JP5394757B2 - Cross-linked foam composition, cross-linked foam, and footwear and laminate using the same - Google Patents

Description

  The present invention relates to a cross-linked foam composition and a cross-linked foam, as well as footwear and a laminate using the same.

  Cross-linked foams are light and flexible, and are widely used as footwear materials, various daily necessities, packaging materials, and the like as materials having high mechanical strength. In recent years, as base polymers for impact absorbers, resins such as polystyrene, polyethylene, and ethylene-vinyl acetate copolymers, and elastomers such as natural rubber, styrene-butadiene copolymers, and acrylonitrile-butadiene copolymers have been used. ing.

  For example, Patent Document 1 discloses, as a polymer for impact-absorbing foams, a copolymer having a tan δ peak composed of a conjugated diene and an aromatic vinyl monomer in the range of −20 to 40 ° C., and a conjugated diene and an aromatic vinyl monomer. A combination with a copolymer having a tan δ peak in the range of −70 to 20 ° C. has been proposed.

JP 05-345833 A

  However, the performance of a crosslinked foam used as an impact absorber or the like is not always sufficient. There is a need for a crosslinked foam that is not only lightweight and flexible, but also has an excellent balance of various physical properties. For example, if it is used as an impact absorber for footwear, etc., it is not only lightweight and flexible, but also has low-temperature curing resistance so that it can be used in cold regions and the impact when landing as a sole used for shoe soles. However, it is required to be excellent in low rebound resilience for relieving stress and mechanical strength such as peel strength and compression set, but development of a crosslinked foam capable of satisfying these physical properties is not sufficient.

  Accordingly, the present invention provides a crosslinked foam, footwear, laminate and a composition for crosslinked foam that can provide them with low temperature curing resistance, low rebound resilience (impact absorbability), peel strength, compression set resistance and weight reduction. The purpose is to provide goods.

  As a result of intensive studies to solve the above problems, the present inventors have obtained two types of hydrogenated copolymers mainly comprising a conjugated diene unit having a specific tan δ peak temperature and a vinyl aromatic unit, By making a composition for crosslinking and foaming containing an ethylene copolymer having a specific Shore A hardness, a crosslinking agent, and a foaming agent, low-temperature curing resistance, low rebound resilience (impact absorption), peel strength, The present inventors have found that a crosslinked foam excellent in compression set and weight reduction can be obtained, and completed the present invention.

That is, the present invention provides the following.
[1] (A) a hydrogenated copolymer of a copolymer mainly composed of a conjugated diene unit and a vinyl aromatic unit having a tan δ peak temperature of −15 ° C. or more and less than 15 ° C., and (B) tan δ peak temperature A hydrogenated copolymer of a copolymer mainly composed of a conjugated diene unit and a vinyl aromatic unit, and (C) an ethylene copolymer 10 having a Shore A hardness of 70 degrees or more. (A) component and (B) component with respect to the sum total of (A) component, (B) component, and (C) component containing 60 mass%, (D) crosslinking agent, and (E) foaming agent The composition for crosslinked foaming whose sum total is 40-90 mass%.
[2] The composition for cross-linking and foaming according to [1], further comprising (F) an inorganic filler.
[3] In the composition for crosslinking and foaming, the content of the component (D) is 0.05 to 3% by mass, the content of the component (E) is 0.2 to 15% by mass, and (F ) The composition for cross-linking and foaming according to [1] or [2], wherein the content of the component is 0 to 20% by mass.
[4] The composition for crosslinking and foaming according to any one of [1] to [3], wherein the Shore A hardness of the component (C) is 75 degrees or more.
[5] The composition for cross-linking and foaming according to any one of [1] to [4], wherein the component (C) is an ethylene / α-olefin copolymer.
[6] The composition for crosslinking and foaming according to any one of [1] to [5], wherein the content of the component (F) is 0 to 10% by mass relative to the total amount of the composition for crosslinking and foaming.
[7] The crosslinked foaming composition according to any one of [1] to [6], wherein the content of the component (A) is greater than the content of the component (B).
[8] The components (A) and / or (B) are hydrogenated copolymers in which 10 to 70 mol% of unsaturated groups contained before hydrogenation are hydrogenated. [1] to [7] The composition for crosslinked foaming as described in any one of these.
[9] (A) component and / or (B) component is a polymer block mainly composed of vinyl aromatic units, a hydrogenated copolymer block mainly composed of vinyl aromatic units and conjugated diene units, The composition for crosslinked foaming according to any one of [1] to [8], comprising:
[10] The component (A) and / or the component (B) contains two or more hydrogenated copolymer blocks composed of conjugated diene units and vinyl aromatic units, each having a different vinyl aromatic content. The composition for cross-linking and foaming according to any one of [1] to [9].
[11] The crosslinked foaming composition according to any one of [1] to [10], wherein at least one of the tan δ peak temperatures of the component (A) is −5 ° C. or higher and lower than 15 ° C.
[12] The crosslinked foaming composition according to any one of [1] to [11], wherein at least one of the tan δ peak temperatures of the component (B) is 15 ° C. or higher and 35 ° C. or lower.
[13] The crosslinked foaming composition according to any one of [1] to [12], wherein the component (A) and / or the component (B) has a linear structure obtained by sequential polymerization.
[14] The content (A / (A + B + C)) of the component (A) is 30 to 65% by mass or less with respect to the total of the components (A), (B), and (C), and (B ) Component content (B / (A + B + C)) is 15 to 50% by mass or less, (C) component content (C / (A + B + C)) is 20 to 55% by mass or less, and crosslinking The content of the component (D) with respect to the total amount of the foaming composition is 0.2 to 1.5% by mass, and the content of the component (E) with respect to the total amount of the crosslinked foaming composition is 0.5 to 10 The composition for cross-linking and foaming according to any one of [1] to [12], which is% by mass.
[15] A cross-linked foam comprising the composition according to any one of [1] to [14].
[16] Footwear comprising the crosslinked foam according to [15].
[17] Footwear comprising the cross-linked foam according to [15] in a midsole or an insole.
[18] A laminate comprising the crosslinked foam according to [15] and a member on which the crosslinked foam is laminated.

  ADVANTAGE OF THE INVENTION According to this invention, the cross-linked foam, footwear, laminated body excellent in low temperature-curing resistance, low rebound resilience (impact absorbability), peel strength, compression set, and weight reduction, and the composition for cross-linking foam which can give them It can be a thing.

  Hereinafter, a mode for carrying out the present invention (hereinafter simply referred to as “the present embodiment”) will be described in detail. The following embodiments are examples for explaining the present invention, and are not intended to limit the present invention to the following contents. The present invention can be implemented with appropriate modifications within the scope of the gist thereof.

  The composition for impact-absorbing cross-linking and foaming of the present embodiment comprises (A) a hydrogenated copolymer of a copolymer mainly composed of a conjugated diene unit and a vinyl aromatic unit having a tan δ peak temperature of −15 ° C. or more and less than 15 ° C. (B) a hydrogenated copolymer of a copolymer mainly composed of a conjugated diene unit and a vinyl aromatic unit having a tan δ peak temperature of 15 ° C. or higher, and (C) a Shore A hardness of 70 ° C. or higher. It contains 10 to 60% by mass of a certain ethylene copolymer, (D) a crosslinking agent, and (E) a foaming agent, and is based on the sum of the components (A), (B), and (C) ( The total of (A) component and (B) component ((A + B) / (A + B + C)) is 40-90 mass%.

<(A) component and (B) component>
Both the component (A) and the component (B) are hydrogenated copolymers of a copolymer mainly composed of a conjugated diene unit and a vinyl aromatic unit, and the tan δ peak temperature of the component (A) is −15 ° C. The temperature is lower than 15 ° C., and the tan δ peak temperature of the component (B) is 15 ° C. or higher.

The component (A) and the component (B) can be obtained by hydrogenating a part or all of a copolymer mainly composed of (i) a conjugated diene unit and (ii) a vinyl aromatic unit.
The “main body” in this embodiment means that the monomer unit is contained in an amount of 60% by mass or more, more preferably 85% by mass or more, and still more preferably 95% by mass or more.

  (I) A conjugated diene unit is a diolefin having a pair of conjugated double bonds. The kind of conjugated diene unit is not particularly limited, and known ones can be used. For example, 1,3-butadiene, isoprene, 2,3-dimethyl-butadiene, 2-methyl-1,3-pentadiene, myrcene, 2-methyl-1,3-pentadiene, 3-methyl-1,3-pentadiene, 4-methyl-1,3-pentadiene, 2-phenyl-1,3-butadiene, 2-phenyl-1,3-pentadiene, 3-phenyl-1,3-pentadiene, 2,3-dimethyl-1,3- Pentadiene, 4-methyl-1,3-pentadiene, 2-hexyl-1,3-butadiene, 3-methyl-1,3-hexadiene, 2-benzyl-1,3-butadiene, 2-p-tolyl-1, 3-butadiene or a mixture thereof can be used. Among these, 1,3-butadiene and isoprene are preferable from the viewpoint of economy. From the viewpoint of peel strength, 1,3-butadiene is more preferable. In the present embodiment, one kind or two or more kinds of conjugated diene units can be used. The type of the conjugated diene unit of the component (A) may be the same as or different from the conjugated diene unit of the component (B).

  (Ii) It does not specifically limit as a vinyl aromatic unit, A well-known thing can be used. Examples thereof include styrene, o-methylstyrene, p-methylstyrene, p-tert-butylstyrene, 1,3-dimethylstyrene, α-methylstyrene, vinylnaphthalene, vinylanthracene and the like. Among these, styrene is preferable from the viewpoint of economy. In the present embodiment, one kind or two or more kinds of vinyl aromatic units can be used. The type of the vinyl aromatic unit of component (A) may be the same as or different from the vinyl aromatic unit of component (B).

  In the present embodiment, at least one tan δ peak temperature of the component (A) is −15 ° C. or higher and lower than 15 ° C., and at least one tan δ peak temperature of the component (B) is 15 ° C. or higher. Thereby, excellent properties can be imparted in all of low-temperature curability, low rebound resilience (impact absorbability), peel strength, compression set, and weight reduction.

From the viewpoint of low-temperature curability and compression set resistance, at least one of the tan δ peak temperatures of the component (A) is preferably −5 ° C. or higher and lower than 15 ° C., more preferably 3 ° C. or higher and lower than 15 ° C. More preferably, the temperature is more than 15 ° C. and more preferably less than 15 ° C.
From the viewpoint of low rebound resilience and weight reduction, it is preferable that at least one of the tan δ peak temperatures of the component (B) is 15 ° C. or higher and 35 ° C. or lower. A more preferred lower limit is 19 ° C. or more, a more preferred upper limit is 30 ° C. or less, and a still more preferred lower limit is 25 ° C. or less.

  The tan δ peak temperatures of the components (A) and (B) can be determined by dynamic viscoelasticity measurement (1 Hz). More specifically, the dynamic viscoelasticity data is obtained by using a torsion type geometry of a rheometer device (for example, “ARES” (manufactured by TA Instruments Inc.), an effective measurement length is 25 mm, Strain 0.5%, frequency 1 Hz, from −50 ° C. to 50 ° C., and a temperature increase rate of 3 ° C./min. The peak temperature can be determined by, for example, “RSI Orchestrator” (manufactured by TI Instruments Inc.).

In this embodiment, the control of the tan δ value peak temperature and the peak tan δ curve shape of the component (A) and the component (B) is, for example,
(1) controlling the vinyl content of the conjugated diene in component (A) and / or component (B),
(2) including a copolymer block of a conjugated diene and a vinyl aromatic compound,
(3) Inclining the concentration of vinyl aromatic units in the copolymer to make it tapered, stepped, concave or convex, etc.
(4) Increasing the molecular weight distribution of a block mainly composed of vinyl fragrance units;
(5) controlling the molecular weight and content of the block mainly composed of vinyl aromatic units;
(6) making a copolymer block containing two or more kinds of conjugated diene units;
(7) It can be carried out by at least one of controlling the amount of double bonds in the copolymer.

  In the present embodiment, the total content of (A) component and (B) component ((A + B) / (A + B + C)) with respect to the total of (A) component, (B) component, and (C) component is 40 to 90% by mass. By setting the content to 40% by mass or more, excellent low rebound resilience can be obtained. By setting the content to 90% by mass or less, low temperature curability, peel strength, and compression set resistance can be improved. A more preferred lower limit is 45% by mass or more, and even more preferred is 65% by mass or more. The upper limit value is more preferably 80% by mass or less, and further preferably 75% by mass or less.

  The total amount of the component (A), the component (B), and the component (C) in the crosslinking composition of the present embodiment is not particularly limited, is preferably 60% by mass or more, more preferably 70% by mass or more, and 80 More preferably, it is more than mass%. By setting it as this content, it can be made excellent in low repulsion, peel strength and compression set.

  Content of (A) component with respect to the sum total of (A) component, (B) component, and (C) component is not specifically limited, 10 mass% or more from a viewpoint of low-temperature curability, peel strength, and compression set resistance From the viewpoint of low rebound resilience, it is preferably 85% by mass or less. More preferably, it is 20-70 mass%, More preferably, it is 30-65 mass% or less, More preferably, it is 50-60 mass%.

  The content of the component (B) relative to the sum of the components (A), (B), and (C) is not particularly limited, and is preferably 5% by mass or more from the viewpoint of low rebound resilience, and is resistant to low-temperature curability and resistance. 65 mass% or less is preferable from a viewpoint of compression set. More preferably, it is 15-50 mass%, More preferably, it is 15-30 mass%.

  Content of (C) component with respect to the sum total of (A) component, (B) component, and (C) component is not specifically limited, From the viewpoint of peeling strength, low-temperature curability, and weight reduction, it is 10 mass% or more. Preferably, 60 mass% or less is preferable from the viewpoint of low resilience and flexibility. More preferably, it is 20-55 mass% or less, More preferably, it is 20-45 mass% or less.

  In this embodiment, the relationship between the content of the component (A) and the content of the component (B) is not particularly limited, and the content of the component (A) is (B) from the viewpoint of low temperature curability and peel strength. It is preferable that the content is larger than the content of components (content of component (A)> content of component (B)).

  Regarding the component (A) and the component (B), the hydrogenation rate of the conjugated diene unit in the hydrogenated copolymer is not particularly limited, and is 10 for the total unsaturated bonds of the conjugated diene before hydrogenation, respectively. -70 mol% is preferable, 15-50 mol% is more preferable, and 20-40 mol% is still more preferable. By making the hydrogenation rates of the component (A) and the component (B) within such ranges, the peel strength and compression set resistance can be made excellent.

  In this embodiment, the hydrogenation rate in the hydrogenated copolymer can be measured using a nuclear magnetic resonance apparatus (NMR).

About (A) component and (B) component, it is preferable to have 1 or more polymer blocks which have (ii) vinyl aromatic units as a main component in a copolymer from a viewpoint of manufacturability and peeling strength.
From the viewpoint of peel strength, the hydrogenated copolymer preferably has (ii) a polymer block mainly composed of vinyl aromatic units in the component (A) and / or the component (B).

  Regarding the component (A) and the component (B), the total amount of the polymer block body mainly composed of (ii) vinyl aromatic units in the hydrogenated copolymer is not particularly limited, and is 5 from the viewpoint of manufacturability and peel strength. The mass is preferably at least 40% by mass, from the viewpoint of flexibility. More preferably, it is 10-30 mass%, More preferably, it is 12-25 mass%.

Here, the content of the vinyl aromatic compound polymer block in the hydrogenated copolymer is determined by a method of oxidatively decomposing the copolymer before hydrogenation with tert-butyl hydroperoxide using osmium tetroxide as a catalyst (I.C. M. KOLTHOFF, et al., J. Polym. Sci. 1, 429 (1946), hereinafter also referred to as “osmotic tetroxide method”.
Using the weight of the vinyl aromatic compound polymer block obtained by the osmium tetroxide method (however, the vinyl aromatic compound polymer having an average polymerization degree of 30 or less is excluded), it is defined by the following formula: The

  Content (mass%) of vinyl aromatic compound polymer block = (mass of vinyl aromatic compound block in copolymer before hydrogenation / mass of copolymer before hydrogenation) × 100

  In this embodiment, the molecular chain structure of the component (A) and the component (B) is not limited. From the viewpoint of manufacturability and peel strength, the component (A) and / or the component (B) can be obtained from sequential polymerization. A chain structure is preferred.

  From the viewpoints of low-temperature curability, low rebound resilience (impact absorbability), peel strength, compression set resistance and weight reduction, the component (A) and / or the component (B) is a heavy component mainly composed of vinyl aromatic units. It is preferable to include a coalescence block and a hydrogenated copolymer block mainly composed of a conjugated diene unit and a vinyl aromatic unit.

  In (A) component and (B) component, the content ratio of (ii) vinyl aromatic unit in a copolymer block is not specifically limited, It is 35-65 mass% with respect to the total amount of a hydrogenated copolymer block. Is preferred.

  In the component (A) and the component (B), the distribution of the vinyl aromatic unit in the hydrogenated copolymer block mainly composed of the conjugated diene unit and the vinyl aromatic unit is not particularly limited and is uniformly distributed. Alternatively, it may be a distribution in which a tapered shape, a staircase shape, a concave shape or a convex shape is inclined.

  Furthermore, in this embodiment, from the viewpoint of low-temperature curing resistance and low rebound resilience, the component (A) and / or the component (B) are different in (ii) vinyl aromatic unit content, (i) conjugated dienes It is preferable that two or more hydrogenated copolymer blocks comprising units and (ii) vinyl aromatic units are contained in the component. Thereby, it can be set as the outstanding low-temperature curability and low rebound resilience.

  Regarding the component (A) and the component (B), the microstructure (ratio of cis, trans, vinyl) of the conjugated diene portion in the copolymer before hydrogenation is not particularly limited, and is arbitrary depending on the use of a polar compound described later. Can be changed to

  The vinyl bond content in the conjugated diene before hydrogenation is not particularly limited, and is preferably 5% or more from the viewpoint of manufacturability and 75% or less from the viewpoint of mechanical strength. The vinyl bond content is more preferably 10 to 50%, further preferably 15 to 40%, and still more preferably 15% or more and less than 30%.

In the component (A) and the component (B), the distribution of vinyl content in each molecule is not particularly limited, and the vinyl content may vary.
“Vinyl bond amount” means 1,2-bond of conjugated diene units before hydrogenation, or 1,2-bond of 3,4-bond and 1,4-bond. And the proportion of those incorporated by 3,4-bonds.

  In this embodiment, the amount of vinyl bonds based on the conjugated diene in the copolymer can be determined from a nuclear magnetic resonance apparatus (NMR).

  In (A) component and (B) component, the weight average molecular weight of each hydrogenated copolymer is not specifically limited, Mechanical strength, such as tensile strength at the time of setting it as a crosslinked foam, peeling strength, compression-resistant permanent 70,000 or more is preferable from the viewpoint of distortion, and 500,000 or less is preferable from the viewpoint of molding processability. 80,000 to 450,000 are more preferable, and 100,000 to 400,000 are more preferable.

  In the component (A) and the component (B), the molecular weight distribution of the hydrogenated copolymer is not particularly limited and is preferably 1.01 to 6.00, and 1.03 to 5 from the viewpoint of molding processability. 0.00 is more preferable, and 1.03-2.00 is even more preferable.

  In this embodiment, the weight average molecular weight and molecular weight distribution of the copolymer are measured by gel permeation chromatography (for example, GPC apparatus: LC-10 (manufactured by Shimadzu Corporation), column: TSKgelGMHXL (4.6 mmID × 30 cm) , Solvent: tetrahydrofuran), and can be determined from the molecular weight in terms of polystyrene.

In this embodiment, the manufacturing method of the copolymer used as (A) component and (B) component is not specifically limited, It can obtain by a well-known method. For example, it can be obtained by anionic living polymerization using an initiator such as an organic alkali metal compound in a hydrocarbon solvent.
It does not specifically limit as a hydrocarbon solvent, For example, aliphatic hydrocarbons, such as n-butane, isobutane, n-pentane, n-hexane, n-heptane, n-octane; cyclohexane, cycloheptane, methylcycloheptane And alicyclic hydrocarbons such as aromatic hydrocarbons such as benzene, toluene, xylene, and ethylbenzene.

  The initiator is not particularly limited, and is generally an aliphatic hydrocarbon alkali metal compound, an aromatic hydrocarbon alkali metal compound known to have anionic polymerization activity for a conjugated diene compound and a vinyl aromatic compound, An organic amino alkali metal compound or the like can be used. Examples of the alkali metal include lithium, sodium, and potassium.

  The organic alkali metal compound is not particularly limited, and is preferably an aliphatic and aromatic hydrocarbon lithium compound having 1 to 20 carbon atoms, a compound containing one lithium in one molecule, and a plurality of compounds in one molecule. More preferred are dilithium compounds, trilithium compounds, and tetralithium compounds containing lithium. Specifically, n-propyllithium, n-butyllithium, sec-butyllithium, tert-butyllithium, n-pentyllithium, n-hexyllithium, benzyllithium, phenyllithium, tolyllithium, diisopropenylbenzene and sec- A reaction product of butyllithium, a reaction product of divinylbenzene, sec-butyllithium, and 1,3-butadiene can be used.

The hydrogenated product can be obtained, for example, by hydrogenating the copolymer obtained above. The hydrogenation catalyst is not particularly limited, and known ones can be used, and examples thereof include the following.
(1) A supported heterogeneous hydrogenation catalyst in which a metal such as Ni, Pt, Pd, or Ru is supported on carbon, silica, alumina, diatomaceous earth, or the like,
(2) a so-called Ziegler type hydrogenation catalyst using an organic acid salt such as Ni, Co, Fe, Cr or a transition metal salt such as acetylacetone salt and a reducing agent such as organic aluminum,
(3) A homogeneous hydrogenation catalyst such as a so-called organometallic complex such as an organometallic compound such as Ti, Ru, Rh, or Zr is used.

  As specific hydrogenation catalysts, JP-B-42-8704, JP-B-43-6636, JP-B-63-4841, JP-B-1-37970, JP-B-1-53851, JP-B The hydrogenation catalyst described in 2-9041 gazette can be used.

Preferred hydrogenation catalysts include mixtures with titanocene compounds and / or reducing organometallic compounds.
As the titanocene compound, compounds described in JP-A-8-109219 can be used. Specifically, it has at least one ligand having a (substituted) cyclopentadienyl skeleton, indenyl skeleton or fluorenyl skeleton such as biscyclopentadienyl titanium dichloride and monopentamethylcyclopentadienyl titanium trichloride. Compounds.
Examples of the reducing organometallic compound include organic alkali metal compounds such as organolithium, organomagnesium compounds, organoaluminum compounds, organoboron compounds, and organozinc compounds.

  In this embodiment, if necessary, an atomic group having at least one functional group selected from a hydroxyl group, an epoxy group, an amino group, a silanol group, and an alkoxysilane group is bonded to the component (A) or the component (B). May be.

  In the present embodiment, (C) the ethylene copolymer having a Shore A hardness of 70 degrees or more may be contained in an amount of 10 to 60% by mass, preferably 10 to 45% by mass. As long as it is within the scope of the present embodiment, an ethylene copolymer having a Shore A hardness of less than 70 degrees may be contained as a component other than the component (C).

  The component (C) preferably contains an ethylene copolymer having a Shore A hardness of 75 degrees or more, more preferably an ethylene copolymer of 80 degrees or more, from the viewpoint of peel strength and weight reduction, and 83 degrees. The above ethylene copolymers are more preferable.

  In this embodiment, the Shore A hardness is measured according to ASTM-D2240, and can be measured using, for example, an Asker C type durometer hardness meter.

  Component (C) is a copolymer containing ethylene as a structural unit. It does not specifically limit as an ethylene-type copolymer, A well-known thing can be used. For example, polyethylene (PE) which is a polymer of ethylene, ethylene / vinyl acetate copolymer (EVA) obtained by copolymerizing ethylene and vinyl acetate, and ethylene and an α-olefin having 3 to 10 carbon atoms An ethylene / α-olefin copolymer, which is a low-crystalline random copolymer comprising a block copolymer containing ethylene and α-olefin (for example, a hard segment is crystalline polyethylene and a soft segment is ethylene-octene) Multiblock copolymer comprising random blocks). These ethylene copolymers can be used alone or in combination of two or more.

  In this embodiment, when using polyethylene, the kind is not limited and a well-known thing can be used. Examples include high density polyethylene, ultra high molecular weight high density polyethylene, low density polyethylene, linear low density polyethylene, and ultra low density polyethylene.

In the present embodiment, it may be three or more types of copolymers composed of ethylene and two or more types of compounds other than ethylene. For example, a copolymer (terpolymer) composed of ethylene and two α-olefins can be used.
In order to further improve the mechanical strength of the composition for crosslinking and foaming of the present embodiment, the component (C) is preferably an ethylene / α-olefin copolymer.
When an adhesive is used to bond the crosslinking foaming composition of the present embodiment to other materials, particularly when an aqueous adhesive is used, an ethylene / vinyl acetate copolymer (EVA) is used in combination. It is preferable to do.
An ethylene / α-olefin copolymer and an ethylene / vinyl acetate copolymer (EVA) may be used in combination.

The ethylene / α-olefin copolymer that can be used in the present embodiment is not particularly limited, and commercially available products can be used. For example, Tuffmer (made by Mitsui Chemicals), Engage (made by Dow), Infuse (made by Dow), etc. are mentioned.
The ethylene / vinyl acetate copolymer (EVA) that can be used in the present embodiment is not particularly limited, and a known one can be used. For example, EVAFLEX (manufactured by Dupont), LEVAPREN (manufactured by LANXESS) and the like can be mentioned.

  The content of (C) with respect to the sum of the (A) component, the (B) component, and the (C) component is not particularly limited, and is preferably 10% by mass or more from the viewpoint of peel strength, low temperature curability, and weight reduction. From the viewpoint of low rebound resilience and flexibility, 60% by mass or less is preferable. More preferably, it is 20 mass% or more and 55 mass% or less, More preferably, it is 20 mass% or more and 45 mass% or less.

The composition for cross-linking and foaming of the present embodiment contains (D) a cross-linking agent.
In the present embodiment, the crosslinking agent that can be used as the component (D) is not particularly limited, and known ones can be used. Examples thereof include organic peroxides, sulfur compounds, phenol resin compounds, quinoid compounds, bismaleimide compounds, isocyanate compounds, thiuram compounds, morpholine disulfides, and hydrosilicon compounds. Among these, an organic peroxide is preferable. Examples of the organic peroxide include dicumyl peroxide, di-t-butyl peroxide, 2,5-dimethyl-2,5-di- (t-butylperoxy) hexane, 2,5-dimethyl-2,5- Di- (t-butylperoxy) hexyne-3, 1,3-bis (t-butylperoxyisopropyl) benzene, 1,1-bis (t-butylperoxy) -3,3,5-trimethylcyclohexane, n-butyl -4,4-bis (t-butylperoxy) valerate, benzoyl peroxide, p-chlorobenzoyl peroxide, 2,4-dichlorobenzoyl peroxide, t-butylperoxybenzoate, t-butylperbenzoate, t-butylperoxyisopropyl carbonate, Diacetyl peroxide, lauroyl peroxide, t-butyl Torque mill peroxide and the like.

  In the present embodiment, the content of the component (D) in the crosslinked foaming composition is not particularly limited, and is preferably 0.05% by mass or more from the viewpoint of mechanical strength, compression set resistance and foamability, and is flexible. From the viewpoint of mechanical strength, it is preferably 3% by mass or less. More preferably, they are 0.2 mass% or more and 1.5 mass% or less, More preferably, they are 0.3 mass% or more and 1.0 mass% or less.

The composition for cross-linking and foaming of the present embodiment contains (E) a foaming agent.
The foaming agent that can be used as the component (E) in the present embodiment is not particularly limited, and known ones can be used. For example, azodicarbonamide (ADCA), N, N′-dinitrosopentamethylenetetramine, 4,4′-oxybis (benzenesulfonyl hydrazide), diphenylsulfone-3,3′-disulfonyl hydrazide, p-toluenesulfonyl semicarbazide, Preference is given to organic pyrolytic foaming agents such as trihydrazinotriazine, and inorganic pyrolytic foaming agents such as sodium hydrogen carbonate, sodium carbonate, ammonium hydrogen carbonate and ammonium carbonate. Among these, azodicarbonamide (ADCA) and sodium hydrogen carbonate are more preferable from the viewpoint of peel strength and compression set.

  The content of the component (E) in the composition for crosslinking and foaming is not particularly limited, and is preferably 0.2% by mass or more from the viewpoint of weight reduction, and 15% by mass or less from the viewpoint of peel strength and compression set resistance. preferable. More preferably, it is 0.3 mass% or more and 10 mass% or less, More preferably, it is 0.5 mass% or more and 10 mass% or less, More preferably, it is 0.8 mass% or more and 5.0 mass% or less. is there.

In this embodiment, it is preferable to contain (F) an inorganic filler. By containing an inorganic filler, foamability and shape stability can be further improved.
The content of the component (F) is not particularly limited, and is preferably 20% by mass or less, more preferably 10% by mass or less, and still more preferably 6% by mass or less from the viewpoints of weight reduction and peel strength.

  The inorganic filler that can be used as the component (F) is not particularly limited as long as it is generally used for blending thermoplastic resins and rubber-like polymers, and known ones can be used. For example, silica, talc, mica, calcium silicate, hydrotalcite, kaolin, diatomaceous earth, graphite, calcium carbonate, magnesium carbonate, magnesium hydroxide, aluminum hydroxide, calcium sulfate, barium sulfate and other inorganic fillers, carbon black, etc. Is mentioned.

  If necessary, the composition for crosslinking and foaming of the present embodiment may contain other components as long as the purpose of the present embodiment is not impaired. The other components that can be contained in the present embodiment are not particularly limited. For example, other polymers, crosslinking aids, heat stabilizers, weathering stabilizers, flame retardants, hydrochloric acid absorbents, pigments, organic metals Various additives, such as a compound, are mentioned.

  As another polymer, for example, butyl rubber or brominated butyl rubber can be used from the viewpoint of low rebound resilience, low temperature curability, or processability during production.

  Examples of the crosslinking aid include sulfur, p-quinonedioxime, p, p′-dibenzoylquinonedioxime, N-methyl-N-4-dinitrosoaniline, nitrosobenzene, diphenylguanidine, and trimethylolpropane-N. , N′-m-phenylenedimaleimide and other peroxy crosslinking aids; divinylbenzene, triallyl cyanurate (TAC), triallyl isocyanurate (TAIC); ethylene glycol dimethacrylate, diethylene glycol dimethacrylate, polyethylene glycol dimethacrylate, Examples thereof include multifunctional methacrylate monomers such as trimethylolpropane trimethacrylate and allyl methacrylate; and multifunctional vinyl monomers such as vinyl butyrate and vinyl stearate. Among these, triallyl cyanurate (TAC) and triallyl isocyanurate (TAIC) are preferable from the viewpoint of peel strength.

  From the viewpoint of peel strength and compression set resistance, an organometallic compound containing a metal selected from Groups 2 to 12 of the periodic table may be added. Specifically, zinc diacrylate (ZDA) or zinc dimethacrylate (ZDMA) is preferable, and by adding these organometallic compounds, the gel fraction of the resulting crosslinked foam is increased, and the foamed cells are made finer. And uniform.

  If necessary, a softener may be added to improve processability. The softening agent is not particularly limited, and a known softening agent can be used. Preferably, it is a mineral oil or a liquid or low molecular weight synthetic softening agent. Among them, a mineral oil-based rubber softening agent called process oil or extender oil used for softening, increasing volume and improving processability of rubber is preferable.

The mineral oil rubber softener is a mixture of aromatic rings, naphthene rings and paraffin chains. A paraffin chain having 50% or more of carbon atoms in the total carbon is called paraffinic. A naphthene ring having 30 to 45% of all carbon atoms is called a naphthene group. Those having an aromatic carbon number exceeding 30% of the total carbon are called aromatic. Among these, naphthenic and / or paraffinic softeners are more preferable.
Synthetic softeners include, for example, polybutene, low molecular weight polybutadiene liquid paraffin, and the like, but the mineral oil rubber softener is more preferable.

  The compounding amount of the softening agent in the present embodiment is not particularly limited, and is preferably 0 to 100 parts by mass, more preferably 0 to 20 parts by mass with respect to 100 parts by mass of the hydrogenated copolymer.

  In this embodiment, in addition, a lubricant such as stearic acid, behenic acid, zinc stearate, calcium stearate, magnesium stearate, ethylene bisstearamide, a release agent, a plasticizer such as organic polysiloxane, mineral oil, Antioxidants such as hindered phenol antioxidants, phosphorus, sulfur and amine heat stabilizers, hindered amine light stabilizers, benzotriazole ultraviolet absorbers, flame retardants, antistatic agents, organic fibers, glass fibers , Reinforcing agents such as carbon fiber and metal whisker, and coloring agents such as titanium oxide, iron oxide, and carbon black can be used. For example, it is described in “Handbook Rubber / Plastic Compounding Chemicals” (edited by Rubber Digest Co., Ltd.). May be used as appropriate.

The composition for crosslinking and foaming according to the present embodiment is a temperature at which (D) the crosslinking agent and (E) the foaming agent are not decomposed using a kneader such as a Henschel mixer, a Banbury mixer, a roll, and an extruder at the above-described ratio. Can be prepared by melt mixing. In the present embodiment, the mixing method is not particularly limited. For example, after the components other than the component (D) and the component (E) are mixed in advance, the component (D) and the component (E) may be added and mixed. Good.
Moreover, the shape of the composition for crosslinked foaming of this embodiment is not specifically limited, It can shape | mold to a desired shape suitably. For example, it can be in the form of a pellet, a sheet (sometimes referred to as a film), a strand, or a chip.

  Specifically, the composition for cross-linking and foaming of the present embodiment can be prepared as a pellet by using a granulator or the like. Or the pellet of the composition for crosslinked foaming obtained in this way can be made into a sheet form by preparing using an extruder or a calendar molding machine. In addition, after kneading each component of the composition for cross-linking and foaming with a Brabender, etc., a method of forming into a sheet shape with a calender roll, a method of forming into a sheet with a press molding machine, kneading with an extruder, and then a T-die Alternatively, a method of forming a sheet through an annular die can be used. Thereby, an uncrosslinked and unfoamed foamable sheet can be prepared.

  By crosslinking and foaming the composition for crosslinking and foaming of the present embodiment, a crosslinked foam can be obtained. The cross-linked foam of this embodiment is excellent in low-temperature curing resistance, low rebound resilience (impact absorbability), peel strength, compression set resistance, and weight reduction.

  In the present embodiment, the crosslinked foamed composition can be crosslinked and foamed by press molding or injection molding. For example, it is suitable for injection-crosslinking foam molding into a predetermined mold using a pelletized composition for cross-linking foaming.

Here, an example in which the crosslinked foaming composition of the present embodiment is formed into a sheet will be described.
The composition for crosslinking and foaming of the present embodiment formed into a sheet by the above method was cut into a size in the range of 1.0 to 1.2 times the volume of the mold, and maintained at 120 to 200 ° C. Insert into the mold. The mold clamping pressure is 30 to 300 kgf / cm ² , and the composition is obtained by pressurizing and melting under the conditions of a holding time of 10 to 90 minutes, performing a crosslinking reaction and decomposing the foaming agent, and then opening the mold. A primary cross-linked foam can be produced by foaming.

  The shape of the cross-linking foaming mold for producing the primary cross-linked foam is not particularly limited, but a mold having such a shape as to obtain a sheet is used. The cross-linking foaming mold preferably has a completely sealed structure so that gas generated when the resin is melted or when the foaming agent is decomposed is not released. As the mold, a mold having a taper on the inner surface is preferable from the viewpoint of resin releasability.

In this embodiment, you may provide a predetermined shape by compression-molding a primary crosslinked foam as needed. The compression molding conditions at this time are not particularly limited. For example, the mold temperature is 120 to 200 ° C., the clamping pressure is 30 to 300 kgf / cm ² , the compression time is 5 to 60 minutes, and the compression ratio is 1.1 to 1.1. The range is 3.0.

  In the present embodiment, the foamed foamed product can be formed by molding the crosslinked foaming composition into various shapes and sizes in addition to the sheet shape. In the present embodiment, the shape and size of the obtained foamed molded article and the crosslinked foaming composition constituting the foamed molded article are not particularly limited, and can be molded into various shapes other than the sheet shape.

  The cross-linked foam of this embodiment can be used as a sheet (sometimes referred to as a film), injection molded products of various shapes, hollow molded products, compressed air molded products, vacuum molded products, extrusion molded products, and the like.

  Specifically, the cross-linked foam of the present embodiment is a flooring material such as an apartment, a wall material, a ceiling, a window frame, a shutter, a door, a soundproof wall, a roof material, a vibration control device, a new vibration isolation surface device, a damper, Construction materials such as plumbing pipes such as water supply and drainage pipes; Damping films, anti-vibration sheets, anti-tip sheets such as anti-vibration mats, mats and films; record support turntables, CD players, microphone holders, speaker cone edges, It can be used as a member capable of reducing unpleasant noise and resonance noise such as an acoustic device such as a radio cassette or mini-disc; an OA device such as a copy machine, a FAX, or a printer; an information transmission device such as a mobile phone or a mobile PC.

  Further, it can be used as a member for reducing unpleasant noise and resonance generated by driving motors of household electric appliances such as TV, refrigerator, air conditioner outdoor unit and sound in a duct, noise in a car engine room and a car. Among them, because of its high shock absorption, it is suitable for shock-absorbing foams such as shoes, fall prevention sheets, mats and films, and also suitable as a soundproof sheet for piping such as water supply pipes and drain pipes. is there.

  Among these, the crosslinked foam of the present embodiment can be suitably used as a footwear material, and can be more suitably used as a midsole or insole among footwear materials.

  Midsole, insole, etc. are not only lightweight as soles used for shoe soles, but also need to have low rebound resilience in order to alleviate the impact at the time of landing, and are resistant to the shoe soles from falling. It is required to be excellent in compression set. Furthermore, when using shoes in cold districts, low-temperature curability is also required. At the time of manufacture, in order to obtain a desired shape, it is also desired that molding is easy. From such a viewpoint, the crosslinked foam of the present embodiment is suitable because it is excellent in low-temperature curability, low rebound resilience (impact absorbability), peel strength, compression set, and weight reduction.

The midsole for shoes of this embodiment is used by bonding an outsole or an upper after molding, for example. The insole (insole) for shoes of this embodiment is used, for example, by inserting the shoe into the shoe after manufacturing the shoe.
It can be set as the laminated body containing the crosslinked foam of this embodiment, and the member laminated | stacked with this crosslinked foam. Thus, in this embodiment, it can be set as the laminated body which laminated | stacked the crosslinked foam and various materials. Thereby, it can be used according to various uses. The member to be laminated is not particularly limited, and a known member can be used.
In the present embodiment, the method for stacking is not particularly limited, and a known method can be used. For example, pasting with an adhesive, forming and adhering in a mold at the same time, heating after cross-linking, crosslinking and adhering, and the like can be mentioned.

The present embodiment will be described more specifically by the following examples, but the present embodiment is not limited to these examples.

(I) Measurement of properties and physical properties of polymer The properties and physical properties of the polymer were measured as follows.

(1) Styrene content, vinyl bond amount of conjugated diene, hydrogenation rate of double bond based on conjugated diene compound vinyl aromatic monomer unit, 1,4-bond unit and 1,2-bond unit of butadiene, The amount of ethylene units or butylene units was measured by nuclear magnetic resonance spectrum analysis (NMR).
The measuring instrument is a nuclear magnetic resonance apparatus “JNM-LA400” (manufactured by JEOL), deuterated chloroform is used as a solvent, sample concentration is 50 mg / mL, observation frequency is 400 MHz, tetramethylsilane (TMS) as a chemical shift standard, Measurement was performed at a pulse delay of 2.904 seconds, a scan count of 64 times, a pulse width of 45 degrees, and a measurement temperature of 26 ° C.

(2) Polystyrene block content Using a copolymer before hydrogenation, M.M. Kolthoff, et al. , J .; Polym. Sci. 1, 429 (1946). For the decomposition of the copolymer, a 0.1 g / 125 mL tertiary butanol solution of an osmic acid solution was used.

(3) Weight average molecular weight and molecular weight distribution The weight average molecular weight and molecular weight distribution of the copolymer were measured by gel permeation chromatography (GPC).
The measuring instrument was “LC-10” (manufactured by Shimadzu Corporation, column: TSKgelGMHXL (4.6 mm ID × 30 cm), two: solvent: tetrahydrofuran), and the molecular weight was determined from the polystyrene-equivalent molecular weight of commercially available standard polystyrene.
The molecular weight distribution is a ratio (M _w / M _n ) of the obtained weight average molecular weight (M _w ) and number average molecular weight (M _n ).

(4) Coupling rate The molecular weight distribution of GPC measurement was determined using the peak area before coupling and the peak area after coupling.

(5) Tan δ Peak Temperature Each tan δ peak temperature of the component (A) and the component (B) was determined by dynamic viscoelasticity measurement (1 Hz). Specifically, the dynamic viscoelasticity data is obtained by cutting a sample into a size of 10 mm in width and 35 mm in length, and using a twist type geometry of a rheometer device “ARES” (manufactured by TI Instruments Inc.). The sample was set, and the effective measurement length was 25 mm, the strain was 0.5%, the frequency was 1 Hz, and the value obtained from −50 ° C. to 50 ° C. at a temperature rising rate of 3 ° C./min. The peak temperature was determined by automatic measurement of “RSI Orchestrator” (manufactured by TA Instruments Inc.).

(II) Preparation of hydrogenated copolymer (1) Preparation of hydrogenation catalyst Hydrogenation catalyst I used for the hydrogenation reaction was prepared by the following method.
Charge 1 liter of dried and purified cyclohexane to a nitrogen-substituted reaction vessel, add 100 mmol of bis (η5-cyclopentadienyl) titanium dichloride, and add an n-hexane solution containing 200 mmol of trimethylaluminum while stirring sufficiently. And allowed to react at room temperature for 3 days.

(2) Production method of hydrogenated copolymer <Polymer 1>
A block copolymer was prepared by the following method using a stirrer having an internal volume of 10 L and a jacketed tank reactor.
After a predetermined amount of cyclohexane was charged into the reactor and adjusted to 70 ° C., the amount of n-butyllithium was 0.06 with respect to the total of all monomers (total amount of butadiene monomer and styrene monomer charged into the reactor). It added from the bottom part of the reactor so that it might become a mass part. Further, a cyclohexane solution of N, N, N ′, N′-tetramethylethylenediamine was added so that the amount of N, N, N ′, N′-tetramethylethylenediamine was 0.4 mol with respect to 1 mol of n-butyllithium. Added. Then, the cyclohexane solution containing 10 mass parts of styrene of the 1st step was supplied as a monomer in 5 minutes, and the reactor internal temperature was adjusted to 70 degreeC. After stopping the supply, the reaction was carried out for 15 minutes while adjusting the temperature in the reactor to 70 ° C.
Next, a cyclohexane solution containing 17 parts by mass of butadiene in the second step and 10 parts by mass of styrene is continuously supplied to the reactor at a constant rate over 20 minutes, and the temperature in the reactor is adjusted to 70 to 80 ° C. It was adjusted. After stopping the supply, the reaction was carried out for 5 minutes while adjusting the temperature in the reactor to 70 to 80 ° C.
Further, a cyclohexane solution containing 20 parts by mass of butadiene in the third step and 35 parts by mass of styrene is continuously supplied to the reactor at a constant rate over 40 minutes, and the temperature in the reactor during that period is increased to 70 to 80 ° C. It adjusted so that it might become. After stopping the supply, the reaction was carried out for 10 minutes while adjusting the temperature in the reactor to 70 to 80 ° C.
Finally, a cyclohexane solution containing 8 parts by mass of styrene in the 4th step was supplied over 5 minutes, and the temperature in the reactor was adjusted to 70 ° C. After stopping the supply, the reaction was carried out for 15 minutes while adjusting the temperature in the reactor to 70 ° C.

  After completion of the polymerization, a cyclohexane solution of methanol was added so that the amount of methanol with respect to 1 mol of n-butyllithium was 1 equivalent to complete the polymerization reaction. When the copolymer obtained by polymerization was analyzed, the styrene content was 63% by mass, the polystyrene block content was 21% by mass, the vinyl bond content of the butadiene part was 21%, the weight average molecular weight was 160,000, and the molecular weight distribution was 1.05.

  To the copolymer obtained by batch coupling polymerization, 100 ppm of the above hydrogenation catalyst I in terms of titanium is added per 100 parts by mass of the non-hydrogenated copolymer, and the hydrogenation reaction is carried out at a hydrogen pressure of 0.7 MPa and a temperature of 65 ° C. went. After the reaction is completed, octadecyl-3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate is added as a stabilizer to 0.25 parts by mass with respect to 100 parts by mass of the polymer. 1) was obtained.

  The hydrogenation rate of polymer 1 was 36%, the melt flow rate (190 ° C., 2.16 kg) was 4 g / 10 min, and the tan δ peak temperature was 8 ° C.

<Polymer 2>
A block copolymer was prepared by the following method using a stirrer having an internal volume of 10 L and a jacketed tank reactor.
After a predetermined amount of cyclohexane was charged into the reactor and the temperature was adjusted to 70 ° C., the amount of n-butyllithium was 0. 0 with respect to the total of all monomers (total amount of butadiene monomer and styrene monomer charged into the reactor). It added from the bottom part of the reactor so that it might become 09 mass parts. Further, a cyclohexane solution of N, N, N ′, N′-tetramethylethylenediamine is added so that the amount of N, N, N ′, N′-tetramethylethylenediamine is 0.7 mol with respect to 1 mol of n-butyllithium. Added. Thereafter, a cyclohexane solution (monomer concentration: 24% by mass) containing 20 parts by mass of styrene as a monomer was supplied over 10 minutes, and the temperature in the reactor was adjusted to 70 ° C. After stopping the supply, the reaction was carried out for 15 minutes while adjusting the temperature in the reactor to 70 ° C.
Next, a cyclohexane solution (monomer concentration: 24% by mass) containing 33 parts by mass of butadiene and 47 parts by mass of styrene is continuously supplied to the reactor at a constant rate over 60 minutes, and the temperature in the reactor during that period is 70. It adjusted so that it might become ~ 80 degreeC. After stopping the supply, the reaction was carried out for 10 minutes while adjusting the temperature in the reactor to 70 ° C.
After completion of the polymerization, the cyclohexane solution of ethyl benzoate was added so that the amount of the bifunctional coupling agent ethyl benzoate was 0.5 equivalent to 1 mol of n-butyllithium, and the temperature inside the reactor was adjusted to 70 ° C. The reaction was allowed to proceed for 10 minutes.
When the copolymer obtained by batch coupling polymerization was analyzed, the styrene content was 67% by mass, the polystyrene block content was 20% by mass, the vinyl bond content of the butadiene part was 25% by mass, and the coupling rate was 50%. The weight average molecular weight was 190,000 and the molecular weight distribution was 1.7.

To the copolymer obtained by batch coupling polymerization, the above hydrogenation catalyst is added at 100 ppm in terms of titanium per 100 parts by mass of the non-hydrogenated copolymer, and a hydrogenation reaction is performed at a hydrogen pressure of 0.7 MPa and a temperature of 65 ° C. It was. After completion of the reaction, methanol was added, and then octadecyl-3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate as a stabilizer was added in an amount of 0.25 parts by mass with respect to 100 parts by mass of the polymer. A hydrogenated copolymer (Polymer 2) was obtained.
The hydrogenation rate of polymer 2 was 30%, the melt flow rate (190 ° C., 2.16 kg) was 4 g / 10 min, and the tan δ peak temperature was 19 ° C.

<Polymer 3>
A block copolymer was prepared by the following method using a stirrer having an internal volume of 10 liters and a jacketed tank reactor.
After a predetermined amount of cyclohexane was charged into the reactor and adjusted to a temperature of 60 ° C., the amount of n-butyllithium was 0. 0 with respect to the total of all monomers (total amount of butadiene monomer and styrene monomer charged into the reactor). It added from the bottom part of the reactor so that it might become 07 mass parts. Further, a cyclohexane solution of N, N, N ′, N′-tetramethylethylenediamine so that the amount of N, N, N ′, N′-tetramethylethylenediamine is 1.6 mol with respect to 1 mol of n-butyllithium. Was added. Thereafter, a cyclohexane solution containing 7 parts by mass of styrene as a monomer (monomer concentration: 24% by mass) was supplied for 10 minutes, and the temperature in the reactor was adjusted to 60 ° C. After stopping the supply, the reaction was carried out for 15 minutes while adjusting the temperature in the reactor to 60 ° C.
Subsequently, a cyclohexane solution containing 86 parts by mass of butadiene (monomer concentration: 24% by mass) is continuously supplied to the reactor at a constant rate over 100 minutes so that the temperature in the reactor becomes 60 to 70 ° C. Adjusted. After stopping the supply, the reaction was carried out for 10 minutes while adjusting the temperature in the reactor to 60 to 70 ° C.

Next, a cyclohexane solution containing 7 parts by mass of styrene (monomer concentration: 24% by mass) is supplied over 10 minutes, and the temperature in the reactor is adjusted to 60 to 70 ° C. during the period. The reaction was performed while adjusting the temperature in the reactor to 60 to 70 ° C. for 1 minute.
When the copolymer obtained by batch polymerization was analyzed, the styrene content was 14% by mass, the polystyrene block content was 14% by mass, the vinyl bond content in the butadiene portion was 75% by mass, the weight average molecular weight was 150,000, and the molecular weight. The distribution was 1.1.

After completion of the polymerization, the above hydrogenation catalyst is added to the copolymer obtained by batch polymerization at 100 ppm in terms of titanium per 100 parts by mass of the non-hydrogenated copolymer, and the hydrogenation reaction is performed at a hydrogen pressure of 0.7 MPa and a temperature of 65 ° C. Went. After completion of the reaction, methanol was added, and then octadecyl-3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate as a stabilizer was added in an amount of 0.25 parts by mass with respect to 100 parts by mass of the polymer. A hydrogenated copolymer (Polymer 3) was obtained.
Polymer 3 had a hydrogenation rate of 98%, a melt flow rate (230 ° C., 2.16 kg) of 3.0 g / 10 min, and a tan δ peak temperature of −19 ° C.

(III) Other composition / ethylene copolymer “ENGAGE8480” (manufactured by Dow, specific gravity: 0.902, Shore A hardness: 89 degrees, glass transition temperature: −31 ° C.)
Ethylene copolymer “ENGAGE8180” (Dow, specific gravity: 0.863, Shore A hardness: 63 degrees, glass transition temperature: −55 ° C.)
・ Foaming agent “Exceller AK-2” (manufactured by Eiwa Chemical Industry Co., Ltd., N, N′-dinitrosopentamethylenetetramine (DPT) / azodicarbonamide (ADCA))

(IV) Production of cross-linked foam Using a kneader as a melt kneader, the blended components in the first step shown in Table 1 were kneaded at a kneading temperature of 110 to 120 ° C and a kneading time of 15 minutes.
Next, using a two-roll open mill as a melt kneader, the kneaded product of the first step and each compounding component of the second step shown in Table 1 are kneaded at a kneading temperature of about 90 to 100 ° C. and a kneading time of 10 minutes. did.
Next, the kneaded product obtained using the compression molding machine is compressed at a temperature of 170 ° C. and a pressure of 150 kgf / cm ² for 15 minutes, and the mold is opened to foam the composition, thereby producing a primary crosslinked foamed body. did. After storing the primary foam for 24 hours at room temperature, it was held at 170 ° C. for 15 minutes at a pressure of 150 kgf / cm ² (compression ratio: 140% to 150%) for 10 minutes. And it cooled to room temperature with water cooling, the pressure was released | released, and the 1-cm-thick crosslinked foaming molded article was obtained. Crosslinked foamed molded articles were produced for Examples 1 to 4 and Comparative Examples 1 to 4, respectively, and their characteristics were measured.

(V) Measurement of characteristics of cross-linked foamed molded article (1) 22 ° C. Hardness Based on ASTM-D2240, the hardness of the cross-linked foam at 22 ° C. was measured using an Asker C type durometer hardness meter.
(2) Compression set A compression set test was performed in accordance with JIS-K6262, using the crosslinked foamed molded article of (IV). The measurement conditions were a temperature of 50 ° C., 50% compression, and 6 hours.

(3) Peel strength (IV) A cross-linked foamed molded product was used. After the cross-linked foam premium was cut to a width of 2 cm, a cut was made in the central portion of the thickness and peeled at a rate of 100 mm / min. The peel strength was determined from the following formula.

Peel strength = measured maximum peel strength / 2 (N / cm)

(4) Low-temperature curing resistance Based on ASTM-D2240, the hardness of the cross-linked foam at 22 ° C. and −5 ° C. was measured using an Asker C type durometer hardness meter, and the width of the hardness change was evaluated.
It is better that the hardness change is small, and 25 degrees or less is “◯”, and more than 25 degrees is “x”.

(5) Rebound resilience Using the cross-linked foamed molded article of (IV), steel balls (16.3 g) were dropped onto a cross-linked foam test piece. The rebound resilience was obtained from the following formula. The measurement temperature was 22 ° C.

Rebound resilience (%) = [H _R / H ₀ ] × 100
H ₀ = sphere fall height
H _R = The height at which the sphere repels

[Examples 1-4, Comparative Examples 1-4]
Examples 1-4 have a specific gravity of 0.31 or less, a 22 ° C. hardness (Shore A hardness) of 50 degrees, a compression set of 31% or less, and a peel strength of 30 N / cm or more. The low-temperature curability was all “◯” and the rebound resilience was 14 or less.
On the other hand, Comparative Examples 1 to 4 were inferior in at least one of specific gravity, 22 ° C. hardness (Shore A hardness), compression set, peel strength, low-temperature curability, and rebound resilience.
As described above, according to the present example, the composition for cross-linking and foaming of the present embodiment is a cross-linking foam having excellent low temperature curability, low rebound resilience (impact absorbability), peel strength, compression set resistance and weight reduction. It was shown that it could be with the body.

  The cross-linked foam of the present invention and the cross-linked foam obtained therefrom can be used in the form of sheets and molded products of various shapes. For example, it can be used in a wide range of fields as building materials for condominiums, various films, equipment devices such as acoustic equipment, OA equipment and mobile phones, and various members for home appliances. In particular, the cross-linked foam of the present invention is suitable as a footwear material, and can be particularly suitably used as a midsole or insole for shoes.

Claims (18)

(A) a hydrogenated copolymer of a copolymer mainly composed of a conjugated diene unit and a vinyl aromatic unit, wherein the tan δ peak temperature is −15 ° C. or higher and lower than 15 ° C .;
(B) a hydrogenated copolymer of a copolymer mainly comprising a conjugated diene unit and a vinyl aromatic unit, wherein the tan δ peak temperature is 15 ° C. or higher;
(C) 10 to 60% by mass of an ethylene copolymer having a Shore A hardness of 70 degrees or more;
(D) a crosslinking agent;
(E) a foaming agent,
The component (A) and / or the component (B) is a hydrogenated copolymer in which 10 to 70 mol% of unsaturated groups contained before hydrogenation are hydrogenated,
The composition for crosslinked foaming, wherein the total of the component (A) and the component (B) is 40 to 90% by mass relative to the total of the component (A), the component (B), and the component (C). The composition for crosslinked foaming according to claim 1, wherein the vinyl bond content in the conjugated diene before hydrogenation is 10 to 40%. (F) The composition for crosslinked foaming of Claim 1 or 2 which further contains an inorganic filler. In the crosslinked foaming composition,
Content of the said (D) component is 0.05-3 mass%,
Content of the said (E) component is 0.2-15 mass%,
The composition for crosslinked foaming according to any one of claims 1 to 3, wherein the content of the component (F) is 0 to 20% by mass. The composition for crosslinked foaming according to any one of claims 1 to 4 , wherein the Shore A hardness of the component (C) is 75 degrees or more. The composition for crosslinked foaming according to any one of claims 1 to 5 , wherein the component (C) is an ethylene / α-olefin copolymer. The composition for crosslinked foaming according to any one of claims 1 to 6 , wherein the content of the component (F) is 0 to 10% by mass relative to the total amount of the composition for crosslinked foaming. The composition for crosslinked foaming according to any one of claims 1 to 7 , wherein the content of the component (A) is larger than the content of the component (B).   The component (A) and / or the component (B) are a polymer block mainly composed of vinyl aromatic units, and a hydrogenated copolymer block mainly composed of vinyl aromatic units and conjugated diene units. The composition for crosslinked foaming as described in any one of Claims 1-8 containing.   The component (A) and / or the component (B) contains two or more hydrogenated copolymer blocks composed of conjugated diene units and vinyl aromatic units, each having a different content of vinyl aromatic units. The composition for crosslinked foaming according to any one of claims 1 to 9.   The composition for crosslinked foaming according to any one of claims 1 to 10, wherein at least one of the tan δ peak temperatures of the component (A) is -5 ° C or higher and lower than 15 ° C.   The composition for crosslinked foaming according to any one of claims 1 to 11, wherein at least one of the tan δ peak temperatures of the component (B) is 15 ° C or higher and 35 ° C or lower.   The composition for crosslinked foaming according to any one of claims 1 to 12, wherein the component (A) and / or the component (B) has a linear structure obtained by sequential polymerization. With respect to the sum of the component (A), the component (B) and the component (C),
The content (A / (A + B + C)) of the component (A) is 30 to 65% by mass or less,
The content of the component (B) (B / (A + B + C)) is 15 to 50% by mass or less,
The content (C / (A + B + C)) of the component (C) is 20 to 55% by mass or less, and the content of the component (D) with respect to the total amount of the composition for crosslinking foaming is 0.2 to 1.5% by mass,
The composition for crosslinked foaming according to any one of claims 1 to 12, wherein the content of the component (E) with respect to the total amount of the composition for crosslinked foaming is 0.5 to 10% by mass.   The crosslinked foamed body which consists of a composition as described in any one of Claims 1-14.   Footwear comprising the crosslinked foam according to claim 15.   Footwear comprising the crosslinked foam according to claim 15 in a midsole or an insole.   A laminate comprising the crosslinked foam according to claim 15 and a member on which the crosslinked foam is laminated.