the number average molecular weight in terms of polystyrene in the gel permeation chromatography (GPC method) is preferably 30,000 to 1, 〇〇〇, 〇〇〇, and more. The foam having a fluidity and workability can be obtained by setting the molecular weight of the component (a) to the above range, preferably from 40 Å to 5 Torr, and more preferably from 5 Å to 300,000 Å. Use the composition. (Component (b): Isoprene-based rubber and/or diene-based rubber) δ-gas isoprene-based rubber, natural rubber and isoprene rubber, so-called diene rubber, stupid ethylene • Butadiene copolymerized rubber, polybutadiene rubber, acrylonitrile butadiene copolymerized rubber, ethylene/propylene/diene copolymerized rubber, etc., as component (b) constituting the foam of the present embodiment, These may be used alone or in combination of two or more. Ingredient (b) may contain oils such as paraffin oil, naphthenic oil, aromatic oil, or dioctyl phthalate, dibutyl phthalate, dioctyl sebacate, dioctyl adipate. And other plasticizers. As the above-mentioned stone ring oil, the Diana manufactured by Idemitsu Kosan Co., Ltd. can be cited.

Process Oil pw-90、pw-380、PS-32、PS-90、PS-430,富 土興產公司製造之Fukkol Process P-100、P-200、p_3〇〇、 157712.doc -17- 201213426 p_4〇〇、P-500,曰礦共石公司製造之Kyoseki Process P-200、P-300、P-500、Kyoseki EPT750、Kyoseki 1000、 Kyoseki Process S90,Shell Chemicals公司製造之Lubrex 26 ' Lubrex 100、Lubrex 460,Exxon Mobil公司製造之 Esso Process Oil 815 ' Esso Process Oil 845 ' Esso Process Oil B-l,Exxon Mobil公司製造之Naprex 32 ’新日本石油 公司製造之 Mitsubishi 10 Light Process Oil等。 作為上述環烷油,可列舉:出光興產公司製造之DianaProcess Oil pw-90, pw-380, PS-32, PS-90, PS-430, Fukkol Process P-100, P-200, p_3〇〇, 157712.doc -17- 201213426 P_4〇〇, P-500, Kyoseki Process P-200, P-300, P-500, Kyoseki EPT750, Kyoseki 1000, Kyoseki Process S90 manufactured by Yankuang Co., Ltd., Lubrex 26 'Lubrex 100 manufactured by Shell Chemicals Co., Ltd. Lubrex 460, Esso Process Oil 815 'Esso Process Oil 845 ' manufactured by Exxon Mobil Co., Ltd. Esso Process Oil Bl, Naprex 32 manufactured by Exxon Mobil Co., Ltd., Mitsubishi 10 Light Process Oil, manufactured by Nippon Oil Corporation. As the above naphthenic oil, Diana manufactured by Idemitsu Kosan Co., Ltd. can be cited.

Process Oil NS-24、NS-100、NM-26、NM-280、NP-24, Exxon Mobil公司製造之Naprex 38,富士興產公司製造之 Fukkol FLEX # 1060N、# 1150N、# 1400N ' # 2040N、 # 2050N,日礦共石公司製造之Kyoseki Process R25、 R50 ' R200 ' R1000 9 Shell Chemicals公司製造之 Shellflex 371JY、Shellflex 371N、Shellflex 451、Shellflex N-40、 Shellflex 22、Shellflex 22R、Shellflex 32R、Shellflex 100R、Shellflex 100S、Shellflex l〇〇SA、Shellflex 220RS、Shellflex 220S、Shellflex 260、Shellflex 320R、 Shellflex 680,新日本石油公司製造之Koumorex No.2 Process Oil,Exxon Mobil公司製造之Esso Process Oil L-2、Esso Process Oil 765 ’新日本石油公司製造之 Mitsubishi 20 Light Process Oil等。 作為上述芳香油,可列舉:出光興產公司製造之Diana Process Oil AC-12 ' AC460 ' AH-16 ' AH-58 ' ExxonProcess Oil NS-24, NS-100, NM-26, NM-280, NP-24, Naprex 38 manufactured by Exxon Mobil, Fukkol FLEX # 1060N, # 1150N, # 1400N ' # 2040N, manufactured by Fujising Co., Ltd. # 2050N, Kyoseki Process R25, R50 'R200 ' R1000 manufactured by Nippon Mining & Co., Ltd. R1000 9 Shellflex 371JY, Shellflex 371N, Shellflex 451, Shellflex N-40, Shellflex 22, Shellflex 22R, Shellflex 32R, Shellflex 100R manufactured by Shell Chemicals , Shellflex 100S, Shellflex l〇〇SA, Shellflex 220RS, Shellflex 220S, Shellflex 260, Shellflex 320R, Shellflex 680, Koumorex No. 2 Process Oil manufactured by Nippon Oil Corporation, Esso Process Oil L-2 manufactured by Exxon Mobil, Esso Process Oil 765 'Mitsubishi 20 Light Process Oil manufactured by Nippon Oil Corporation. As the above-mentioned aromatic oil, Diana Process Oil AC-12 'AC460 ' AH-16 ' AH-58 ' Exxon manufactured by Idemitsu Kosan Co., Ltd.

Mobil公司製造之Mobile Sol K、Mobile Sol 22、Mobile 157712.doc -18- 201213426Mobil's Mobile Sol K, Mobile Sol 22, Mobile 157712.doc -18- 201213426

Sol 130,日礦共石公司製造之Kyoseki Process X50、 X100、X140 ’ Shell Chemicals 公司製造之 Rezox Νο·3、 Dutorex 729UK,新日本石油公司製造之Koumorex 200、 300、500、700,Exxon Mobil公司製造之Esso Process Oil 110、Esso Process Oil 120,新日本石油公司製造之 Mitsubishi 34 Heavy Process Oil、Mitsubishi 44 Heavy Process Oil、Mitsubishi 38 Heavy Process Oil、Mitsubishi 39 Heavy Process Oil等。 塑化劑之調配量相對於成分(b) 100質量份,較佳為 1〜200質量份,更佳為10〜100質量份,尤佳為15〜8〇質量 份。 若塑化劑之調配量為1〜200質量份,則本實施形態之發 泡體成為加工性優異者。 作為成分(b),可列舉聚丁二烯作為較佳例,作為聚丁 二烯橡膠,亦包括:包含1,2鍵(乙烯基)5%〜20%、包含反 1,4鍵0〜3%、其餘成分為順ι,4鍵之乙烯基順聚丁二烯橡 膠’或包含順1,4鍵92%以上、包含ι,2鍵〇%〜3%、其餘成 分為反1,4鍵之橡膠的高順聚丁二烯橡膠等。 於本實施形態之第1實施形態之發泡體中’上述成分 與成分(b)之質量比(成分(a)/成分〜3〇)/(7〇〜99),較 佳為(2~25)/(75〜98),更佳為(5〜20)/(80~95)。 若成分(a)與成分(b)之質量比為(1〜30)/(70-99),則發泡 體可獲得優異之硬度及尺寸穩定性。 (成分(c):填充劑) 157712.doc -19- 201213426 :為填充劑’例如可列舉:二氧切碳酸妈黏土、 ΠΓ、硫酸銷、破酸鎮'玻璃織維、玻璃珠、欽酸 卸炭黑、石厌二氧化石夕、雙相填料等。 第1實施形態之發泡體中搶古 一 忍體中填充劑之調配量相對於上述 成为(a)與成分(b)之合計量1〇〇曾 里 貝里份,為1〜100質量份, 較佳為2〜90質量份,更佳為3 7 曰 、 尺佳马3 75質1份,尤佳為5〜50質量 份0 、 若成分⑷:填充劑之調配量為Η。。質量份,則本實施 形態之發泡體可獲得較佳之硬度及較佳之比重。 (成分(d):發泡劑) 作為發泡劑,例如可使用其本身公知之無機發泡劑或有 機發泡劑。 例如可列舉:重碳酸鈉、重碳酸 至反敗钕、妷酸鈉、碳酸銨、 偶氮一甲酿胺、二亞石肖.¾. X n m 兄月丞五亞曱基四胺、二亞硝基對笨二 曱酿胺、偶氮二異丁腈、偶氮二甲酸 »又识 τ本石頁酿肼等錯 酿肼類等。特別是更佳為偶氮二甲酿胺、二亞硝基五亞= 基四胺、磺醯肼類、重碳酸鈉。該等發泡劑可併二 衍生物等公知的發泡助劑。 又,作為發泡劑’可使用熱膨脹性微膠囊。 該熱膨脹性微膠囊係包含熱塑性中空球體之發包粒子 且包含含有包住氣體之熱塑性樹脂之殼(shell)所者。 若將該熱膨服性微膠囊加熱’則熱塑性殼备 ^ 曰,氣體 會增大壓力,結果球體膨脹而發揮出作為發泡劑的作用 作為構成上述微膠囊之殼的熱塑性樹脂,例如 ° J列舉: 157712.doc •20- 201213426 偏二氯乙烯-丙烯腈共聚物、偏二氯乙烯_甲基丙烯酸甲酯 共^^物、偏一氯乙婦_子基丙婦酸乙|旨、丙稀腈-甲基丙婦 酸甲酯共聚物、丙烯腈-f基丙烯酸乙酯等。 又’作為藉由加熱而變成氣體之化合物,可列舉異戊 烷、異丁烷、異丙烷等。 熱膨脹性微膠囊之質量平均粒徑通常為〗0〜丨00 pm,較 佳為20〜80 μηι左右。 作為熱膨脹性微膠囊,例如可列舉:JApAN fillite股 份有限公司製造之expancel DU、wu系歹J,松本油脂公 司製造之Microsphere F-30、F-50、F-80S、F-85 等。 若將熱膨腸性微膠囊用作發泡劑,則藉由加熱,隨著各 微膠囊所内藏的氣體生成成分之氣體化而均句膨服,而可 獲得均質之發泡體。 吸熱性發泡劑作為發泡 用,因此較佳。 二甲醯胺 '二亞硝基五 再者’藉由併用發熱性發泡劑與 劑’而可抑制發泡成型時之發熱作 作為發熱性發泡劑,可列舉偶氮 亞甲基四胺等。 又’作為吸熱性發泡劑,可列與#成 夕J舉奴酸虱鈉等,此時,產 生氣體為二氧化碳。 第1實施形態之發泡體中,成分 刀(d) ·發泡劑之調配量相 對於上述成分⑷與成分⑻之人 、《计1 100質量份,而為 0.1-30質量份’較佳為〇 5〜2〇 Λ里份,更佳為1〜15質量 份0 若成分(d):發泡劑之調配量从1,質量份,則本實施 157712.doc .21· 201213426 形態之發泡體可獲得優異之硬度,且比重達到較佳值。 (成分(e):熱塑性彈性體及/或熱塑性樹脂) 本實施形態之發泡體中除了上述成分(a)〜成分(d)外,還 可含有成分(e):熱塑性彈性體及/或熱塑性樹脂。 作為熱塑性彈性體,例如若根據硬鏈段之化學組成之分 類,則可列舉.稀煙系熱塑性彈性體(TPO)、胺基甲酸酯 系熱塑性彈性體(TPU)、酯系熱塑性彈性體(TpEE)、酿胺 系熱塑性彈性體(TPAE)等。 又,此外,有氣乙烯系熱塑性彈性體(Tpvc)、離子簇型 熱塑性彈性體(離子聚合物)' 含有氟樹脂作為拘束嵌段之 氟系熱塑性彈性體等(再者,有時將藉由利用樹脂/橡膠混 合之熱塑性彈性體中,一面使成為軟鏈段之橡膠交聯一面 混練,將橡膠分散粒徑細化,而提高性能之動態交聯之 TPO稱為TPV)。上述熱塑性彈性體可單獨使用!種,亦可 併用2種以上。 又,作為其他熱塑性彈性體,可使用上述成分(a)或成分 (b)以外之合成橡膠,可列舉:氟橡膠、聚矽氧橡膠 '南2 丁基橡膠(例如氯化丁基橡膠、溴化丁基橡膠等)等,該等 可單獨使用1種,亦可併用2種以上。 作為熱塑性樹脂,若為可塑化溫度為5〇〜3〇(Kc之熱塑性 樹脂,則可無特別限制地使用。 例如可列舉··苯乙烯系樹脂(例如聚苯乙烯、丙烯腈· 苯乙烯共聚物'丙烯腈·丁二烯•苯乙烯共聚物等)、 ABS(AcryI〇nitrile Butadiene Styrene,丙烯腈 _丁二婦苯乙 I57712.doc •22- 201213426 婦)树脂、AES(Acrylonitrile-Ethylene-Styrene,丙稀猜·乙 稀-表乙烯)樹脂、AAS(Acrylnitrile-Acrylicester-Styrene, 丙烯腈丙烯酸酯_苯乙烯)樹脂、聚乙烯、聚丙烯、乙烯· 丙烯樹脂、乙烯-丙烯酸乙酯樹脂、聚氯乙烯、聚偏二氣 乙烯、聚丁烯、聚碳酸酯、聚縮醛、聚苯醚、聚甲基丙烯 酸甲醋、飽和聚酯樹脂(例如聚乳酸之類的羥基羧酸縮合 物、聚丁二酸丁二酯之類的二醇與二羧酸之縮合物等)、 聚醯胺樹脂、氟樹脂、聚砜、聚醚砜、聚芳酯、聚醚醚 酮液晶聚合物等。該等可單獨使用1種,亦可併用2種以 上。 熱塑性樹脂中較佳者為聚苯乙烯、丙稀腈.苯乙烯共聚 物、ABS樹脂、AES樹脂、AAS樹脂' 聚乙烯、聚丙烯、 聚氣乙烯、飽和聚酯樹脂、聚醯胺樹脂。 藉由調配該等熱塑性樹脂,而於本實施形態之發泡體之 成型體中’可防止凹痕或變形,而較佳。 至於成分(e):熱塑性彈性體及/或熱塑性樹脂之調配 量,相對於成分(a)與成分(b)之合計量1〇〇質量份,較佳為 1〜1〇〇質量份,更佳為3〜75質量份,尤佳為5〜5〇質量份。 若成分(e):熱塑性彈性體及/或熱塑性樹脂之調配量為 1〜100質量份’則本實施形態之發泡體可獲得較佳之機械 強度。 (發泡體用組合物) 用以獲得本實施形態之第1形態的之發泡體的發泡體用 組合物係:包含上述成分(a)〜成分(d),上述成分(a)嵌段共 157712.doc -23· 201213426 聚物與上述(b)異&amp;二缔系橡膠及/或:稀系橡膠之質量比 (成刀(a)/成分(b))為(1〜3〇)/(7〇〜99)、較佳為(2〜25)/(75〜98)、 更佳為(5〜20)/(80〜95),相對於上述(a)嵌段共聚物與上述 (b)異戊二烯系橡膠及/或二烯系橡膠之合計量丨⑽質量份而 含有上述(c)填充劑1〜100質量份、較佳為2〜9〇質量份、更 佳為3〜75質量份、尤佳為5〜5〇質量份,含有上述(句發泡 d 0.1〜30質ϊ份、較佳為〇 5〜2〇質量份、更佳為丨〜質量 份。 又,可含有成分(e) ’較佳為相對於成分(a)與成分(1?)之 α计里100質量份,而含有卜丨⑼質量份、更佳為3〜75質量 份、尤佳為5〜50質量份。 製備發泡體用組合物時,可使用先前公知之混練機、擠 出機等。 又,作為(c)填充劑、(d)發泡劑等之調配方法、調配順 序例如可列舉·預先藉由班布裏混合機等使成分(a)、成 分〇3)於100〜180。〇下熔融混練,將所得者使用班布裏混合 機等與(C)填充劑調配後,使用輥等添加(d)發泡劑、交聯 劑等之方法,但並不限定於此。 [發泡體] [第2實施形態之發泡體] 第2實施形態之發泡體含有下述成分(a,)〜成分(句。 (a1)嵌段共聚物’其含有至少2個乙烯基芳香族烴聚合物嵌 段、以及至少1個包含共軛二烯與乙烯基芳香族烴之共聚 物嵌段,且 ’ 157712.doc -24- 201213426 乙稀基芳香族烴之含量為65〜95質 量為5〜35質量%, 質里/。、共輛二烯之含 嵌段共聚物所含有之乙縣料族㈣ 40〜98質量%。 职仅午為 (b) 異戊二埽系橡膠及/或二烯系橡膠。 (c) 填充劑。 (d) 發泡劑。 第2實施形態之發泡體於比重為〇1 n ^ 〇*7 g/cc時,藉由型 唬c測疋之硬度為45〜98,於比重為〇 8〜〇 ^ 型號八測定之硬度為6〇〜98。 ' gee時’错由 (成分(a'):嵌段共聚物) 成分(a’)係如上所述般含有乙稀基芳香族㈣ 之嵌段共聚物。 、八视一烯 成分⑻中之乙稀基芳香族烴之含量_〜95質量。4 佳為68〜93質量%,更佳為70〜90質量%。 。較 成分(a,)中之共軛二烯之含量為、% 7〜32質量°/。,更佳為10〜30質量%。 置。’較佳為 若乙烯基芳香族烴之含量為65〜95 含量為5〜35質量%之範圍,則成為發泡體之硬2-婦之 及熱成型性之平衡優異者,成為適合於鞋用伸長率 成分⑷)中之乙烯基芳香族烴之含量、w包體。 量广由使用紫外線分光光度計,測定相; 之光的吸收光度而求得。 寻疋波長 成分⑻所含有之乙婦基芳香族煙聚合物之嵌段率為 5 157712.doc -25- 201213426 4 0〜98質量%,較佳. 若乙婦芙-意 #量。更佳為6〇〜90質量%。 婦基…煙聚合物之嵌段率為4 圍,則成為尺寸穩輕與熱成㈣❹者,適合^ = 之發泡體。 i σ作為鞋用 Α乙烯基芳香族烴聚合物之嵌段率可藉由成分⑻中之包 香族煙與共輕二嫦之無規共聚物鏈之重量及乙 烯基方香知烴之含量(質量%)來調整。 構^成分(A純共聚物之無規共聚物鏈巾所佔有之乙 稀基芳香族烴量越多1乙烯基芳香族烴聚合物之嵌段率 降低,越少則嵌段率變高。 乙縣芳香族烴聚合物之嵌段率可藉由與上述成分⑷相 同之方法而求得。 成刀(a )具有至少2個乙烯基芳香族烴聚合物嵌段 '以及 至少1個包含共輛二埽與乙婦基芳香族烴之共聚物钱段。 成分〇’)之聚合物結構並無特別限制,例如可使用下述 通式所示之線狀嵌段共聚物或輻射狀嵌段共聚物、或該等 聚合物結構之任意的混合物。又’下述通式所示之輻射狀 嵌段共聚物中’進而至少一個嵌段八及,或嵌段3可鍵結於 X。 (A-B)n+1、A-(B-A)n、B-(A-B)n+丨、 [(A-B)k]m+1-X &gt; [(A-B)k-A]m+,-X &gt; [(B-A)k]m+1-X、[(B-A)k-B]m+1-X、 上述各通式中’嵌段A由乙烯基芳香族烴聚合物構成, 欣^又B由包含共扼二婦與乙細基芳香族烴之共聚物構成。 157712.doc -26- ⑤ 201213426 上述通式中’x例如表示四氯化石夕、四氯化錫、u雙 (N’N-縮水甘油基胺基甲基)環己院、環氧化大豆油等偶合 劑之殘基、或多官能有仙化合物之殘基。 n、k&amp;m分別為1以上之整數、通常為卜5之整數。又, 複數個鍵結之聚合物鏈之結構可相同亦可不同。 構成發泡體所含有之上述成分(a,):嵌段共聚物之嵌段B 中的乙烯基芳香族烴與共軛二烯之共聚物中之乙烯基芳香 族煙可均勻分佈,亦可成模形(漸減)狀分佈。 又:該共聚物中’可於嵌段中分別共存複數個乙烯基芳 香族煙均句分佈之部分及/或成楔形狀分佈之部分。 成刀(a ).肷&amp;共聚物較佳為含有至少⑽無規共聚物歲 段’其包含乙婦基芳香族煙含量為7〇質量%未達ι〇〇質量 %、較佳為75質量%以上98質量%以下之乙烯基芳香族烴 與共輛二稀。 藉此,可獲得硬度與尺寸穩定性良好之發泡體。 &lt;成分(a )欣段共聚物之製造方法〉 成分(a’)可藉由與上述成分⑷相同之方法而製造。 關於成為原料之乙稀基料族烴、絲:烯、烴溶劑、 聚合起始料,可❹與成分⑷相同之材料。 進而’關於聚合溫度、環境氣體等聚合條件,亦可選擇 與成分(a)相同之條件。 &lt;成分(a ).嵌段共聚物之物性〉 成刀(a )嵌奴共聚物較佳為動態黏彈性測定中3〇。〇下 之健存彈性模數⑽為3xl〇8 pa以上2.35χΐ〇9 以下,且 157712.doc -27- 201213426 較佳為動態黏彈性測定之函編之峰值溫度於饥以上 125C以下存在至少1個。 更佳為動態黏彈性浪丨定φ ^ η。广 利疋中30 C下之儲存彈性模數(Ε,)為 5xl08 Pa 以上 2.33x1〇9 Pa 以下,B s „ 上 乂下且更佳為動態黏彈性測定 之函數tan5之峰值温度於9(rc以上U5t以下存在至少ι 個。 藉此’發泡體成為硬度與伸長率及熱成型性之平衡優異 者’成為適合於鞋底者。 成分(a,)之分子量並無特別限定’藉由凝膠滲透層析法 (GPC法)中之聚苯乙烯換算之數量平均分子量’較佳為 30.000 1,〇〇〇,〇〇〇’ 更佳為4〇,〇〇〇〜5〇〇 〇〇〇,尤佳為 5〇 〇〇〇〜 300.000 〇 藉由使成分(a')之分子量為上述範圍,而可獲得流動 性、加工性優異之發泡體用組合物。 關於構成第2實施形態之發泡體之成分(b)、成分(c)、及 成勿(d) ’可使用與上述第1實施形態之發泡體相同之材 料。 又’於第2實施形態之發泡體中,亦可含有成分(e)。 [發泡體之製造方法] 本實施形態之第1實施形態之發泡體係將上述成分(a)、 成分(b)、成分(c)及成分(d)作為必須成分,第2實施形態之 發泡體係將上述成分(a》、成分(b)、成分(c)、及成分(d)作 為必須成分,分別根據需要添加成分(e)而製備發泡體用組 合物’並對該發泡體用組合物實施發泡·交聯處理而獲 157712.doc -28- 201213426 得。 (發泡•交聯處理) 於使上述發泡體用組合物 柳赞/a之步驟中,可藉由以下方 式獲得發泡體··藉由加人至㈣模具内提高溫度而進行發 泡,或使用擠出成型機成型為任意形狀後,於加熱槽内加 熱而進行發泡。 此時之發泡於進行1次發泡後,亦可進行2次發泡而提高 發泡倍率。 發泡條件較佳為將加熱溫度設定為ΐ2〇〜3()(η:,更佳為 140-200 C之範圍,較佳為將加熱時間設定為3分鐘, 更佳為設定為5〜6 0分鐘之範圍。 上述發泡過程中,可同時進行交聯。 本實施形態之發泡體之交聯形態並無特別限制,例如可 應用硫交聯、過氧化物交聯等。 就發泡體之成本及強度之觀點而言,較佳為硫交聯。 又,該發泡體根據需要可調配適量之石夕烷化劑、石夕烷偶 合劑、抗老化劑、硫化加速劑、交聯助劑 [發泡體之物性] 本實施形態之發泡體之比重於第i實施形態及第2實施形 態之發泡體中均為0.1〜0.98 g/cc ’較佳為〇% g/cc。 比重可藉由後述實施例所記載之方法而測定。具體而 言,可依據JIS K 7 112而測定。 比重為0·卜0.7 g/cc之發泡體適合用於要求緩衝性或衝擊 緩衝性、輕里等特性之用途、例如運動鞋等之中底材料。 § 157712.doc -29- 201213426 比重為0·8〜0.98 g/cc之發泡體適合用於要求硬度、尺寸 穩定性及機械強度之特性之用途、例如鞋用外底材料。 發泡體之比重可藉由調整調配組成之(c)成分:填充劑 量、以及(d)成分:發泡劑量來控制。 藉由增加(c)成分:填充劑量而比重變大,藉由增加(d) 成分:發泡劑量而可減小比重。 又,本實施形態之發泡體於比重為〇」〜〇 7 §/“時,藉由 型號C測定之硬度為45〜98 ’較佳為48〜90,更佳為5〇〜85。 於比重為0.8〜0.98 g/cc時,藉由型號a測定之硬度為 60〜98 ’較佳為63〜90,更佳為65〜85。 再者,藉由型號c測定之硬度係指使用厚度12 mm之板 狀試驗片,藉由ASKER C型硬度計(型號C)測定之硬度。 又’藉由型號A測定之硬度係指使用厚度12 mm之板狀 試驗片,依據JIS K 6301彈簧式硬度試驗機A形(型號A)測 定之硬度。 上述發泡體之硬度可藉由調整上述成分(a)〜成分、成 分(a')〜成分(d)之組成及比重來控制。 例如’藉由增加成分(c):填充劑之含量而可提高硬度, 藉由增加成分(d):發泡劑量之含量而提高發泡倍率,而可 降低硬度。即’藉由調整上述成分,可將特定比重之發泡 體之強度控制為上述特定之數值。 [發泡體之用途] 本實施形態之發泡體可有效用作:鞋用中底、鞋墊或外 底材料’具體為男士鞋、女士鞋、休間鞋、跑鞋、慢跑 157712.d〇C .30. ⑤ 201213426 鞋、各種競技用鞋、登山鞋、禮服鞋、高爾夫 底U、拖鞋類、沙灘鞋類等所有鞋類之鞋底即中 底、鞋墊或外底材料。 :,本實施形態之發泡體根據需要亦可用於 =零件、建材零件、工業零件、玩具•”零件運 動•健康零件、看護用品等各種成型品,或各種片、膜、 其他工業用品、緩衝材料、包裝材料等。 又,本實施形態之發泡體之尺寸精度優異,耐久性、緩 衝性亦優異,亦可應用於熱成型海綿,加工成該熱成型海 綿後亦可用於上述各種用途。所謂熱成型海绵,係將發泡 體預備切割成所需要之形狀’於加熱至loo〜i5〇〇c之模呈 内加熱㈣,於發泡體之外立面形成牢固的熔融皮膜後:、 將模具冷卻並取出發泡體而製作者。 實施例 以下’列$具體的實施例以及比較例對本發明進行說 明’但本發明並不限定於後述實施例。 (成分(a):嵌段共聚物之製造例) &lt;嵌段共聚物A-l&gt; 使用具備攪拌機之高壓釜,於氮氣環境下,於包含苯乙 烯18質量份之環己烷溶液中,添加正丁基鋰〇 〇91質量 份、以及相對於正丁基裡而添加〇.1倍莫耳之四子基乙一 胺,於70°C下連續供給25分鐘進行聚合。 繼而’將包含苯乙烯21質量份、及1,3_丁二烯32質量份 之環己烷溶液於70。(:下連續供給65分鐘進行聚合。 1577l2.doc •31 - 201213426 繼而,將包含苯乙烯29質量份之環己烷溶液於70°C下連 續供給35分鐘進行聚合。 然後,於聚合器中,相對於正丁基鋰而添加等莫耳之甲 醇,相對於嵌段共聚物100質量份而添加0.3質量份之作為 穩定劑的2-[1-(2_羥基_3,5_二第三戊基苯基)乙基]-4,6-二第 三戊基笨基丙烯酸酯。 然後,進行脫溶劑而獲得嵌段共聚物A-1。 &lt;嵌段共聚物A-2&gt; 使用具備攪拌機之高壓蚤,於氮氣環境下,於包含苯乙 烯24質量份之環己烷溶液中,添加正丁基鋰0.087質量 份、以及相對於正丁基鋰而添加0·1倍莫耳之四曱基乙二 胺,於70°C下連續供給30分鐘進行聚合。 繼而,將包含苯乙烯22質量份、及1,3-丁二烯27質量份 之環己烷溶液於70°C下連續供給60分鐘進行聚合。 繼而,將包含苯乙烯27質量份之環己烷溶液於70°C下連 續供給35分鐘進行聚合。 然後,於聚合器中,相對於正丁基鋰而添加等莫耳之曱 醇,相對於嵌段共聚物100質量份而添加0.3質量份之作為 穩定劑的2-[1-(2-羥基-3,5-二第三戊基苯基)乙基]-4,6-二第 三戊基苯基丙烯酸酯。 然後,進行脫溶劑而獲得嵌段共聚物A-2。 &lt;嵌段共聚物A-3&gt; 使用具備攪拌機之高壓釜,於氮氣環境下,於包含苯乙 烯31質量份之環己烷溶液中,添加正丁基鋰0.082質量 157712.doc -32- ⑧ 201213426 份 胺 以及相對於正丁基鋰而添加〇.丨倍莫耳 於70°c下連續供給40分鐘進行聚合。 之四甲基乙二 繼而,將包含苯乙烯20質量份、盥^ ” 丁二烯2〇質量份 之環己烷溶液於7(TC下連續供給50分鐘進行聚合。 繼而,將包含苯乙烯6質量份與丨3_ d』一烯2質量份之環 己烷溶液於701下連續供給15分鐘進行聚人。 繼而’將包含苯乙烯21質量份之谡p 貝里忉之缞己烷溶液於70°C下連 續供給30分鐘進行聚合。 然後’於聚合器中,相對於正丁基鐘而添加等莫耳之甲 醇,相對於嵌段共聚物100質量份而添加〇·3質量份之 穩定劑= 2.Π_⑽基_3,5二第三戊基苯基)乙基]_4,6_二第 —戍基本基丙稀酸g旨。 然後,進行脫溶劑而獲得嵌段共聚物A &lt;缺段共聚物A-4&gt; 使用具備攪拌機之高壓蒼,於氮氣環境下,於包含苯乙 烯32貝量伤之%己烷溶液中,添加正丁基鋰0.076質量 伤以及相對於正丁基鋰而添加〇.3倍莫耳之四曱基乙二 胺,於70°C下連續供給4〇分鐘進行聚合。 繼而,將包含苯乙烯21質量份與丨,3_丁二稀12質量份之 環己烷溶液於70°C下連續供給40分鐘進行聚合。 繼而,將包含苯乙烯8質量份與丁二烯3質量份之環 己烷溶液於70°C下連續供給15分鐘進行聚合。 繼而,將包含苯乙烯24質量份之環己烷溶液於7〇。〇下連 續供給30分鐘進行聚合。 § 157712.doc •33· 201213426 然後,於聚合器中,相對於正丁基鋰而添加等莫耳之甲 醇,相對於嵌段共聚物100質量份而添加0.3質量份之作為 穩定劑的2-[1-(2-羥基-3,5-二第三戊基苯基)乙基]-4,6-二第 三戊基笨基丙烯酸酯。 然後,進行脫溶劑而獲得嵌段共聚物A-4。 &lt;嵌段共聚物A-5&gt; 使用具備攪拌機之高壓蚤,於氮氣環境下,於包含苯乙 烯26質量份之環己烷溶液中,添加正丁基鋰0·052質量 份、以及相對於正丁基鋰而添加0·3倍莫耳之四甲基乙二 胺,於70°C下連續供給35分鐘進行聚合。 繼而,將包含苯乙烯30質量份與1,3-丁二烯6.5質量份之 環己烷溶液於70°C下連續供給45分鐘進行聚合。 繼而,將包含苯乙烯10質量份與1,3-丁二烯1,5質量份之 環己烷溶液於70°C下連續供給15分鐘進行聚合。 繼而,將包含苯乙烯26質量份之環己烷溶液於70°C下連 續供給30分鐘進行聚合。 然後,於聚合器中,相對於正丁基鋰而添加等莫耳之甲 醇,相對於嵌段共聚物100質量份而添加0.3質量份之作為 穩定劑的2-[1-(2-羥基-3,5-二第三戊基苯基)乙基]-4,6-二第 三戊基苯基丙烯酸酯。 然後,進行脫溶劑而獲得嵌段共聚物A-5。 &lt;嵌段共聚物A-6&gt; 使用具備攪拌機之高壓釜,於氮氣環境下,於包含苯乙 烯15質量份之環己烷溶液中,添加正丁基鋰0.092質量 157712.doc -34- ⑧ 201213426 伤以及相對於正丁基鋰而添加0.1倍莫耳之四子基乙二 胺,於7〇t:下連續供給20分鐘進行聚合。 繼而,將包含苯乙稀16質量份與仏丁二婦38質量份之 環己烷溶液於7(TC下連續供給6〇分鐘進行聚合。 繼而,將包含苯乙稀6質量份與1}3_丁二婦2質量份之環 己烷溶液於7(TC下連續供給15分鐘進行聚合。 繼而’將包含苯乙烯23質量份之環己烷溶液於7〇(&gt;c下連 續供給3 0分鐘進行聚合。 然後,於聚合H中,㈣於正τ基㈣添加等莫耳之甲 醇’相對於嵌段共聚物100質量份而添加03質量份之作為 穩定劑的2-[Η2-經基_3,5_二第三戊基笨基)乙基]_4,6_二第 三戊基苯基丙浠酸醋。 然後,進行脫溶劑而獲得嵌段共聚物Α_6。 &lt;嵌段共聚物Α-7&gt; 使用具備麟機之高麼爸,於氮氣環境下,於包含苯乙 烯39質量份之環己烷溶液中,&amp;加正了基鋰㈣質量 份、以及相對於正丁基鋰而添加〇3倍莫耳之四甲基乙二 胺,於7〇C下連續供給45分鐘進行聚合。 繼而,將包含苯乙烯20質量份與丨,3_丁二烯2質量份之環 己烧/谷液於70C下連續供給30分鐘進行聚合。 繼而,將包含苯乙烯39質量份之環己烷溶液於7〇χ:下連 續供給45分鐘進行聚合。 然後,於聚合器中,相對於正丁基鋰而添加等莫耳之甲 醇,相對於嵌段共聚物1 〇〇質量份而添加〇 3質量份之作為 157712.doc -35· 201213426 穩定劑的2-[l-(2-羥基-3,5-二第三戊基苯基)乙基]-4,6-二第 三戊基苯基丙烯酸酯。 然後,進行脫溶劑而獲得嵌段共聚物A-7。 &lt;嵌段共聚物A-8&gt; 使用具備攪拌機之高壓釜,於氮氣環境下,於包含苯乙 烯20質量份之環己烷溶液中,添加正丁基鋰0.090質量 份、以及相對於正丁基鋰而添加0.1倍莫耳之四曱基乙二 胺,於70°C下連續供給25分鐘進行聚合。 繼而,將包含苯乙烯16質量份與1,3-丁二烯32質量份之 環己烷溶液於7〇°C下連續供給55分鐘進行聚合。 繼而,將包含苯乙烯8質量份與1,3-丁二烯2質量份之環 己烷溶液於70°C下連續供給15分鐘進行聚合。 繼而,將包含苯乙烯22質量份之環己烷溶液於70°C下連 續供給30分鐘進行聚合。 然後,於聚合器中,相對於正丁基鋰而添加等莫耳之甲 醇,相對於嵌段共聚物100質量份而添加0.3質量份之作為 穩定劑的2-[1-(2-羥基-3,5-二第三戊基苯基)乙基]-4,6-二第 三戊基苯基丙烯酸酯。 然後,進行脫溶劑而獲得嵌段共聚物A-8。 &lt;嵌段共聚物A-9&gt; 使用具備攪拌機之高壓釜,於氮氣環境下,於包含苯乙 烯15質量份之環己烷溶液中,添加正丁基鋰0.074質量 份、以及相對於正丁基鋰而添加0.3倍莫耳之四曱基乙二 胺,於70°C下連續供給20分鐘進行聚合。 157712.doc -36- 201213426 繼而’將包含1,3-丁二烯10質量份之環己烷溶液於抓 下連續供給20分鐘進行聚合。 繼而,將包含苯乙婦57質量份與以.丁二婦18質量份之 環己烷溶液於7(TC下連續供給8〇分鐘進行聚合。 然後,於聚合器中’相對於正丁基鍾而添加等莫耳之甲 醇’相對於嵌段共聚物100質量份而添加〇3質量份之作為 穩定劑的2-[1-(2-經基_3,5_二第三戊基苯基)乙基]_4,6_二第 三戊基苯基丙稀酸醋。 然後,進行脫溶劑而獲得嵌段共聚物A_9。 〈嵌段共聚物A-l〇&gt; 使用具備㈣機之高壓爸,於氮氣環境下,於包含苯乙 烯47質量份之環己燒溶液中,添加正丁基㈣州質量 份、以及相對於正丁基鋰而添加〇3倍莫耳之四甲基乙二 胺,於70°C下連續供給55分鐘進行聚合。 繼而’將包含1,3-丁二烯6質量份之環己烧溶液於賊下 連續供給I5分鐘進行聚合。 繼而將包3苯乙婦47質量份之環己烧溶液於川^下連 續供給5 5分鐘進行聚合。 然後’於聚合器中,相對於正丁基鋰而添加等莫耳之甲 醇相對於嵌段共聚物1〇〇質量份而添加〇·3質量份之作為 穩定劑的2-Π♦經基_3,5•二第三戊基苯基)乙基]_4,6_二第 二戍基苯基丙婦酸g旨。 然後,進行脫溶劑而獲得嵌段共聚物Α_ι〇。 &lt;嵌段共聚物A-ll&gt; 157712.doc -37- 201213426 使用具備攪拌機之高壓釜,於氮氣環境下, ㈣量份之環己貌溶液中,添加正丁基二:量乙 份、以及相對於正丁基鋰而添加0.3倍莫耳之四ρ基乙二 胺’於70°C下連續供給30分鐘進行聚合。 繼而,將包含苯乙烯10質量份與153_ 丁二烯26質量份之 環己烷溶液於70°C下連續供給45分鐘進行聚合。 繼而,將包含苯乙烯12質量份與^· 丁二烯3質量份之環 己烷溶液於70°C下連續供給20分鐘進行聚合。 繼而,將包含苯乙烯22質量份之環己烷溶液於7(Γ(:下連 續供給25分鐘進行聚合。 然後,於聚合器中,相對於正丁基鋰而添加等莫耳之甲 醇,相對於敢段共聚物1〇〇質量份而添加0.3質量份之作為 穩定劑的2-[1-(2-羥基-3,5-二第三戊基苯基)乙基]_4,6二第 三戊基苯基丙稀酸醋。 然後’進行脫溶劑而獲得嵌段共聚物A_丨j。 將成分(a) ’肷段共聚物a- 1〜a- 11之結構、苯乙烯含量 (負夏%)、30 C之儲存彈性模數(E,)、及動態黏彈性測定之 函數tan5之峰值溫度、嵌段共聚物所含有之苯乙烯之嵌段 率分別示於下述表1。 (成分(a):嵌段共聚物之物性之測定方法) &lt;(1)苯乙烯含量(質量。/〇)&gt; 使用紫外線分光光度計(日立UV200),根據262 nm之吸 收強度算出。 &lt;(2) 30°C之儲存彈性模數(Ει)及動態黏彈性測定之函數 157712.doc ⑧ •38- 201213426 tan5之峰值溫度&gt; 使用Rheology (股)製造之黏彈性測定解析裝置DVE-V4, 於振盪頻率35 Hz、升溫速度/min之條件下,使用厚度 2 mm之試驗片,測定溫度-50°C〜150°C之範圍而求得。 &lt;(3)嵌段共聚物所含有之苯乙烯之嵌段率&gt; 應用將四氧化锇作為觸媒藉由過氧化第三丁醇將嵌段共 聚物氧化分解之方法(氧化分解法:I. M. KOLTHOFF,et al·,J. Polym. Sci. 1,429 (1946)所記載之方法),將苯乙烯 之嵌段鏈成分(其中平均聚合度為約30以下之苯乙烯嵌段 成分除外)分離,測定該苯乙烯嵌段鏈之重量,根據下述 式而求得。 苯乙烯之嵌段率(質量%)=(嵌段共聚物中之苯乙烯嵌段 聚合鏈之重量/嵌段共聚物中之苯乙烯之總重量)x 100 157712.doc 39- 5 201213426Sol 130, Kyoseki Process X50, X100, X140 manufactured by Nippon Mining & Co., Ltd. 'Rezox Νο·3, Dutorex 729UK, manufactured by Shell Chemicals, Koumorex 200, 300, 500, 700 manufactured by Nippon Oil Corporation, manufactured by Exxon Mobil Esso Process Oil 110, Esso Process Oil 120, Mitsubishi 34 Heavy Process Oil, Mitsubishi 44 Heavy Process Oil, Mitsubishi 38 Heavy Process Oil, Mitsubishi 39 Heavy Process Oil, etc. manufactured by Nippon Oil Corporation. The compounding amount of the plasticizer is preferably from 1 to 200 parts by mass, more preferably from 10 to 100 parts by mass, even more preferably from 15 to 8 parts by mass, per 100 parts by mass of the component (b). When the amount of the plasticizer is from 1 to 200 parts by mass, the foam of the present embodiment is excellent in workability. As the component (b), polybutadiene is preferred, and as the polybutadiene rubber, the inclusion of the 1,2-bond (vinyl) 5% to 20%, and the inverse 1,4 bond 0~ 3%, the rest of the ingredients are Shun, 4 bonds of vinyl cis-polybutadiene rubber ' or more than 92% of cis 1,4 bonds, including ι, 2 bonds 〇%~3%, the remaining components are anti-1,4 High-poly butadiene rubber of the rubber of the key. In the foam of the first embodiment of the present embodiment, the mass ratio of the component to the component (b) (component (a) / component 〜 3 〇) / (7 〇 to 99) is preferably (2~). 25) / (75 ~ 98), more preferably (5 ~ 20) / (80 ~ 95). When the mass ratio of the component (a) to the component (b) is (1 to 30) / (70 - 99), the foam can obtain excellent hardness and dimensional stability. (Ingredient (c): Filler) 157712.doc -19- 201213426 : For the filler 'For example, it can be exemplified by dioxic carbonate, clay, strontium, sulphuric acid, broken acid town, glass woven, glass beads, and acid. Unloading carbon black, stone anaerobic dioxide, dual phase filler, etc. In the foam of the first embodiment, the blending amount of the filler in the foam is 1 to 100 parts by mass based on the total amount of (a) and the component (b). Preferably, it is 2 to 90 parts by mass, more preferably 3 7 曰, 尺佳马 3 75 份份份, and particularly preferably 5 to 50 parts by mass. 0, if the component (4): the amount of the filler is Η. . In the case of parts by mass, the foam of this embodiment can obtain a preferable hardness and a preferable specific gravity. (Component (d): foaming agent) As the foaming agent, for example, an inorganic foaming agent or an organic foaming agent known per se can be used. For example, sodium bicarbonate, bicarbonate to anti-failure, sodium citrate, ammonium carbonate, azo-nitramine, diazepam. 3⁄4. X nm brothers, quinones, quinones, tetraamines, two The nitro group is a stupid amine, azobisisobutyronitrile, azodicarboxylic acid, and the like. More preferably, it is azo dimethylamine, dinitrosium pentylene = stilbene, sulfonium, sodium bicarbonate. These blowing agents may be known as a foaming aid such as a derivative. Further, as the foaming agent', a heat-expandable microcapsule can be used. The heat-expandable microcapsules include a shell of thermoplastic hollow spheres and a shell containing a thermoplastic resin enclosing the gas. When the heat-expandable microcapsules are heated, the thermoplastic shell is filled, and the gas increases the pressure. As a result, the sphere expands to function as a foaming agent as a thermoplastic resin constituting the shell of the microcapsule, for example, List: 157712.doc •20- 201213426 Vinylidene chloride-acrylonitrile copolymer, vinylidene chloride_methyl methacrylate total compound, partial chloroethene _ sub-based propyl ethyl benzoate B Dilute nitrile-methyl propyl methyl acrylate copolymer, acrylonitrile-f-based ethyl acrylate, and the like. Further, examples of the compound which becomes a gas by heating include isopentane, isobutane, isopropane and the like. The mass average particle diameter of the heat-expandable microcapsules is usually from 0 to 00 pm, preferably from about 20 to 80 μηι. Examples of the heat-expandable microcapsules include expancel DU manufactured by JApAN fillite Co., Ltd., wu system 歹J, Microsphere F-30, F-50, F-80S, F-85 manufactured by Matsumoto Oil & Fats Co., Ltd., and the like. When the heat-expandable microcapsules are used as a foaming agent, by heating, the gas-forming components contained in the respective microcapsules are gasified to be uniformly swollen, and a homogeneous foam can be obtained. The endothermic foaming agent is preferred for foaming. The dimethyl hydrazine dimer nitro pentoxide can be used as a heat-generating foaming agent by suppressing heat generation during foam molding by using a heat-generating foaming agent and agent, and azomethylenetetramine is exemplified. Wait. Further, as the endothermic foaming agent, it is possible to list sodium citrate or the like, and in this case, the generated gas is carbon dioxide. In the foam of the first embodiment, the amount of the component knives (d) and the foaming agent is preferably 0.1 to 30 parts by mass, based on the weight of the components (4) and (8). It is preferably 5 to 2 parts by weight, more preferably 1 to 15 parts by mass. If the component (d): the amount of the foaming agent is from 1, part by mass, the present embodiment is 157712.doc.21·201213426 The foam has excellent hardness and a specific gravity is obtained. (Component (e): Thermoplastic Elastomer and/or Thermoplastic Resin) The foam of the present embodiment may further contain the component (e): a thermoplastic elastomer and/or in addition to the above components (a) to (d). Thermoplastic resin. As the thermoplastic elastomer, for example, according to the classification of the chemical composition of the hard segment, a thin-smoke thermoplastic elastomer (TPO), a urethane-based thermoplastic elastomer (TPU), or an ester-based thermoplastic elastomer ( TpEE), a styrene-based thermoplastic elastomer (TPAE), and the like. In addition, a gas-based thermoplastic elastomer (Tpvc) or an ion cluster-type thermoplastic elastomer (ionomer) contains a fluororesin as a fluorine-based thermoplastic elastomer as a restraining block (again, it may be used by In the thermoplastic elastomer in which the resin/rubber is mixed, the rubber which is a soft segment is cross-linked while being kneaded, and the rubber dispersed particle diameter is refined, and the dynamically crosslinked TPO which improves the performance is called TPV). The above thermoplastic elastomer can be used alone! Two or more kinds may be used in combination. Further, as the other thermoplastic elastomer, a synthetic rubber other than the above component (a) or component (b) may be used, and examples thereof include a fluororubber and a polyoxyethylene rubber 'South 2 butyl rubber (for example, chlorobutyl rubber, bromine The butyl rubber or the like may be used alone or in combination of two or more. The thermoplastic resin is not particularly limited as long as it is a thermoplastic resin having a plasticizing temperature of 5 Torr to 3 Torr (for example, a styrene resin (for example, polystyrene, acrylonitrile, styrene copolymer). 'Acrylonitrile-butadiene-styrene copolymer, ABS (AcryI〇nitrile Butadiene Styrene, acrylonitrile_丁二妇乙乙 I57712.doc •22- 201213426) resin, AES (Acrylonitrile-Ethylene-Styrene) , propylene guess, ethylene-epoxy resin, AAS (Acrylnitrile-Acrylicester-Styrene, acrylonitrile acrylate) resin, polyethylene, polypropylene, ethylene, propylene resin, ethylene-ethyl acrylate resin, poly Vinyl chloride, polyvinylidene gas, polybutene, polycarbonate, polyacetal, polyphenylene ether, polymethyl methacrylate, saturated polyester resin (for example, hydroxycarboxylic acid condensate such as polylactic acid, poly a condensate of a diol such as butyl succinate and a dicarboxylic acid, or the like, a polyamide resin, a fluororesin, a polysulfone, a polyether sulfone, a polyarylate, a polyetheretherketone liquid crystal polymer, or the like. One can be used alone, or Two or more kinds are used. Among the thermoplastic resins, polystyrene, acrylonitrile, styrene copolymer, ABS resin, AES resin, AAS resin, polyethylene, polypropylene, polyethylene oxide, saturated polyester resin, poly The phthalamide resin is preferably formed by preventing the dent or deformation in the molded body of the foam of the present embodiment by blending the thermoplastic resins. As for the component (e): thermoplastic elastomer and/or thermoplastic The blending amount of the resin is preferably 1 to 1 part by mass, more preferably 3 to 75 parts by mass, more preferably 5 to 75 parts by mass, based on 1 part by mass of the total of the component (a) and the component (b). 5 parts by mass. If the component (e): the thermoplastic elastomer and/or the thermoplastic resin is blended in an amount of from 1 to 100 parts by mass, the foam of the present embodiment can obtain a preferable mechanical strength. The foam composition for obtaining the foam of the first embodiment of the present embodiment comprises the above components (a) to (d), and the component (a) block is 157712.doc - 23· 201213426 Polymer and the above (b) different &amp; two association rubber and / or: the quality of rare rubber The ratio (former (a) / component (b)) is (1 to 3 〇) / (7 〇 to 99), preferably (2 to 25) / (75 to 98), more preferably (5~) 20) / (80 to 95), the above (c) is contained in the total amount (10) by mass of the above (a) block copolymer and the above (b) isoprene-based rubber and/or diene rubber. The filler is 1 to 100 parts by mass, preferably 2 to 9 parts by mass, more preferably 3 to 75 parts by mass, particularly preferably 5 to 5 parts by mass, and contains the above (sentence foaming d 0.1 to 30 mass parts) Preferably, it is 5 to 2 parts by mass, more preferably 丨 to parts by mass. Further, the component (e)' may be preferably contained in an amount of 100 parts by mass based on the α of the component (a) and the component (1?), and further contains 3 parts by mass, more preferably 3 to 75 parts by mass. Good for 5 to 50 parts by mass. When preparing a composition for a foam, a conventionally known kneader, extruder, or the like can be used. In addition, as a method of blending (c) a filler, (d) a foaming agent, and the like, for example, the component (a) and the component 〇3) are 100 to 180 in advance by a Banbury mixer or the like. After the mixture is kneaded by kneading, the obtained product is blended with a filler (C) using a Banbury mixer or the like, and then a method of adding (d) a foaming agent, a crosslinking agent or the like using a roll or the like is used, but the invention is not limited thereto. [Foam] [Foam according to the second embodiment] The foam of the second embodiment contains the following components (a,) to (sentence. (a1) block copolymer which contains at least 2 ethylene. a base aromatic hydrocarbon polymer block, and at least one copolymer block comprising a conjugated diene and a vinyl aromatic hydrocarbon, and the content of the '157712.doc -24-201213426 ethylene-based aromatic hydrocarbon is 65~ The mass of 95 is 5 to 35 mass%, and the mass of the block copolymer containing a total of diene is contained in the B-county (4) 40 to 98% by mass. The job is only (b) isoprene Rubber and/or diene rubber (c) Filler (d) Foaming agent. The foam of the second embodiment has a specific gravity of 〇1 n ^ 〇*7 g/cc. The hardness of the test is 45~98, and the hardness is 〇8~〇^. The hardness of the model 8 is 6〇~98. 'gee' is wrong (component (a'): block copolymer) composition (a' A block copolymer containing an ethylene-based aromatic (IV) as described above. The content of the ethylene-based aromatic hydrocarbon in the octa-ene component (8) is ~~95 mass. 4 is preferably 68 to 93% by mass. More preferably 70~90 The content of the conjugated diene in the component (a,) is, in the range of 7 to 32 mass%, more preferably 10 to 30 mass%. Preferably, if the vinyl aromatic hydrocarbon When the content is in the range of from 5 to 35% by mass in the range of from 65 to 95, the balance between the hardness of the foam and the thermoformability of the foam is excellent, and the vinyl is suitable for the elongation component (4) of the shoe. Aromatic hydrocarbon content, w inclusions. The amount is determined by measuring the absorbance of the light by using an ultraviolet spectrophotometer. Searching for the wavelength The component ratio of the Ethylene-based aromatic smoke polymer contained in the component (8) is 5 157712.doc -25- 201213426 4 0~98% by mass, preferably. If the mother-in-law is intended. More preferably 6〇~90% by mass. The base ratio of the base of the tobacco polymer is 4, which is a foam with a stable size and a heat (4). The block ratio of i σ as a vinyl aromatic hydrocarbon polymer for shoes can be determined by the weight of the random copolymer chain of the aromatic cigarette and the common light bismuth in the component (8) and the content of the vinyl scented hydrocarbon. (% by mass) to adjust. The component (the amount of the ethylene-based aromatic hydrocarbons occupied by the random copolymer chain of the A-pure copolymer is decreased as the block ratio of the vinyl aromatic hydrocarbon polymer is decreased, and the block rate is increased as the ratio is decreased. The block ratio of the aromatic hydrocarbon polymer of the county can be determined by the same method as the above component (4). The formed blade (a) has at least two vinyl aromatic hydrocarbon polymer blocks' and at least one contains a total of A copolymer of diterpene and anthracene-based aromatic hydrocarbon. The polymer structure of the component 〇') is not particularly limited, and for example, a linear block copolymer or a radial block represented by the following formula may be used. a copolymer, or any mixture of such polymer structures. Further, in the radial block copolymer represented by the following formula, further than at least one block VIII or block 3 may be bonded to X. (AB)n+1, A-(BA)n, B-(AB)n+丨, [(AB)k]m+1-X &gt; [(AB)kA]m+,-X &gt; [(BA k]m+1-X, [(BA)kB]m+1-X, in the above various formulas, 'block A is composed of a vinyl aromatic hydrocarbon polymer, and Xin B and B are composed of a total of two women. It is composed of a copolymer of an aromatic hydrocarbon. 157712.doc -26- 5 201213426 'x" in the above formula, for example, represents tetrachloride, tin tetrachloride, u bis (N'N-glycidylaminomethyl) cyclohexan, epoxidized soybean oil, etc. The residue of the coupling agent or the residue of the polyfunctional compound. n, k & m are integers of 1 or more, and are usually integers of 5 . Further, the structure of the plurality of bonded polymer chains may be the same or different. The above-mentioned component (a,) contained in the foam: the vinyl aromatic smoke in the copolymer of the vinyl aromatic hydrocarbon and the conjugated diene in the block B of the block copolymer may be uniformly distributed, or Formed (decreasing) distribution. Further, in the copolymer, a portion of a plurality of vinyl aromatic smoke homogenous sentence distributions and/or a wedge-shaped distribution portion may be coexisted in the block. The knives (a). 肷 & copolymer preferably contain at least (10) random copolymers of the age of 'the content of the ethyl succinyl aromatic fumes is 7 〇 mass%, not more than 10% by mass, preferably 75 A vinyl aromatic hydrocarbon having a mass% or more and 98% by mass or less is co-boiled. Thereby, a foam having good hardness and dimensional stability can be obtained. &lt;Component (a) Method for producing a segment copolymer> The component (a') can be produced by the same method as the above component (4). The ethylene-based hydrocarbon, silk:ene, hydrocarbon solvent, and polymerization starting material which are raw materials may be the same as the component (4). Further, the polymerization conditions such as the polymerization temperature and the ambient gas may be selected under the same conditions as the component (a). &lt;Component (a). Physical properties of the block copolymer > The knives (a) inlaid copolymer is preferably 3 Å in the dynamic viscoelasticity measurement. The elastic modulus of elasticity under the armpit (10) is 3xl 〇 8 pa or more and 2.35 χΐ〇 9 or less, and 157712.doc -27- 201213426 is preferably the dynamic viscoelasticity measurement. The peak temperature is at least 1 below 150C. One. More preferably, the dynamic viscoelastic wave is set to φ ^ η. The storage elastic modulus (Ε,) at 30 C in Guangli 为 is 5xl08 Pa or more and 2.33x1 〇 9 Pa or less, B s „ upper 乂 and better as a function of dynamic viscoelasticity measurement. The peak temperature of tan5 is 9 ( There is at least ι above U5t in rc. The 'foaming body is excellent in the balance between hardness and elongation and thermoformability'. It is suitable for the sole. The molecular weight of the component (a,) is not particularly limited. The polystyrene-equivalent number average molecular weight in the gel permeation chromatography (GPC method) is preferably 30.000 1, 〇〇〇, 〇〇〇 ' more preferably 4 〇, 〇〇〇 〜 5 〇〇〇〇〇 In particular, the composition for a foam having excellent fluidity and workability can be obtained by setting the molecular weight of the component (a') to the above range in the range of 5 Å to 300.000 Å. In the foam of the second embodiment, the foam of the second embodiment can be used as the component (b), the component (c), and the material (d). The component (e) may be contained. [Method for Producing Foam] First Embodiment of the Present Embodiment In the foaming system, the component (a), the component (b), the component (c), and the component (d) are essential components, and the foaming system of the second embodiment has the component (a), the component (b), and the component. (c) and (d) as an essential component, each component (e) is added as needed to prepare a composition for a foaming body', and the foaming composition is subjected to a foaming/crosslinking treatment to obtain 157,712. Doc -28-201213426. (Foaming and cross-linking treatment) In the step of the above-mentioned composition for foams, liuzan/a, a foam can be obtained by adding a mold to the (four) mold. After foaming by raising the temperature, or molding into an arbitrary shape using an extrusion molding machine, it is heated in a heating tank to foam. At this time, the foaming is performed once after foaming, and the foaming may be performed twice. The foaming condition is preferably increased. The heating temperature is preferably set to ΐ2〇~3() (η:, more preferably in the range of 140-200 C, preferably the heating time is set to 3 minutes, more preferably It is set to a range of 5 to 60 minutes. In the above foaming process, crosslinking can be carried out at the same time. The cross-linking form of the foam is not particularly limited, and for example, sulfur cross-linking, peroxide cross-linking, etc. may be applied. From the viewpoint of cost and strength of the foam, sulfur cross-linking is preferred. The body may be appropriately formulated with an appropriate amount of alkane alkylating agent, an anthracene coupling agent, an anti-aging agent, a vulcanization accelerator, and a crosslinking auxiliary agent. [The physical properties of the foam] The proportion of the foam of the embodiment is in the i-th In the foam of the embodiment and the second embodiment, 0.1 to 0.98 g/cc' is preferably 〇% g/cc. The specific gravity can be measured by the method described in the examples below. Measured in JIS K 7 112. The foam having a specific gravity of 0·b 0.7 g/cc is suitable for use in applications requiring cushioning properties such as cushioning properties, cushioning properties, and light weight, such as midsole materials such as sports shoes. § 157712.doc -29- 201213426 Foams with a specific gravity of 0·8 to 0.98 g/cc are suitable for applications requiring characteristics of hardness, dimensional stability and mechanical strength, such as outsole materials for shoes. The specific gravity of the foam can be controlled by adjusting the composition of the compound (c): the amount of the filler, and the component (d): the amount of foaming. By increasing the component (c): the filling dose and the specific gravity becomes large, the specific gravity can be reduced by increasing the component (d): the foaming amount. Further, in the foam of the present embodiment, when the specific gravity is 〇"~〇7 §/", the hardness measured by the model C is 45 to 98', preferably 48 to 90, more preferably 5 to 85. When the specific gravity is 0.8 to 0.98 g/cc, the hardness measured by the model a is 60 to 98', preferably 63 to 90, more preferably 65 to 85. Further, the hardness measured by the model c means the thickness used. 12 mm test piece, hardness measured by ASKER C type hardness tester (model C). 'Density measured by type A means a plate test piece with a thickness of 12 mm, according to JIS K 6301 spring type The hardness measured by the hardness tester A-shape (model A). The hardness of the above-mentioned foam can be controlled by adjusting the composition and specific gravity of the above components (a) to components, components (a') to (d). By increasing the content of the component (c): the filler, the hardness can be increased, and the foaming ratio can be increased by increasing the content of the component (d): the amount of the foaming agent, and the hardness can be lowered. That is, by adjusting the above components, The strength of the foam having a specific specific gravity is controlled to the above specific numerical value. [Use of Foam] This embodiment The foam can be effectively used as: midsole, insole or outsole material for shoes. Specifically, men's shoes, ladies' shoes, rest shoes, running shoes, jogging 157712.d〇C.30. 5 201213426 shoes, various athletic shoes, The soles of the footwear, the dress shoes, the golf sole U, the slippers, the beach shoes, etc. are the midsole, the insole or the outsole material. The foam of the embodiment can also be used for the parts, building materials as needed. Parts, industrial parts, toys, "parts sports, health parts, care products, and other molded products, or various sheets, films, other industrial supplies, cushioning materials, packaging materials, etc. Further, the foam of the present embodiment is excellent in dimensional accuracy, excellent in durability and cushioning property, and can be applied to a thermoformed sponge, and can be used for the above various applications after being processed into the thermoformed sponge. The so-called thermoformed sponge is prepared by cutting the foam into a desired shape and heating it in a mold heated to loo~i5〇〇c (4), after forming a firm molten film on the outer surface of the foam: The mold is cooled and the foam is taken out and produced. EXAMPLES Hereinafter, the present invention will be described with reference to specific examples and comparative examples, but the present invention is not limited to the examples described below. (Component (a): Production Example of Block Copolymer) &lt;Block Copolymer A-1&gt; Using an autoclave equipped with a stirrer, in a cyclohexane solution containing 18 parts by mass of styrene under a nitrogen atmosphere, 91 parts by mass of n-butyllithium ruthenium was added, and 四.1 mol of tetrakis-ethylideneamine was added to n-butyl group, and the mixture was continuously supplied at 70 ° C for 25 minutes to carry out polymerization. Then, a solution containing 21 parts by mass of styrene and 32 parts by mass of 1,3-butadiene was used at 70. (: Polymerization was carried out continuously for 65 minutes. 1577l2.doc • 31 - 201213426 Then, a cyclohexane solution containing 29 parts by mass of styrene was continuously supplied at 70 ° C for 35 minutes for polymerization. Then, in the polymerization vessel, Adding a molar amount of methanol to n-butyllithium, and adding 0.3 parts by mass of 2-[1-(2_hydroxy_3,5_2, third) as a stabilizer with respect to 100 parts by mass of the block copolymer Butyl phenyl)ethyl]-4,6-di-p-pentyl phenyl acrylate. Then, solvent removal was carried out to obtain block copolymer A-1. &lt;Block copolymer A-2&gt; The high pressure enthalpy of the stirrer was added to 0.087 parts by mass of n-butyllithium in a cyclohexane solution containing 24 parts by mass of styrene under nitrogen atmosphere, and 0.4 times of moles of moles of n-butyllithium was added. The mercaptoethylenediamine was continuously supplied at 70 ° C for 30 minutes to carry out polymerization. Then, a cyclohexane solution containing 22 parts by mass of styrene and 27 parts by mass of 1,3-butadiene was continuously dried at 70 ° C. The polymerization was carried out for 60 minutes. Then, a cyclohexane solution containing 27 parts by mass of styrene was continuously supplied at 35 ° C for 35 minutes. Then, in the polymerizer, isomolar sterol is added to n-butyllithium, and 0.3 parts by mass of 2-[1-(s) as a stabilizer is added to 100 parts by mass of the block copolymer. 2-Hydroxy-3,5-di-t-pentylphenyl)ethyl]-4,6-di-p-pentyl phenyl acrylate. Then, solvent removal was carried out to obtain block copolymer A-2. Block copolymer A-3&gt; Using an autoclave equipped with a stirrer, under a nitrogen atmosphere, in a cyclohexane solution containing 31 parts by mass of styrene, n-butyllithium 0.082 mass 157712.doc -32- 8 201213426 was added. The amine and the butyl oxime are continuously supplied for 40 minutes at 70 ° C for polymerization with respect to n-butyllithium. The tetramethylethylene 2 will then contain 20 parts by mass of styrene, 盥 ^ ” 2 parts by mass of a cyclohexane solution was continuously supplied at 7 (TC) for polymerization for 50 minutes. Then, a cyclohexane solution containing 6 parts by mass of styrene and 2 parts by mass of 丨3_d'-ene was continuously dried at 701. Supply for 15 minutes for concentration. Then '21 parts by mass of styrene containing styrene, lysine and hexane solution at 70 ° C The polymerization was continued for 30 minutes, and then, in the polymerization reactor, isomolar methanol was added to the n-butyl group, and 3 parts by mass of the stabilizer was added to 100 parts by mass of the block copolymer. Π_(10)yl_3,5-di-di-pentylphenyl)ethyl]- 4,6-di-di-p-based acrylic acid g. Then, solvent removal is carried out to obtain block copolymer A &lt;A-4&gt; Using a high pressure condensate equipped with a stirrer, a 0.076 mass loss of n-butyllithium and a ruthenium addition to n-butyllithium were added to a hexane solution containing 32 Å of styrene in a nitrogen atmosphere. .3 times mole of tetradecylethylenediamine was continuously supplied at 70 ° C for 4 minutes to carry out polymerization. Then, a cyclohexane solution containing 21 parts by mass of styrene and 12 parts by mass of hydrazine and 3-butane dilute was continuously supplied at 70 ° C for 40 minutes to carry out polymerization. Then, a cyclohexane solution containing 8 parts by mass of styrene and 3 parts by mass of butadiene was continuously supplied at 70 ° C for 15 minutes to carry out polymerization. Then, 24 parts by mass of a styrene solution containing styrene was placed at 7 Torr. The mixture was continuously supplied for 30 minutes for polymerization. § 157712.doc •33·201213426 Then, in a polymerizer, isomolar methanol is added to n-butyllithium, and 0.3 parts by mass of a stabilizer 2 is added to 100 parts by mass of the block copolymer. [1-(2-Hydroxy-3,5-di-t-pentylphenyl)ethyl]-4,6-di-p-pentyl phenyl acrylate. Then, solvent removal was carried out to obtain block copolymer A-4. &lt;Block Copolymer A-5&gt; Using a high pressure crucible equipped with a stirrer, 0.052 parts by mass of n-butyllithium was added to a cyclohexane solution containing 26 parts by mass of styrene under a nitrogen atmosphere, and To the n-butyllithium, 0.4 M mole of tetramethylethylenediamine was added, and the mixture was continuously supplied at 70 ° C for 35 minutes for polymerization. Then, a cyclohexane solution containing 30 parts by mass of styrene and 6.5 parts by mass of 1,3-butadiene was continuously supplied at 70 ° C for 45 minutes to carry out polymerization. Then, a cyclohexane solution containing 10 parts by mass of styrene and 1,5 parts by mass of 1,3-butadiene was continuously supplied at 70 ° C for 15 minutes to carry out polymerization. Then, a cyclohexane solution containing 26 parts by mass of styrene was continuously supplied at 70 ° C for 30 minutes to carry out polymerization. Then, in the polymerization vessel, isomolar methanol was added to n-butyllithium, and 0.3 parts by mass of 2-[1-(2-hydroxy-) as a stabilizer was added to 100 parts by mass of the block copolymer. 3,5-Di-t-pentylphenyl)ethyl]-4,6-di-p-pentyl phenyl acrylate. Then, solvent removal was carried out to obtain block copolymer A-5. &lt;Block copolymer A-6&gt; Using an autoclave equipped with a stirrer, n-butyllithium 0.092 mass 157712.doc -34-8 was added to a cyclohexane solution containing 15 parts by mass of styrene under a nitrogen atmosphere. 201213426 Injury and addition of 0.1 times mole of tetrakis-ethylenediamine to n-butyllithium, and continuous polymerization for 20 minutes at 7 〇t: for polymerization. Then, a cyclohexane solution containing 16 parts by mass of styrene and 38 parts by mass of butyl bismuth was continuously supplied at 7 (TC) for polymerization for 6 minutes. Then, 6 parts by mass of styrene and 1}3 were contained. 2 parts by mass of a cyclohexane solution was continuously supplied at 7 (TC for 15 minutes for polymerization. Then, a solution containing 23 parts by mass of styrene in cyclohexane was continuously supplied at 7 Torr (&gt;c). Then, in the polymerization H, (4) adding a molar amount of methanol to the positive τ group (tetra), and adding 03 parts by mass of the 2-[Η2-perylene group as a stabilizer with respect to 100 parts by mass of the block copolymer. _3,5_2,3,3,5-pentyl)ethyl]_4,6-di-p-pentyl phenylpropanate vinegar. Then, solvent removal is carried out to obtain a block copolymer Α_6. &lt;block copolymerization Α-7&gt; Using a high-powered dad with a machine, in a nitrogen atmosphere, in a cyclohexane solution containing 39 parts by mass of styrene, &amp; plus (4) parts by mass, and relative to n-butyl group Lithium was added with 3 times moles of tetramethylethylenediamine, and the mixture was continuously supplied at 7 ° C for 45 minutes for polymerization. Then, 20 parts by mass of styrene was contained. 2 parts of butadiene, 2 parts by mass of cyclohexane calcined / gluten solution was continuously supplied for 30 minutes at 70 C for polymerization. Then, a cyclohexane solution containing 39 parts by mass of styrene was continuously supplied for 45 minutes at 7 Torr: Then, in the polymerization reactor, isomolar methanol is added to n-butyllithium, and 3 parts by mass of ruthenium is added to 1 part by mass of the block copolymer as 157712.doc -35·201213426 Stabilizer 2-[l-(2-hydroxy-3,5-di-p-pentylphenyl)ethyl]-4,6-di-p-pentyl phenyl acrylate. Block copolymer A-7. &lt;Block copolymer A-8&gt; Using an autoclave equipped with a stirrer, n-butyllithium 0.090 was added to a cyclohexane solution containing 20 parts by mass of styrene under a nitrogen atmosphere. The mass fraction and the tetramethylethylenediamine added with 0.1 times mole of n-butyllithium were continuously supplied at 70 ° C for 25 minutes for polymerization. Then, 16 parts by mass of styrene and 1,3- were contained. 32 parts by mass of butadiene solution of butadiene was continuously supplied at 55 ° C for 55 minutes for polymerization. Then, styrene 8 was contained. The mixture was continuously supplied with a cyclohexane solution of 2 parts by mass of 1,3-butadiene at 70 ° C for 15 minutes. Then, a cyclohexane solution containing 22 parts by mass of styrene was continuously supplied at 70 ° C. The polymerization was carried out for 30 minutes. Then, in the polymerization apparatus, isomolar methanol was added to n-butyllithium, and 0.3 parts by mass of 2-[1- as a stabilizer was added to 100 parts by mass of the block copolymer. (2-Hydroxy-3,5-di-p-pentylphenyl)ethyl]-4,6-di-p-pentyl phenyl acrylate. Then, solvent removal was carried out to obtain block copolymer A-8. &lt;Block copolymer A-9&gt; Using an autoclave equipped with a stirrer, 0.074 parts by mass of n-butyllithium was added to a cyclohexane solution containing 15 parts by mass of styrene under a nitrogen atmosphere, and relative to n-butyl To the base lithium, 0.3-mole of tetradecylethylenediamine was added, and the mixture was continuously supplied at 70 ° C for 20 minutes for polymerization. 157712.doc -36-201213426 Then, 10 parts by mass of a cyclohexane solution containing 1,3-butadiene was continuously supplied under grasping for 20 minutes for polymerization. Then, 57 parts by mass of phenylethyl women and 18 parts by mass of a cyclohexane solution of butyl women were continuously supplied at 7 (TC for 8 minutes to carry out polymerization. Then, in the polymerizer, 'relative to the n-butyl group And adding the molar amount of methanol of the molar amount of 2-[1-(2-pyridyl_3,5-di-p-pentylphenyl) as a stabilizer with respect to 100 parts by mass of the block copolymer Ethyl]_4,6_di-p-pentyl phenyl acrylate vinegar. Then, solvent removal is carried out to obtain block copolymer A_9. <Block copolymer Al 〇> Using a high-pressure dad with (4) machine, To a cyclohexane solution containing 47 parts by mass of styrene, a n-butyl (tetra) portion by mass, and a tetramethylethylenediamine having a molar ratio of 3 times moles to n-butyllithium were added under a nitrogen atmosphere. The polymerization was carried out by continuously supplying at 55 ° C for 55 minutes. Then, a solution of 6 parts by mass of 1,3-butadiene in a cyclohexane solution was continuously supplied to the thief for 1 minute to carry out polymerization. The portion of the cyclohexane solution is continuously supplied for 5 to 5 minutes for polymerization. Then, in the polymerization device, it is added with respect to n-butyllithium. The methanol of the ear is added with 〇·3 parts by mass of 2-Π ♦ methoxy- 3,5•di-t-amylphenyl)ethyl]_4 as a stabilizer with respect to 1 part by mass of the block copolymer. 6_two second decyl phenyl acetoin g. Then, solvent removal was carried out to obtain a block copolymer Α_ι〇. &lt;Block copolymer A-ll&gt; 157712.doc -37- 201213426 An autoclave equipped with a stirrer is added with n-butyl dibasic in an amount of a cyclohexane solution in a nitrogen atmosphere, and The addition of 0.3 times mole of tetra-p-ethylene ethylenediamine to n-butyllithium was continuously supplied at 70 ° C for 30 minutes to carry out polymerization. Then, a cyclohexane solution containing 10 parts by mass of styrene and 26 parts by mass of 153-butadiene was continuously supplied at 70 ° C for 45 minutes to carry out polymerization. Then, a cyclohexane solution containing 12 parts by mass of styrene and 3 parts by mass of butadiene was continuously supplied at 70 ° C for 20 minutes to carry out polymerization. Then, a cyclohexane solution containing 22 parts by mass of styrene was polymerized at 7 (continuously supplied for 25 minutes). Then, in the polymerization vessel, isomolar methanol was added with respect to n-butyllithium. Adding 0.3 parts by mass of 2-[1-(2-hydroxy-3,5-di-p-pentylphenyl)ethyl]- 4,6-di Tripentyl phenyl acrylate vinegar. Then 'desolvation to obtain block copolymer A_丨j. The composition of component (a) '肷 segment copolymer a-1~a-11, styrene content ( The storage elastic modulus (E,) of 30%, the peak temperature of the function of dynamic viscoelasticity measurement, and the block ratio of styrene contained in the block copolymer are shown in Table 1 below. (Component (a): Method for measuring physical properties of block copolymer) &lt;(1) Styrene content (mass/〇)&gt; Using an ultraviolet spectrophotometer (Hitachi UV200), it was calculated from the absorption intensity at 262 nm. &lt;(2) Storage elastic modulus at 30 ° C (Ει) and function of dynamic viscoelasticity measurement 157712.doc 8 •38- 201213426 peak temperature of tan5> Using R The viscoelasticity measuring and analyzing device DVE-V4 manufactured by heology is used to measure the temperature range of -50 ° C to 150 ° C under the conditions of an oscillation frequency of 35 Hz and a temperature increase rate / min. &lt;(3) Block rate of styrene contained in block copolymer&gt; Method for oxidative decomposition of block copolymer by using perylene tetroxide as a catalyst by peroxidizing tert-butanol Decomposition method: IM KOLTHOFF, et al., J. Polym. Sci. 1, 429 (1946), the block chain component of styrene (the styrene block having an average degree of polymerization of about 30 or less) The components are separated, and the weight of the styrene block chain is determined according to the following formula: Block ratio of styrene (% by mass) = (weight of styrene block polymeric chain in the block copolymer / The total weight of styrene in the block copolymer) x 100 157712.doc 39- 5 201213426

【II 笨乙烯之嵌段率 (質量%) ON Ο VO VO Ό VO m v〇 s o 〇\ v〇 tan5峰值溫度 (°C) T—Η oo 1—H CN CN g 1—H T-H 〇\ g 30°C 之 Ε· (χΙΟ8 Pa) 寸 cn 卜 oo 12.8 23.4 CN cn 28.3 o CN — 29.2 CN VO 苯乙稀含量 (質量%) oo cn oo OO § VO CM 成分(a):嵌段 共聚物之結構 A1-B-A2 A1-B-A2 A1-B1-B2-A2 A1-B1-B2-A2 A1-B1-B2-A2 A1-B1-B2-A2 A1-B-A2 A1-B1-B2-A2 A-C-B A1-C-A2 A1-B1-B2-A2 嵌段共聚物 &lt; CN &lt; A-3 A-4 yr^ &lt; A-6 … _ 1 A-7 A-8 &lt; A-10 A-ll -40- 157712.doc 201213426[II Block rate of stupid ethylene (% by mass) ON Ο VO VO Ό VO mv〇so 〇 \ v〇tan5 peak temperature (°C) T—Η oo 1—H CN CN g 1—H TH 〇\ g 30 °C Ε · (χΙΟ8 Pa) inch cn oo 12.8 23.4 CN cn 28.3 o CN — 29.2 CN VO styrene content (% by mass) oo cn oo OO § VO CM component (a): structure of block copolymer A1-B-A2 A1-B-A2 A1-B1-B2-A2 A1-B1-B2-A2 A1-B1-B2-A2 A1-B1-B2-A2 A1-B-A2 A1-B1-B2-A2 ACB A1-C-A2 A1-B1-B2-A2 block copolymer &lt; CN &lt; A-3 A-4 yr^ &lt; A-6 ... _ 1 A-7 A-8 &lt; A-10 A -ll -40- 157712.doc 201213426

所加之字(數字)係用於區別各部位者, A-ll之結構中之A表示 二烯之無規共聚物嵌段 示聚笨乙 段、C表 結構可相同亦 (發泡體之特性之測定方法、評價方法) 對實施例及比較例中所製作之發泡體之特性的 法、及評價方法進行說明。 7 &lt;(4)比重&gt; 依據JIS K 7112進行測定。 &lt;(5)硬度(型號A)&gt; 使用厚度12 mm之板狀試驗片,依據JIS κ 63〇ι彈簧式 硬度試驗機Α形(型號Α)進行測定. ’》 &lt;(6)硬度(型號C)&gt; 使用厚度12 mm之板狀試驗片,藉由ASKER c型硬度計 (型號C)進行測定。 &lt;(7)拉伸強度(Tb)、切割時伸長率(Eb)〉 依據JIS K 6251測定厚度2 mm之板狀試驗片。The added word (number) is used to distinguish each part. The A in the structure of A-ll indicates that the random copolymer block of the diene shows a polystyrene block, and the structure of the C table can be the same (the characteristics of the foam) Measurement method and evaluation method) The method and evaluation method of the characteristics of the foam produced in the examples and the comparative examples will be described. 7 &lt;(4) Specific Gravity&gt; Measurement was carried out in accordance with JIS K 7112. &lt;(5) Hardness (Model A)&gt; Using a plate-shaped test piece having a thickness of 12 mm, it was measured in accordance with a JIS κ 63〇ι spring type hardness tester (model Α). '》 &lt;(6) Hardness (Model C)&gt; A plate-shaped test piece having a thickness of 12 mm was used, and measurement was performed by an Asker c-type hardness tester (Model C). &lt;(7) Tensile strength (Tb), elongation at the time of cutting (Eb)> A plate-shaped test piece having a thickness of 2 mm was measured in accordance with JIS K 6251.

Tb之單位設為(MPa) ’ Eb之單位設為(%)。 &lt;(8)尺寸穩定性(α)&gt; 測定藉由150(縱)χ150(橫)χ4 mm(厚度)之模具進行2次成 型之片的24小時之收縮率。 又’將比較例1設為1 〇〇而算出指數。 指數越小則判斷為收縮率越小且尺寸穩定性越優異。 再者’比較例1中之發泡後之收縮率為丨.8%。 157712.doc -41 - 201213426 &lt;(9)尺寸穩定性(β)&gt; 測定藉由!5〇(縱)χ150(橫)x4 mm(厚度)之模具進行硫化 發泡之片的24小時後之收縮率。 又’將比較例10設為1 〇〇而算出指數。 指數越小,則判斷為收縮率越小且尺寸穩定性越優異。 再者,比較例10中之發泡後之收縮率為12%。 &lt;(10)熱成型性&gt; 目視調查2次加熱成型後之成型品的狀態。 〇表不實用上無問題之狀態、x表示凹凸狀態差而作為製 品會導致不良之狀態。 [實施例1〜6]、[比較例1〜5] 使用成分(a)之嵌段共聚物、以及作為成分(b) 的BR及SBR,於其中使用作為成分⑷的二氧化矽、以及 作為成分⑷的發泡劑,進而使用其他添加劑,將該等調配 組成與發泡體物性示於下述表2。 使用1.7 L之試驗用班布裏混合機,將最高溫度調節成 170〜180°C,而將表2所示之調配組成中除發泡劑、其他添 加劑外的調配材料進行混練。 繼而於10尺寸^t上添加發泡劑及其他添加劑對該混練 物進行混練,將其輥出成片狀後’於14(rc進行丨次加熱壓 製成型(交聯、發泡)。 壓製條件係以1次成型品之内部硬度為35〜5〇(型號c)之 方式適當調整條件。 以30%之壓縮率對藉由該條件製作之丨次成型品實施2次成 型(於150 C下加熱壓製7分鐘、冷卻15分鐘)而獲得發泡體。 157712.doc -42- 201213426The unit of Tb is set to (MPa) ’ The unit of Eb is set to (%). &lt;(8) Dimensional stability (α)&gt; The 24-hour shrinkage ratio of the sheet which was formed twice by a mold of 150 (vertical) 150 (horizontal) χ 4 mm (thickness) was measured. Further, the index was calculated by setting Comparative Example 1 to 1 〇〇. The smaller the index, the smaller the shrinkage ratio and the more excellent the dimensional stability. Further, the shrinkage ratio after the foaming in Comparative Example 1 was 丨.8%. 157712.doc -41 - 201213426 &lt;(9) Dimensional stability (β)&gt; Measurement by! The shrinkage rate of the vulcanized foamed sheet after 5 hours (vertical) χ 150 (horizontal) x 4 mm (thickness) was measured. Further, the index was calculated by setting Comparative Example 10 to 1 〇〇. The smaller the index, the smaller the shrinkage ratio and the more excellent the dimensional stability. Further, the shrinkage ratio after foaming in Comparative Example 10 was 12%. &lt;(10) Thermoformability&gt; The state of the molded article after the second heat molding was visually investigated. The table is not practical and has no problem, and x indicates that the uneven state is poor and the product is in a bad state. [Examples 1 to 6] and [Comparative Examples 1 to 5] The block copolymer of the component (a) and the BR and SBR as the component (b) were used, and as the component (4), cerium oxide was used, and The foaming agent of the component (4) and other additives were used, and the composition and the physical properties of the foam were shown in Table 2 below. The maximum temperature was adjusted to 170 to 180 ° C using a 1.7 L test Banbury mixer, and the blending materials other than the foaming agent and other additives in the blending composition shown in Table 2 were kneaded. Then, the kneaded material is kneaded by adding a foaming agent and other additives to a size of 10, and the mixture is kneaded into a sheet shape, and then subjected to heat-press molding (cross-linking, foaming) at 14 (r). The condition is appropriately adjusted in such a manner that the internal hardness of the molded article is 35 to 5 〇 (model c). The molding of the molded product produced by the conditions is performed at a compression ratio of 30% (at 150 C). The film was heated and pressed for 7 minutes and cooled for 15 minutes to obtain a foam. 157712.doc -42- 201213426

CN 比較例5 A-10 yn v〇 寸 cn I 0.45 ίο 00 s 〇 比較例4 A-9 Ό ^Ti ΓΛ 寸 cn 0.41 m (N rS 400 g X 比較例3 A-8 in wn v〇 m cn 0.42 丨 沄 (N 440 (N X 比較例2 A-7 in v〇 m 寸 0.45 1 cn — § 〇 比較例1 A-6 in v〇 «-Η cn 寸 CO 0.38 1 穿 \o &lt;N 440 〇 X 實施例6 A-11 κη in v〇 in m 寸 CO 0.43 1 VO (N cn 370 On 00 〇 實施例5 A-5 in v〇 cn 寸 c〇 0.44 VO VO CO — 290 00 〇 實施例4 A-4 v〇 m 寸 m 0.43 CN VO 00 CO 340 ⑺ 00 〇 實施例3 A-3 v〇 ό m 寸 CO 0,42 00 (N rn 380 OS 60 〇 實施例2 A-2 in iri VO m 寸 ro 0.42 */) CO 390 (S On 〇 實施例1 1 &lt; \〇 cn rf CO 0.39 &lt;N 00 CN 420 〇 嵌段共聚物之種類 (質量%) BR(fi%) SBR(質量。/〇) 二氧化矽(質量份) 發泡劑1(質量份) 發泡劑2(質量份) 其他添加劑(質量份) 比重(g/cc) 硬度(型號c) Tb(MPa) Eb(%) 尺寸穩定性(a) 熱成型性 成分⑻ 成分(b) 成分(C) 成分(d) 1 發泡體物性 43 - 157712.doc 201213426 上述表2中之符號等詳細内容如下所述。 BR;聚丁二烯(曰本瑞翁(ΖΕΟΝ)(股)公司製造之「Nipol BR1220」) SBR ;苯乙烯-丁二烯共聚物(KUMHO公司製造之 「SBR1502」) 二氧化矽;Tosoh Silica(股)公司製造之「Nipsil VN3」 發泡劑1 ; Ρ,Ρ'-氧基雙苯磺醯肼(OBSH) 發泡劑2 ;偶氮二曱醯胺(ADCA) 其他添加劑;聚乙二醇(山陽化成工業(股)公司製造、商品 名「PEG# 4000」)1質量份 硬脂酸(旭電化(股)公司製造)1質量份 發泡助劑(脲衍生物、三協化成(股)公司製 造、商品名「Selton NF」)1質量份 DCP(98%過氧化二異丙苯、曰本油脂(股)公 司製造、商品名「PERCUMYL D」0.4質量份 [實施例7〜10]、[比較例6〜9] 如表3所示,改變成分(a)之種類與量及成分(b)、(c)、 (d)之量,藉由與實施例1相同之方法獲得發泡體。 表3中之符號等詳細内容與表2相同,物性之測定法亦與 上述相同。 157712.doc -44- ⑧ 201213426 比較例9 Α-3 in in VO in 卜 寸 cn 0.08 寸 〇 420 CN cn X 比較例8 Α-3 m \〇 o t—H T*~H cn 寸 m -1 0.58 (N § a\ 00 〇 比較例7 1 g in m 寸 cn 0.43 Ο) 510 卜 r—H 1—H X 比較例6 Α-3 ο m !/&quot;&gt; m 寸 cn 0.44 yn m cn 230 m 00 〇 實施例10 Α-3 VO iTi ΓΛ 寸 cn 0.39 (N (N 470 (N a\ 〇 實施例9 Α-3 m iT) m 寸 cn 0.44 \Τ) VjO 口 370 〇 實施例8 Α-1 (N in S vn 1-H cn 寸 rn 0.42 νΤ) m cn 370 00 00 〇 實施例7 Α-3 yr) IQ τ-Η cn 寸 cn 0.41 (N 440 v〇 Ch 〇 嵌段共聚物之種類(質量%) BR(質量%) 呂611(質量%) 二氧化矽(質量份) 發泡劑1(質量份) 1_ 發泡劑2(質量份) 其他添加劑(質量份) 比重(g/cc) 硬度(型號C) 1 Tb(MPa) Eb(%) 尺寸穩定性(a) 熱成型性 成分⑷ 成分(b) 成分(C) 成分⑹ 發泡體物性 -5 157712.doc .45 - 201213426 [實施例11] 對於上述[實施例11]之調配組成,相對於成分(a)與成分 (b) 100質量份,而添加5質量份之EVA(乙烯-乙酸乙烯酯共 聚物、Tosoh公司製造、EVAUE633、乙酸乙稀酯含量 =20%、MI=20)。 藉由其他條件與實施例1相同之方法而獲得發泡體。 所得之發泡體之比重為0.39 g/cc,硬度為54,Tb為3 _0 MPa,Eb為390%,尺寸穩定性為93,熱成型性為〇表現良 好之物性。 可知實施例1〜11之發泡體均為硬度、尺寸穩定性、熱成 型性及機械強度優異之發泡體。 [實施例12〜17]、[比較例 使用作為成分(a)的嵌段共聚物a-1〜〗1、作為成分(b)的 BR(順1,4聚丁二烯):高順聚丁二烯&amp;S_SBR,使用作為成 分(C)的二氧化矽' 以及作為成分(d)的發泡劑進而使用 其他添加劑,將該等調配組成與發泡體物性示於下述表 4 〇 使用1.7 L之试驗用班布裏混合機,將最高溫度調節為 170~180°C,將下诚矣dp;匕- 表4所不之調配組成中除發泡劑、其他 添加劑外之調配材料進行混練。 繼而,於10尺寸輕μ I上添加發泡劑及其他添加劑對該; 物進行混練,將盆叙、 /、觀出成片狀後’放入模具進行硫介 交聯)、發泡而獲得菸 ^ /包體。硫化係於160。(:下進行] 鐘。 1577l2.doc ⑧ -46 - 201213426 比較例14 A-10 (N »n o 0.93 Μ 153 OS 比較例13 A-9 &lt;Ν »〇 &lt;Ti 10.1 0.91 1 〇 11.4 S 比較例12 A-8 in in ci 0.90 1 10.0 Ό (N &gt;—« o 比較例11 A-7 «Λ CN to »〇 10.1 1 0.93 1 CN 〇\ 'O VO 比較例10 A-6 (N m 1··^ 10.1 0.89 io v© 10.5 o 實施例17 A-11 u-i (N in 10.1 0.90 cn 11.2 〇 實施例16 A-5 VV CN ^—4 *Ti o 0.93 ] g 14.2 ON 實施例15 A-4 (N o 0.92 r- 12.2 is 00 實施例14 A-3 (N 10.1 0.91 1 S 11.2 v〇 ON 00 00 實施例13 A-2 (N iTi o 0.91 CN 11.4 s 5; 實施例12 1 &lt; (N in 10.1 1 0.90 o Ό 10.3 o 1-H r*H ΙΛ Q\ 嵌段共聚物之種類 (質量%) BR(順1,4聚丁二烯) (質量%) 5-5811(質量%) 二氧化矽(質量份) 發泡劑1(質量份) 發泡劑2(質量份) 其他添加劑(質量份) 1 比重(g/cc) 硬度(型號A) Tb(MPa) Eb(%) 尺寸穩定性(β) 成分⑻ 成分(b) 成分⑹ 成分(d) 發泡體物 性 • 47· 157712.doc 201213426 上述表4中之符號等詳細内容如以下所述。 BR(順1,4聚丁二烯);曰本合成橡膠(股)公司製造之「BR- 18j S-SBR;苯乙烯-丁二烯共聚物(旭化成化學(股)公司製造 之「Asaprene 303」) 二氧化矽;Tosoh Silica(股)公司製造之「Nipsil VN3」 發泡劑1; P,P'-氧基雙苯磺醯肼(0BSH) 發泡劑2;偶氮二曱醯胺(ADCA) 其他添加劑,聚乙·一醇(山陽化成工業(股)公司製造、商品 名「PEG# 4000」)1質量份 氧化鋅3質量份 硬脂酸(旭電化(股)公司製造)1質量份 氧化鈦(銳鈦礦型)4質量份 發泡助劑(脲衍生物、三協化成(股)公司製 造、商品名「SeltonNF」)1質量份 DCP(98%過氧化二異丙苯、曰本油脂(股)公 司製造、商品名「PERCUMYL D」0.05質量份 硫0.05質量份 [實施例I8〜21]、[比較例15〜18] 如下述表5所示’改變成分(a)之種類與量及成分(b)、 (c)、(d)之量’藉由與上述實施例12相同之方法獲得發泡 體。 表5中之符號等詳細内容與表4相同,物性之測定法亦與 上述相同° 157712.doc -48- 201213426 比較例18 A-3 (N in 10.1 0.73 CN V&quot;) &lt;N 寸 ϊ-Η (N CS 比較例17 A-3 (N m 〇 τ-Η T—Η &lt;ό 0.95 00 00 13.8 &lt;N 00 比較例16 晒 % o 0.89 VO ON VO i i m 比較例15 A-3 cs y-^ 10.1 0.92 〇\ (N cK CN VO z 實施例21 A-3 (Ν m &lt;N i〇 〇 0.86 Os o 實施例20 A-3 CN yr\ \r\ 〇 in 10.1 丨 0.93 § Oi 00 QO 實施例19 A-1 m m i/Ί in 〇 10.1 0.91 Os 12.8 m 00 實施例18 A-3 00 in 10.1 0.90 Ό VO 〇\ 00 o m 嵌段共聚物之種類 (質量%) BR(順1,4聚丁二烯) (質量%) 8名311(質量%) 二氧化矽(質量份) 發泡劑l(質量份) 發泡劑2(質量份), 其他添加劑(質量份) 比重(g/cc) 硬度(型號A) Tb(MPa) Eb(%) 尺寸穩定性(β) 成分(a) 成分(b) 成分(C) 成分(d) 1 發泡體物性 -49- 157712.doc 201213426 [實施例22] 對於上述[實施例1 8]之調配組成,相對於成分(a)與成分 (b)100質量份,而添加5質量份之EVA(乙烯-匕酸乙烯酯共 聚物、Tosoh公司製造、EVAUE63 3、乙酸乙稀酿含量 =20%、MI=20) 〇 藉由其他條件與[實施例1 8]相同之方法而獲得發泡體。 所得之發泡體之比重為〇.9〇 g/cc,硬度為68,Tb為9.2 MPa ’ Eb為110%,尺寸穩定性為95表現良好之物性。 可知實施例12〜22之發泡體均為硬度、尺寸穩定性、及 機械強度優異之發泡體。 產業上之可利用性 ^明之發泡體適合於鞋用中底、鞋塾或外底材料, 材料5而::男士鞋、女士鞋、休閒鞋等所有鞋類之鞋 材枓,而具有產業上之可利用性。 157712.doc ⑧ •50-CN Comparative Example 5 A-10 yn v〇inchcn I 0.45 ίο 00 s 〇Comparative Example 4 A-9 Ό ^Ti ΓΛ inch cn 0.41 m (N rS 400 g X Comparative Example 3 A-8 in wn v〇m cn 0.42 丨沄 (N 440 (NX Comparative Example 2 A-7 in v〇m inch 0.45 1 cn — § 〇 Comparative Example 1 A-6 in v〇«-Η cn inch CO 0.38 1 wear \o &lt;N 440 〇 X Example 6 A-11 κη in v〇in m inch CO 0.43 1 VO (N cn 370 On 00 〇 Example 5 A-5 in v〇cn inch c〇0.44 VO VO CO — 290 00 〇 Example 4 A -4 v〇m inch m 0.43 CN VO 00 CO 340 (7) 00 〇 Example 3 A-3 v〇ό m inch CO 0,42 00 (N rn 380 OS 60 〇Example 2 A-2 in iri VO m inch Ro 0.42 */) CO 390 (S On 〇Example 1 1 &lt; \〇cn rf CO 0.39 &lt;N 00 CN 420 Type of 〇 block copolymer (% by mass) BR(fi%) SBR (mass./ 〇) cerium oxide (parts by mass) Foaming agent 1 (parts by mass) Foaming agent 2 (parts by mass) Other additives (parts by mass) Specific gravity (g/cc) Hardness (model c) Tb (MPa) Eb (%) Dimensional stability (a) Thermoformability component (8) Component (b) Component (C) Component (d) 1 hair Physical properties 43 - 157712.doc 201213426 The details of the symbols in Table 2 above are as follows: BR; polybutadiene ("Nipol BR1220" manufactured by 曰本瑞翁(ΖΕΟΝ))) SBR; styrene - Butadiene copolymer ("SBR1502" manufactured by KUMHO Co., Ltd.) cerium oxide; "Nipsil VN3" foaming agent 1 manufactured by Tosoh Silica Co., Ltd.; Ρ, Ρ'-oxybisbenzene sulfonate (OBSH) ) foaming agent 2; azodiamine (ADCA) other additives; polyethylene glycol (manufactured by Shanyang Chemical Industry Co., Ltd., trade name "PEG# 4000") 1 part by mass of stearic acid (Acacia ( (manufactured by the company) 1 part by mass of foaming auxiliary (urea derivative, manufactured by Sankyo Chemical Co., Ltd., trade name "Selton NF") 1 part by mass of DCP (98% dicumyl peroxide, sakamoto grease) (Stock) company, product name "PERCUMYL D" 0.4 parts by mass [Examples 7 to 10], [Comparative Examples 6 to 9] As shown in Table 3, the type, amount and composition of component (a) were changed (b) The amounts of (c) and (d) were obtained by the same method as in Example 1. The details of the symbols and the like in Table 3 are the same as those in Table 2, and the measurement method of the physical properties is also the same as described above. 157712.doc -44- 8 201213426 Comparative Example 9 Α-3 in in VO in 卜 inch 0.08 inch 〇420 CN cn X Comparative Example 8 Α-3 m \〇ot-HT*~H cn inch m -1 0.58 ( N § a\ 00 〇Comparative Example 7 1 g in m inch cn 0.43 Ο) 510 卜r-H 1—HX Comparative Example 6 Α-3 ο m !/&quot;&gt; m inch cn 0.44 yn m cn 230 m 00 〇Example 10 Α-3 VO iTi 寸 inch cn 0.39 (N (N 470 (N a 〇 Example 9 Α-3 m iT) m inch cn 0.44 \Τ) VjO port 370 〇 Example 8 Α-1 ( N in S vn 1-H cn inch rn 0.42 νΤ) m cn 370 00 00 〇 Example 7 Α-3 yr) IQ τ-Η cn inch cn 0.41 (N 440 v〇Ch 〇 block copolymer type (quality %) BR (% by mass) Lu 611 (% by mass) cerium oxide (parts by mass) Foaming agent 1 (parts by mass) 1_Blowing agent 2 (parts by mass) Other additives (parts by mass) Specific gravity (g/cc) Hardness (Model C) 1 Tb (MPa) Eb (%) Dimensional stability (a) Thermoformability component (4) Component (b) Component (C) Component (6) Foam physical property - 5 157712.doc .45 - 201213426 [Examples 11] With respect to the compounding composition of the above [Example 11], with respect to the component (a) and the component (b) 100 parts by mass, and 5 parts by mass of EVA (ethylene-vinyl acetate copolymer, manufactured by Tosoh Corporation, EVAUE 633, ethyl acetate content = 20%, MI = 20) was added. The other conditions were the same as in Example 1. A foam was obtained by the method. The obtained foam had a specific gravity of 0.39 g/cc, a hardness of 54, a Tb of 3 _0 MPa, an Eb of 390%, a dimensional stability of 93, and a thermoformability which is a property of 〇. The foams of Examples 1 to 11 were all foams excellent in hardness, dimensional stability, thermoformability, and mechanical strength. [Examples 12 to 17], [Comparative examples were used as the components (a). Segment copolymer a-1 to 1:1, BR (cis 1,4 polybutadiene) as component (b): high-cis polybutadiene & S_SBR, using cerium oxide as component (C) and as a component The foaming agent of (d) is further used with other additives, and the composition of the blend and the physical properties of the foam are shown in Table 4 below. The test banbury mixer is used in 1.7 L, and the maximum temperature is adjusted to 170-180. °C, will be under the 矣 dp; 匕 - Table 4 is not in the mix of the composition of the foaming agent, other additives Line kneading. Then, the foaming agent and other additives are added to the 10 size light μ I to knead the material, and the mixture is formed into a sheet, and then placed in a mold for sulfur-crosslinking and foaming. Smoke ^ / inclusion body. The vulcanization is at 160. (: proceeding under the clock) 1577l2.doc 8 -46 - 201213426 Comparative Example 14 A-10 (N »no 0.93 Μ 153 OS Comparative Example 13 A-9 &lt;Ν »〇&lt;Ti 10.1 0.91 1 〇11.4 S Comparison Example 12 A-8 in in ci 0.90 1 10.0 Ό (N &gt; - « o Comparative Example 11 A-7 «Λ CN to »〇10.1 1 0.93 1 CN 〇\ 'O VO Comparative Example 10 A-6 (N m 1··^ 10.1 0.89 io v© 10.5 o Example 17 A-11 ui (N in 10.1 0.90 cn 11.2 〇Example 16 A-5 VV CN ^—4 *Ti o 0.93 ] g 14.2 ON Example 15 A- 4 (N o 0.92 r- 12.2 is 00 Example 14 A-3 (N 10.1 0.91 1 S 11.2 v〇ON 00 00 Example 13 A-2 (N iTi o 0.91 CN 11.4 s 5; Example 12 1 &lt; (N in 10.1 1 0.90 o Ό 10.3 o 1-H r*H ΙΛ Q\ Type of block copolymer (% by mass) BR (cis 1,4 polybutadiene) (% by mass) 5-5811 (% by mass) ) Cerium dioxide (parts by mass) Foaming agent 1 (parts by mass) Foaming agent 2 (parts by mass) Other additives (parts by mass) 1 Specific gravity (g/cc) Hardness (Model A) Tb (MPa) Eb (%) Dimensional stability (β) Component (8) Component (b) Component (6) Component (d) Foam • 47· 157712.doc 201213426 The details of the symbols in Table 4 above are as follows: BR (cis 1,4 polybutadiene); "BR- 18j S-SBR" manufactured by 曰本合成橡胶有限公司; styrene-butadiene copolymer ("Asaprene 303" manufactured by Asahi Kasei Chemicals Co., Ltd.) cerium oxide; "Nipsil VN3" foaming agent 1 manufactured by Tosoh Silica Co., Ltd.; P, P'-oxygen Bis-benzene sulfonate (0BSH) foaming agent 2; azodiamine (ADCA) Other additives, polyethylidene alcohol (manufactured by Shanyang Chemical Industry Co., Ltd., trade name "PEG# 4000")1 3% by mass of zinc oxide (manufactured by Asahi Kasei Co., Ltd.), 1 part by mass of titanium oxide (anatase type), 4 parts by mass of a foaming auxiliary (urea derivative, manufactured by Sankyo Chemical Co., Ltd.) , product name "SeltonNF") 1 part by mass of DCP (98% dicumyl peroxide, sakamoto oil company), trade name "PERCUMYL D" 0.05 parts by mass sulfur 0.05 parts by mass [Examples I8 to 21] [Comparative Examples 15 to 18] As shown in Table 5 below, 'Change the type and amount of component (a) and components (b), (c), d) The amount 'by the same procedures as in Example 12 to obtain the above-described foam. The details of the symbols in Table 5 are the same as those in Table 4, and the measurement method of physical properties is also the same as above. 157712.doc -48-201213426 Comparative Example 18 A-3 (N in 10.1 0.73 CN V&quot;) &lt;N inch ϊ- Η (N CS Comparative Example 17 A-3 (N m 〇τ-Η T-Η &lt;ό 0.95 00 00 13.8 &lt; N 00 Comparative Example 16 Sun % o 0.89 VO ON VO iim Comparative Example 15 A-3 cs y -^ 10.1 0.92 〇\ (N cK CN VO z Example 21 A-3 (Ν m &lt;N i〇〇0.86 Os o Example 20 A-3 CN yr\ \r\ 〇in 10.1 丨0.93 § Oi 00 QO Example 19 A-1 mmi/Ί in 〇10.1 0.91 Os 12.8 m 00 Example 18 A-3 00 in 10.1 0.90 Ό VO 〇\ 00 om Type of block copolymer (% by mass) BR (cis 1,4 Polybutadiene) (% by mass) 8 311 (% by mass) cerium oxide (parts by mass) Foaming agent l (parts by mass) Foaming agent 2 (parts by mass), other additives (parts by mass) Specific gravity (g/ Cc) Hardness (Model A) Tb (MPa) Eb (%) Dimensional stability (β) Component (a) Component (b) Component (C) Component (d) 1 Foam physical property -49- 157712.doc 201213426 [ Example 22] For the compounding composition of the above [Example 18], 5 parts by mass of EVA (ethylene-vinyl phthalate copolymer, manufactured by Tosoh, EVAUE 63 3, ethyl acetate content = 20%, MI =) was added to 100 parts by mass of the component (a) and the component (b). 20) A foam was obtained by the same method as [Example 18] under other conditions. The obtained foam had a specific gravity of 〇.9〇g/cc, a hardness of 68, and a Tb of 9.2 MPa. Eb was 110%, and the dimensional stability was 95. The foams of Examples 12 to 22 were all foams excellent in hardness, dimensional stability, and mechanical strength. Industrial Applicability Suitable for shoe midsole, shoe last or outsole material, material 5:: men's shoes, ladies' shoes, casual shoes and other footwear materials, but with industrial availability. 157712.doc 8 •50-

Claims (1)

201213426 七、申請專利範園: -種發泡體’其係使包含下述成分之發泡體用組合物交 聯而成:⑷嵌段共聚物,其含有至少2個乙婦基芳香族 烴聚合物嵌段、以及至少i個包含共輛二稀與乙稀基芳 香族烴之共聚物嵌段,且 質量%、共軛二烯之含 乙烯基芳香族烴之含量為65〜95 量為5〜35質量%, 嵌段共聚物所含有之乙烯基芳香族烴聚合物之 為40〜98質量%, 储存彈性模數(E,)為3x10 Γ 動態黏彈性測定中3〇°c P a以上2·35&gt;&lt;1〇9 p以下 日叙* Pa以下,且動態黏彈性測定之函數 之峰值溫度於85。(:以上125ΐ:以下存在至少丨個; (b)異戊二烯系橡膠及/或二烯系橡膠; 0)填充劑; (d)發泡劑; 上述⑷嵌段共聚物與上述(b)異戊二稀系橡膠及/或二 稀系橡膠之貝量比(⑷/⑻)為(卜叫/⑺〜99); 使相對於上述⑷嵌段共聚物與上述⑻ 膠及/或二稀系橡膠之合計量1G㈣旦卜⑥“ τ置iuo貝里伤,而含有上述(c) 真充劑1〜100質量份、上述(d)發泡劑〇1〜3〇質量份; 且該發泡體比重為(U〜0 98 g/cc。 2.如請求項1之發泡體,其中上诚旃p 述(a)嵌段共聚物係動態黏 測疋之函數ίαηδ之峰值温度於9〇。〇以上125。〔以下存 在至少1個。 157712.doc 201213426 3·如請求項1或2之發泡體,其中上述(a)嵌段共聚物含有至 ;1個包含乙烯基芳香族烴含量為7〇質量%以上未達 質量%之乙婦基芳香族煙與共輛二婦之無規共聚物嵌 段。 4. 如請求項1至3中任一項之發泡體,其中上述(a)嵌段共聚 物含有至少i個包含乙烯基芳香族烴含量為75質量%以上 98質量%以下之乙烯基芳香族烴與共軛二烯之無規共聚 物嵌段。 ~ 5. 如請求項1至4中任一項之發泡體,其中相對於上述(a)嵌 段共聚物與上述(b)異戊二烯系橡膠及/或二烯系橡膠之 合計量100質量份,含有: 上述(C)填充劑2〜90質量份、 上述(d)發泡劑〇.5〜20質量份。 6. 如請求項1至5中任一項之發泡體’其中相對於上述(&amp;)嵌 段共聚物與上述(b)異戊二烯系橡膠及/或二烯系橡膠之 合計量100質量份,進而含有: (e)熱塑性彈性體及/或熱塑性樹脂1〜丨〇〇質量份。 7. 如請求項1至6中任一項之發泡體,其比重為〇1〜〇 7 g/cc、或比重為 〇·8〜0.98 g/cc。 8. 一種鞋底,其係將如請求項1至7中任一項之發泡體成型 而成。 9. 一種發泡體用組合物’其包含:(a)嵌段共聚物,其含有 至少2個乙烯基芳香族烴聚合物嵌段、以及至少1個包含 共輛二烯與乙烯基芳香族烴之共聚物嵌段,且 157712.doc 201213426 乙烯基芳香族烴之含量為65〜95質量。共軛二烯之含 量為5〜35質量%, 嵌段共聚物所含有之乙烯基芳香族烴聚合物 之嵌段率 為40〜98質量%, ψ ίο. 動態黏彈性測定中机下之錯存彈性模數(eWx1〇8 Pa以上2·35χ1〇 pa以下,且動態黏彈性測定之函數匕以 之峰值溫度於85t以上125t以下存在至少丨個; (b) 異戊二烯系橡膠及/或二烯系橡膠; (c) 填充劑; (d) 發泡劑; 上述(a)嵌段共聚物與上述(b)異戊二烯系橡膠及/或二 烯系橡膠之質量比“…/化乃為^〜^^川〜%); 相對於上述⑷喪段共聚物與上述(b)異戊二稀系橡膠 及/或二烯系橡膠之合計量質量份,而含有上述(c)填 充劑1〜100質量份、上述(d)發泡劑〇 &gt;30質量份。 一種發泡體,其包含:(ai)嵌段共聚物,其含有至少2個 乙烯基芳香族烴聚合物嵌段、以及至少丨個包含共軛二 稀與乙烯基芳香族烴之共聚物嵌段,且 乙烯基芳香族烴之含量為65〜95質量%、共軛二烯之含 量為5〜35質量%, 敢·#又共聚物所含有之乙烯基芳香族烴聚合物之嵌段率 為40〜98質量% ; (b) 異戊二烯系橡膠及/或二烯系橡膠; (c) 填充劑; 157712.doc 5 201213426 (d)發泡劑; 比重為0.1〜0.7 g/cc時,藉由型號C測定之硬度為 45〜98 ; 比重為0.8〜0.98 g/cc時,藉由型號A測定之硬度為 60〜98 〇 157712.doc -4- ⑧ 201213426 四、指定代表圖: (一) 本案指定代表圖為:(無) (二) 本代表圖之元件符號簡單說明: 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式: (無) 157712.doc ⑤ * *201213426 VII. Application for Patent Park: - A type of foam which is obtained by crosslinking a composition containing a foam having the following components: (4) a block copolymer containing at least two ethyl women's aromatic hydrocarbons a polymer block, and at least i copolymer blocks comprising a total of dilute and ethylene-based aromatic hydrocarbons, and the content of the vinyl-containing aromatic hydrocarbons of the mass % and the conjugated diene is 65 to 95. 5 to 35 mass%, the vinyl aromatic hydrocarbon polymer contained in the block copolymer is 40 to 98% by mass, and the storage elastic modulus (E,) is 3x10 〇 in the dynamic viscoelasticity measurement 3〇°c P a The above 2·35&gt;&lt;1〇9p is less than or equal to *Pa, and the peak temperature of the function of the dynamic viscoelasticity measurement is 85. (: 125 以上 above: at least one of the following; (b) isoprene-based rubber and/or diene-based rubber; 0) filler; (d) foaming agent; (4) block copolymer and the above (b) The ratio of the amount of the isoprene-based rubber and/or the di-thin rubber ((4)/(8)) is ((4) to 99); compared with the above (4) block copolymer and the above (8) glue and/or two The total amount of the rare rubber is 1G (four) denier 6" τ set iuo bei injury, and contains 1 to 100 parts by mass of the above (c) true charge, and the above (d) foaming agent 〇 1 to 3 parts by mass; The specific gravity of the foam is (U~0 98 g/cc. 2. The foam according to claim 1, wherein the upper layer is a function of the dynamic cohesive enthalpy of the block copolymer ίαηδ 9〇.〇125. [There is at least one of the following. 157712.doc 201213426 3. The foam of claim 1 or 2, wherein the (a) block copolymer contains to; one contains vinyl aromatic a random copolymer block of a total amount of 7% by mass or more and less than 7% by mass of the ethylene-based aromatic tobacco and a total of two women. 4. The foam according to any one of claims 1 to 3, The above (a) block copolymer contains at least i random copolymer blocks of a vinyl aromatic hydrocarbon and a conjugated diene having a vinyl aromatic hydrocarbon content of 75% by mass or more and 98% by mass or less. The foam according to any one of claims 1 to 4, wherein a total mass of 100 mass relative to the above (a) block copolymer and the above (b) isoprene-based rubber and/or diene rubber And a part of the above-mentioned (C) filler: 2 to 90 parts by mass, and the above (d) foaming agent 〇 5 to 20 parts by mass. 6. The foam according to any one of claims 1 to 5, wherein 100 parts by mass of the above-mentioned (&amp;) block copolymer and the above (b) isoprene-based rubber and/or diene-based rubber, and further contains: (e) thermoplastic elastomer and/or thermoplastic resin 1 The foam according to any one of claims 1 to 6, which has a specific gravity of 〇1 to 〇7 g/cc, or a specific gravity of 〇·8 to 0.98 g/cc. A shoe sole formed by molding the foam of any one of claims 1 to 7. 9. A composition for a foam comprising: (a) a block copolymer, There are at least two vinyl aromatic hydrocarbon polymer blocks, and at least one copolymer block comprising a total of a diene and a vinyl aromatic hydrocarbon, and the content of the 157712.doc 201213426 vinyl aromatic hydrocarbon is 65~ 95 mass. The content of the conjugated diene is 5 to 35% by mass, and the block ratio of the vinyl aromatic hydrocarbon polymer contained in the block copolymer is 40 to 98% by mass, ψ ίο. The next error is the elastic modulus (eWx1〇8 Pa or more and 2.35χ1〇pa or less, and the function of dynamic viscoelasticity measurement is at least one peak temperature above 85t and 125t; (b) isoprene (a) a filler; (d) a foaming agent; the mass of the above (a) block copolymer and the above (b) isoprene-based rubber and/or diene rubber It is contained in the total mass fraction of the above-mentioned (b) isocyanate rubber and/or the diene rubber, and is contained in the above-mentioned (4) toluene copolymer and the above (b) isoprene rubber and/or diene rubber. The above (c) filler is 1 to 100 parts by mass, and the above (d) foaming agent 〇 is 30 parts by mass. A foam comprising: (ai) a block copolymer comprising at least two vinyl aromatic hydrocarbon polymer blocks, and at least one copolymer comprising a conjugated dilute and a vinyl aromatic hydrocarbon And the content of the vinyl aromatic hydrocarbon is 65 to 95% by mass, the content of the conjugated diene is 5 to 35% by mass, and the block ratio of the vinyl aromatic hydrocarbon polymer contained in the copolymer 40 to 98% by mass; (b) Isoprene-based rubber and/or diene-based rubber; (c) Filler; 157712.doc 5 201213426 (d) Foaming agent; Specific gravity: 0.1 to 0.7 g/cc The hardness measured by the model C is 45 to 98; when the specific gravity is 0.8 to 0.98 g/cc, the hardness measured by the model A is 60 to 98 〇 157712.doc -4- 8 201213426 4. Designation: (1) The representative representative of the case is: (none) (2) The symbol of the symbol of the representative figure is simple: 5. If there is a chemical formula in this case, please disclose the chemical formula that best shows the characteristics of the invention: (none) 157712.doc 5 * *
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