JP2011173998A - Styrenic thermoplastic elastomer latex and method for producing the same - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a latex which give a styrenic thermoplastic elastomer film excellent in transparency and metal adhesiveness. <P>SOLUTION: A styrenic thermoplastic elastomer (A) and a polyvinyl alcohol resin (B) are melt-kneaded, the polyvinyl alcohol resin (B) in the obtained melt-kneaded matter is dissolved in water, and the styrenic thermoplastic elastomer (A) is dispersed in the water. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

  The present invention relates to a styrene-based thermoplastic elastomer latex, and more particularly, to a latex from which a styrene-based thermoplastic elastomer film excellent in transparency and metal adhesion can be obtained.

Styrenic thermoplastic elastomers are useful as a substitute for vulcanized rubber or as a modifier for various plastics because of their excellent flexibility and excellent rubber elasticity at low temperatures.
In addition, a latex obtained by emulsifying and dispersing such a styrene thermoplastic elastomer in water has a high cohesive force and can obtain a film having mechanical strength, flexibility, and rubber elasticity. Widely used for agents.

Such a styrene thermoplastic elastomer latex is usually mixed with an organic solvent solution of a styrene thermoplastic elastomer with an emulsifier such as a surfactant or a water-soluble polymer, and water, and using a homogenizer or an ultrasonic disperser. After emulsification, the organic solvent is removed by heating or the like.
In recent years, regarding a method for producing such a styrene-based thermoplastic elastomer latex, as a method for obtaining a latex having a small particle size and excellent storage stability, a method using an ammonium salt having a specific structure or an amine salt as an emulsifier (for example, patent literature) 1) and a method of imparting mechanical stability to latex by coexisting a tackifier resin in an organic solvent phase before emulsification (see, for example, Patent Document 2).

  However, a dry film obtained from a styrene-based thermoplastic elastomer latex produced by a conventional production method has room for improvement in terms of transparency. For example, application to coating agents is limited.

On the other hand, polyvinylidene fluoride is widely used as a negative electrode binder for lithium secondary batteries, but this is usually used as an organic solvent solution such as N-methylpyrrolidone, and from the consideration of the environment, There is a strong demand for binders that can be used in aqueous systems.
In response to such demands, for example, water-soluble polymers such as carboxymethylcellulose, and those using latexes such as rubber and thermoplastic elastomer in combination to impart flexibility to them are being studied.
However, in the case of these aqueous binders, it has been found that the adhesion to the metal material used as the negative electrode current collector is insufficient.

JP 2000-212287 A JP 2000-219748 A

  The present invention has been made in view of the above-mentioned circumstances, and its purpose is to provide a styrene-based thermoplastic elastomer latex that provides a styrene-based thermoplastic elastomer film excellent in transparency and excellent in adhesion to a metal surface. Is to provide.

As a result of intensive studies in view of the above circumstances, the present inventor has melt-kneaded the styrene-based thermoplastic elastomer (A) and the polyvinyl alcohol-based resin (B), and the polyvinyl alcohol-based resin ( It was found that the object of the present invention was achieved by a styrene-based thermoplastic elastomer latex characterized in that B) was dissolved in water and a styrene-based thermoplastic elastomer was dispersed in water, and the present invention was completed.
That is, in the present invention, a PVA resin is obtained by melt-kneading a styrene thermoplastic elastomer (hereinafter sometimes abbreviated as elastomer) and a polyvinyl alcohol resin (hereinafter polyvinyl alcohol is abbreviated as PVA). A latex in which a styrene-based thermoplastic elastomer is finely dispersed in water is obtained by dissolving the PVA-based resin in the melt-kneaded material in water. is there.

In this case, it is assumed that the PVA-based resin functions as a medium for forming the elastomer into fine particles by melt kneading, and further functions as a protective colloid when the fine particles are finely dispersed in water.
In the present invention, it is particularly preferable to use an elastomer having a carboxylic acid group or a derivative group thereof in the side chain, and a PVA resin having an α-hydroxyalkyl group in the side chain. It is presumed that these react when melt kneading to obtain fine particles in which a PVA resin is grafted on the surface of the elastomer, and that the grafted PVA resin contributes to the improvement of the stability of the elastomer.

  The styrenic thermoplastic elastomer latex of the present invention is useful as a coating agent, binder, adhesive / adhesive, and water-soluble resin modifier, and since a film with particularly excellent transparency is obtained, cosmetics are required. It is suitable for the intended use. Moreover, since the dry film is excellent in adhesion to metals, it is suitable for coating agents and binders of various metal materials. For example, application to a negative electrode binder of a lithium secondary battery can be expected.

  In addition, since the method for producing a latex of the present invention does not require the use of an organic solvent, it is highly safe in the production process, and the obtained latex and its dried product do not contain an organic solvent. It has excellent physical properties.

The description of the constituent requirements described below is an example (representative example) of an embodiment of the present invention, and is not limited to these contents.
Hereinafter, the present invention will be described in detail.
The styrene-based thermoplastic elastomer latex of the present invention is obtained by melt-kneading a styrene-based thermoplastic elastomer (A) and a PVA-based resin (B), and dissolving the PVA-based resin (B) in the obtained melt-kneaded material in water. The elastomer is obtained by dispersing in water.

[Styrenic thermoplastic elastomer (A)]
First, the styrenic thermoplastic elastomer (A) used in the present invention will be described.
The elastomer (A) used in the present invention has a polymer block of an aromatic vinyl compound typified by styrene as a hard segment, a polymer block of a conjugated diene compound as a soft segment, and a double block remaining in the polymer block. Some or all of the bonds have hydrogenated blocks or isobutylene polymer blocks.
In particular, in the present invention, as the elastomer, those having a carboxylic acid group or a derivative group thereof in the side chain are preferably used.

  The constitution of each block in the elastomer (A) is such that when the hard segment is indicated by X and the soft segment is indicated by Y, a diblock copolymer represented by XY, XYX or Y Examples include a triblock copolymer represented by -XY, and a polyblock copolymer in which X and Y are alternately connected, and the structure includes linear, branched, and star shapes. be able to. Among these, a linear triblock copolymer represented by XYX is preferable in terms of mechanical properties.

  Monomers used for forming the polymer block of the aromatic vinyl compound as a hard segment include styrene; α-methylstyrene, β-methylstyrene, o-methylstyrene, m-methylstyrene, p-methylstyrene, t- Alkyl styrene such as butyl styrene, 2,4-dimethyl styrene, 2,4,6-trimethyl styrene; halogenated styrene such as monofluoro styrene, difluoro styrene, monochloro styrene, dichloro styrene, methoxy styrene; vinyl naphthalene, vinyl anthracene, Examples thereof include vinyl compounds having an aromatic ring other than a benzene ring such as indene and acetonaphthylene, and derivatives thereof. The polymer block of the aromatic vinyl compound may be a homopolymer block of the above-described monomer or a copolymer block of a plurality of monomers, but a styrene homopolymer block is preferably used.

  The polymer block of the aromatic vinyl compound may be a copolymer obtained by copolymerizing a small amount of monomers other than the aromatic vinyl compound as long as the effects of the present invention are not impaired. Examples of such monomers include butene, pentene, and hexene. Examples thereof include olefins such as butadiene, isoprene and other diene compounds, methyl vinyl ether and other vinyl ether compounds and allyl ether compounds, and the copolymerization ratio is usually 10 mol% or less of the entire polymer block.

  The weight average molecular weight of the polymer block of the aromatic vinyl compound in the elastomer (A) is usually 10,000 to 300,000, particularly 20,000 to 200,000, more preferably 50,000 to 100,000. Those are preferably used.

  Moreover, as a monomer used for formation of the polymer block which is a soft segment, 1,3-butadiene, isoprene (2-methyl-1,3-butadiene), 2,3-dimethyl-1,3-butadiene, Conjugated diene compounds such as 1,3-pentadiene, and isobutylene can be used, and these may be used alone or in combination. Of these, a homopolymer block or copolymer block of isoprene, butadiene, and isobutylene is preferable, and a homopolymer block of butadiene or isobutylene is particularly preferably used.

In the case of such a polymer block of a conjugated diene compound, a plurality of bonding forms may be taken by polymerization. For example, in butadiene, a butadiene unit (—CH ₂ —CH (CH═CH ₂ ) by 1,2-bonding is used. -) And 1,4-bonded butadiene units (—CH ₂ —CH═CH—CH ₂ —) are formed. Since these production ratios vary depending on the type of conjugated diene compound, it cannot be generally stated, but in the case of butadiene, the ratio of 1,2-bond production is usually in the range of 20 to 80 mol%.

The polymer block of such a conjugated diene compound can improve the heat resistance and weather resistance of the styrenic thermoplastic elastomer by hydrogenating part or all of the remaining double bonds. The hydrogenation rate at that time is preferably 50 mol% or more, and particularly preferably 70 mol% or more.
By this hydrogenation, for example, the butadiene unit of 1,2-bond of butadiene becomes a butylene unit (—CH ₂ —CH (CH ₂ —CH ₃ ) —), and the butadiene unit generated by the 1,4-bond is Two continuous ethylene units (—CH ₂ —CH ₂ —CH ₂ —CH ₂ —) are formed, but usually the former is preferred.

  In addition, the polymer block which is such a soft segment may be a copolymer obtained by copolymerizing a small amount of monomers other than the above-mentioned monomers within the range that does not impair the effects of the present invention. Examples of such monomers include aromatic vinyl compounds such as styrene. Olefins such as butene, pentene, and hexene, vinyl ether compounds such as methyl vinyl ether, and allyl ether compounds. The copolymerization ratio thereof is usually 10 mol% or less of the entire polymer block.

  The weight average molecular weight of the polymer block derived from the conjugated diene compound or isobutylene in the elastomer (A) is usually 10,000 to 300,000, particularly 20,000 to 200,000, and more preferably 50,000. Those having a viscosity of 000 to 100,000 are preferably used.

  As described above, in the elastomer (A) used in the present invention, the hard segment is a polymer block of an aromatic vinyl compound, the soft segment is a polymer block of a conjugated diene compound, and a part of the residual double bond, Alternatively, the polymer block is entirely composed of a hydrogenated polymer block, an isobutylene polymer block, and the like. Typical examples thereof include a styrene / butadiene block copolymer (SBS) using styrene and butadiene as raw materials, and a butadiene of SBS. Styrene / butadiene / butylene block copolymer (SBBS) in which side chain double bonds in the structural unit are hydrogenated, and styrene / ethylene / butylene block copolymer (SEBS) in which main chain double bonds are hydrogenated, Styrene / isoprene block copolymer from styrene and isoprene (SIPS), styrene / isobutylene block copolymer of styrene and isobutylene as a raw material (SIBS) and the like can be illustrated, among others thermal stability, SEBS or SIBS has excellent weather resistance is preferably used.

  The content ratio of the polymer block of the aromatic vinyl compound that is the hard segment and the polymer block that is the soft segment in the elastomer (A) is usually 10/90 to 70/30 in weight ratio, A range of 20/80 to 50/50 is preferred. If the content ratio of the polymer block of the aromatic vinyl compound is too much or too little, the balance between the flexibility of the elastomer (A) and the rubber elasticity may be lost, and as a result, it was obtained from the latex of the present invention. Properties such as dry film may be insufficient.

Such an elastomer (A) obtains a block copolymer having a polymer block of an aromatic vinyl compound and a polymer block of a conjugated diene compound or isobutylene, and, if necessary, in the polymer block of the conjugated diene compound. It can be obtained by hydrogenating double bonds.
First, as a method for producing a block copolymer having a polymer block of an aromatic vinyl compound and a conjugated diene compound or an isobutylene polymer block, a known method can be used. And a method of sequentially polymerizing an aromatic vinyl compound and a conjugated diene compound or isobutylene in an inert organic solvent.
Next, as a method of hydrogenating the block copolymer having the polymer block of the aromatic vinyl compound and the polymer block of the conjugated diene compound, a known method can be used, for example, a borohydride compound, etc. And a method using a reducing agent, hydrogen reduction using a metal catalyst such as platinum, palladium, Raney nickel, and the like.

  The elastomer (A) used in the present invention preferably has a carboxylic acid group or a derivative group thereof in the side chain, and by using a styrene thermoplastic elastomer having such a carboxylic acid (derivative) group. In particular, a latex having excellent stability can be obtained.

The content of the carboxylic acid (derivative) group in the elastomer (A) is such that the acid value measured by a titration method is usually 0.5 to 20 mg CH ₃ ONa / g, particularly 1 to 10 mg CH ₃ ONa / g, Those of 2 to ₅ mg CH ₃ ONa / g are preferably used.
If the acid value is too low, the effect of introducing a carboxylic acid (derivative) group cannot be sufficiently obtained, and if it is too high, a gel may be generated during melt-kneading with the PVA resin (B).

  As a method for introducing such a carboxylic acid group or a derivative group thereof into the elastomer, a known method can be used. For example, an α, β-unsaturated carboxylic acid or its carboxylic acid group or its A method of copolymerizing a derivative or a method of adding an α, β-unsaturated carboxylic acid or a derivative thereof to the elastomer after the production of the elastomer is preferably used. Examples of such an addition method include a method using a radical reaction in a solution in the presence or absence of a radical initiator, and a method of melt kneading in an extruder.

  Examples of α, β-unsaturated carboxylic acids or derivatives thereof used for introducing carboxyl groups include α, β-unsaturated monocarboxylic acids such as acrylic acid and methacrylic acid; maleic acid, succinic acid, itaconic acid, phthalic acid and the like Α, β-unsaturated dicarboxylic acid; α, β-unsaturated monocarboxylic acid ester such as glycidyl acrylate, glycidyl methacrylate, hydroxyethyl acrylate, hydroxymethyl methacrylate; maleic anhydride, succinic anhydride, itaconic anhydride, phthalic anhydride Examples include α, β-unsaturated dicarboxylic acid anhydrides such as acids.

The weight average molecular weight of the elastomer (A) used in the present invention is usually 50,000 to 500,000, particularly 120,000 to 450,000, more preferably 150,000 to 400,000. .
Further, the melt viscosity of the elastomer (A) at 220 ° C. and a shear rate of 122 sec ⁻¹ is usually 100 to 3000 mPa · s, particularly 300 to 2000 mPa · s, and more preferably 800 to 1500 mPa · s.
If the weight average molecular weight is too large or the melt viscosity is too high, workability during melt kneading with the PVA resin (B) and dispersibility in the PVA resin (B) may be reduced. If the weight average molecular weight is too small or the melt viscosity is too low, the mechanical strength of the dry film obtained from the latex of the present invention may be insufficient.
The weight average molecular weight of the elastomer (A) is a value obtained by using GPC and polystyrene as a standard.

  In the present invention, one type of elastomer (A) may be used, but a plurality of types may be appropriately mixed and used for the purpose of obtaining desired characteristics. In that case, those having a carboxylic acid (derivative) group and those having no carboxylic acid (derivative) group may be used in combination.

  Examples of commercially available styrenic thermoplastic elastomers (A) having a carboxylic acid (derivative) group include “Tuftec M Series” manufactured by Asahi Kasei Co., Ltd., which is a modified carboxyl group of SBS, and “f-Dynalon” manufactured by JSR. And “Clayton FG” manufactured by Shell Japan.

Moreover, as a commercial item of the styrenic thermoplastic elastomer (A) which does not have a carboxylic acid (derivative) group, Asahi Kasei Co., Ltd. made by Asahi Kasei Co., Ltd. which is SBS, for example, Asahi Kasei which is SBBS “Tough Tech P Series” manufactured by Asahi Kasei Co., Ltd., which is SEBS, and the like.
Other commercially available products include “Clayton G”, “Clayton D” and “Califlex TR” manufactured by Shell Japan, “Septon” and “Hypler” manufactured by Kuraray, “Dynalon” and “JSR-TR” manufactured by JSR. , “JSR-SIS”, “Quintac” manufactured by Nippon Zeon Co., Ltd., “Electrified STR” manufactured by Electrochemical Co., Ltd., and the like.

[PVA resin (B)]
Next, the PVA resin (B) used in the present invention will be described.
The PVA resin (B) used in the present invention is a water-soluble resin obtained by saponifying a polyvinyl ester resin obtained by polymerizing a vinyl ester monomer, and has a vinyl alcohol structural unit as a main component. And a vinyl ester structural unit remaining depending on the degree of saponification.
In the present invention, a modified PVA resin having an α-hydroxyalkyl group in the side chain is particularly preferably used as the PVA resin (B). When the primary hydroxyl group in the α-hydroxyalkyl group has a carboxylic acid group or a derivative group thereof as the styrenic thermoplastic elastomer (A), the reactivity with these functional groups is high, and melt kneading These reactions sometimes cause the PVA resin (B) to be grafted onto the styrene thermoplastic elastomer (A), thereby contributing to an improvement in the stability of the latex.

Such α-hydroxyalkyl groups usually have 2 to 10 carbon atoms, and those having 2 to 6, particularly 2 to 4 carbon atoms are preferably used. When there are too many such carbon numbers, the water solubility of PVA-type resin (B) may be inhibited.
Among the α-hydroxyalkyl groups, a dihydroxyalkyl group represented by the following general formula (1) is particularly preferable from the viewpoint of improving the stability of the styrene-based thermoplastic elastomer latex.

The α-hydroxyalkyl group is preferably directly bonded to the main chain of the PVA resin from the viewpoint of thermal stability. However, as long as the effect of the present invention is not hindered, the α-hydroxyalkyl group may be bonded via various bonding chains. It may be bonded to the main chain of the resin.
Examples of such a linking chain include hydrocarbon chains such as alkylene, alkenylene, alkynylene, phenylene, and naphthylene, linking chains including an ether bond such as —O— and — (CH ₂ O) _m —, —CO—, — CO (CH ₂ ) _m CO—-bonded chain containing a carbonyl group, —S—, —SO—, —SO ₂ —, etc., sulfur-containing bond chain, —NR—, —CONR—, etc. Examples thereof include a bond chain containing atoms and a bond chain containing metal atoms such as silicon, titanium, and aluminum.
If such a bond chain is long, the water resistance of the film obtained from the latex of the present invention tends to be impaired, or the stability of the latex tends to be lowered. Therefore, the short one is preferable, and the number of atoms is preferably 3 or less. .
Therefore, the most preferable PVA resin (B) used in the present invention is the following general formula (2) in which the dihydroxyalkyl group represented by the general formula (1) is directly bonded to the main chain of the PVA resin. It has a structural unit represented by these.

    The α-hydroxyalkyl group may have a small amount of substituents other than hydroxyl groups as long as the effects of the present invention are not impaired. Examples of such substituents include methyl groups, ethyl groups, and n-propyl groups. And a functional group such as a halogen group, a hydroxyl group, an ester group, a carboxylic acid group, and a sulfonic acid group. It is done.

  The content of the α-hydroxyalkyl group in the PVA resin (B) used in the present invention is usually 1 to 12 mol%, particularly 3 to 10 mol%, more preferably 6 to 8 mol%. It is done. If the content of the α-hydroxyalkyl group is too small, the effect of introducing the α-hydroxyalkyl group cannot be sufficiently obtained. If the content is too large, the water resistance of the film obtained from the styrene-based thermoplastic elastomer latex of the present invention is insufficient. Tend to.

As a method for introducing an α-hydroxyalkyl group into the PVA-based resin, either a copolymerization method or a post-reaction method can be used.
For example, as a method by post-reaction, a method in which a glycidyl compound is added to a hydroxyl group of a PVA resin can be mentioned. However, according to such a method, since the α-hydroxyalkyl group is bonded to the main chain by an ether bond, it may not be preferable for applications that require thermal stability.

In the case of copolymerization, when a vinyl ester monomer is copolymerized into a polyvinyl ester resin, an olefin compound having an α-hydroxyalkyl group may be used as the copolymer monomer. Monohydroxy olefin compounds such as 4-hydroxy-1-butene, 5-hydroxy-1-pentene, 6-hydroxy-1-hexene, 3,4-dihydroxy-1-butene, 4,5-dihydroxy-1-pentene And dihydroxyolefin compounds such as 5,6-dihydroxy-1-hexene.
In addition, those in which the hydroxyl group in the olefin compound having such a hydroxyl group is protected with a functional group that can be deprotected in a saponification step or the like are preferable from the viewpoint of copolymerization with a vinyl ester or the like. In particular, an acetylated product having a common by-product in the saponification step and vinyl acetate frequently used as a vinyl ester monomer is preferably used.
Therefore, when the PVA resin (B) having the structural unit represented by the general formula (2) is produced by copolymerization, 3,4-dihydroxy-1-butene and its derivatives are preferably used as the copolymerization monomer. It is done.

Examples of the method for producing the PVA resin (B) having the structural unit represented by the general formula (2) include (i) 3,4-dihydroxy-1-butene as a copolymerization monomer or an acylated product thereof. A method in which a derivative is used and this is copolymerized with a vinyl ester monomer and ethylene, and then the obtained copolymer is saponified; (ii) vinyl ethylene carbonate is used as a copolymerizable monomer, and the resulting copolymer is A method of saponification and decarboxylation, (iii) a method of saponifying and deacetalizing the resulting copolymer using 2,2-dialkyl-4-vinyl-1,3-dioxolane as a copolymerization monomer, and the like. Can be mentioned.
As the methods (i), (ii), and (iii), for example, a method described in JP-A-2006-95825 can be used.

  Among these, the method (i) is preferably used because it is excellent in copolymerization reactivity, can easily introduce a modifying group into EVOH, and has excellent industrial handling properties. In particular, 3,4-diacetoxy-1-butene, which is an acetylated product of 3,4-dihydroxy-1-butene, is excellent in copolymerizability with vinyl ester monomers and the like, and is often used as vinyl ester monomers. Since a by-product at the time of saponification is common, it is preferable because it can be separated and recovered at the same time.

  The saponification degree (measured in accordance with JIS K6726) of the PVA resin (B) used in the present invention is usually 80 to 100 mol%, particularly 85 to 99.9 mol%, and further 88. Those of ˜99 mol% are preferably used. When the saponification degree is too low, an acetic acid odor is generated during melt-kneading with the styrenic thermoplastic elastomer, which may remain in the melt-kneaded product and further in the latex.

Moreover, the average degree of polymerization (measured according to JIS K6726) of the PVA resin (B) is usually 200 to 1800, particularly 250 to 1000, and more preferably 300 to 500. If the average degree of polymerization is too small or too large, when the melt-kneaded product with the styrene-based thermoplastic elastomer (A) is used, the styrene-based thermoplastic elastomer (A) is dispersed in the melt-kneaded product. As a result, it may be difficult to obtain a latex in which uniform fine particles are dispersed. When the latex is too large, shear heat generation increases during melt-kneading, and PVA resin (B) or styrene heat Plastic elastomer (A)
There is a tendency for the work to be easily decomposed.

  The PVA resin (B) used in the present invention may be one type or a mixture of two or more types. The PVA resin containing the α-hydroxy group described above and other modifications A combination with PVA resin or unmodified PVA, or a combination of PVA resins having different degrees of polymerization and saponification can be used.

[Styrenic thermoplastic elastomer latex]
Next, the styrenic thermoplastic elastomer latex obtained in the present invention will be described.
The latex of the present invention melts and kneads the above-mentioned styrene-based thermoplastic elastomer (A) and PVA-based resin (B), dissolves the PVA-based resin (B) in the obtained melt-kneaded product in water, and takes this It is obtained by dispersing an elastomer in water.

  In the production of the latex of the present invention, the blending ratio (A / B) of the elastomer (A) and the PVA resin (B) is usually 10/90 to 40/60, particularly 20/80 to 30 in terms of weight ratio. A range of / 70 is preferably used. When the blending ratio is too small, the elastomer concentration in the obtained latex is lowered, and the ratio of the PVA resin in the dried product obtained from the latex is increased, so that the water resistance tends to be insufficient. On the other hand, if it is too large, the elastomer (A) is not sufficiently dispersed in the melt-kneaded product, and it may be difficult to obtain a uniformly finely dispersed latex.

First, the process of melt-kneading the styrene thermoplastic elastomer (A) and the PVA resin (B) will be described.
The melt kneading of the elastomer (A) and the PVA resin (B) can be performed using a known kneading apparatus such as a kneader ruder, an extruder, a mixing roll, a Banbury mixer, or a blast mill. A method using a machine is industrially preferred.
Examples of such an extruder include a single screw extruder and a twin screw extruder. Among these, a twin screw extruder having the same screw rotation direction is more preferable because sufficient kneading can be obtained by appropriate shearing. The L / D of such an extruder is usually 10 to 80, and those having 15 to 70, more preferably 15 to 60 are preferably used. If the L / D is too small, melt kneading may be insufficient, and the dispersibility of the elastomer (A) in the melt kneaded product may be insufficient. Conversely, if too large, it is preferable to give excessive shear. There is no tendency to cause shearing fever.

  The screw rotation speed of the extruder is usually from 10 to 400 rpm, particularly preferably from 30 to 300 rpm, more preferably from 50 to 250 rpm. If the rotational speed is too small, the discharge tends to be unstable, and if it is too large, the resin may be deteriorated due to undesirable shearing heat generation.

The resin temperature in the extruder is usually 80 to 260 ° C., and particularly preferably 130 to 240 ° C., more preferably 180 to 230 ° C. If the resin temperature is too high, the PVA resin (B) or the elastomer (A) may be thermally decomposed. Conversely, if it is too low, the melt kneading is insufficient and the elastomer (A) in the melt kneaded product is insufficient. There is a tendency for dispersibility to be insufficient.
The method for adjusting the resin temperature is not particularly limited, but usually, a method of appropriately setting the temperature of the cylinder in the extruder and the number of rotations is used.

The melt-kneaded product discharged from the extruder is preferably made into pellets from the viewpoint of transfer to the next step and ease of handling, and the pelletizing method is not particularly limited. A method is used in which the material is extruded into strands, cooled, and then cut into an appropriate length. The cooling method is not particularly limited, but a method of contacting a liquid held at a temperature lower than the temperature of the extruded resin and a method of blowing cold air are preferably used. As the liquid, a PVA resin ( It is necessary to be an organic solvent that does not dissolve B). For example, an alcohol-based solvent can be used, but an air cooling system is preferably used in terms of the environment.
The shape of such a pellet is usually cylindrical, and the size thereof is preferably smaller considering that it is later brought into contact with water and the PVA resin (B) therein is dissolved and removed. The diameter is preferably 2 to 6 mm, and the strand cut length is preferably about 1 to 6 mm. In addition, while EVOH discharged from the extruder is still in a molten state, a method of cutting in the air or in an organic solvent can also be used, in which case a nearly spherical pellet is obtained. As the size, a range of 2 to 5 mmφ in diameter is preferably used.

Next, the process for producing the latex of the present invention from the melt-kneaded product of the styrene thermoplastic elastomer (A) and the PVA resin (B) obtained in the above process will be described.
This process dissolves the PVA resin (B) contained therein from the melt-kneaded product of the obtained elastomer (A) and PVA resin (B), and the method is not particularly limited. Usually, however, the latex of the present invention can be obtained by putting the pellets of the melt-kneaded product obtained by the above-mentioned method into water, stirring and heating as necessary.

  The solid content concentration of the styrene-based thermoplastic elastomer latex obtained by such a method is usually 10 to 50% by weight, and particularly preferably 10 to 40% by weight. If the solid content concentration is too small, it is not preferable because it requires a lot of energy and time to remove the moisture. If the solid content concentration is too large, the fluidity is lowered and workability may be hindered.

  The particle size of the styrenic thermoplastic elastomer in the latex of the present invention obtained by such a method is usually 50 to 2000 nm, particularly 100 to 1000 nm, more preferably 150 to 800 nm μm.

Hereinafter, the present invention will be described with reference to examples. However, the present invention is not limited to the description of the examples unless it exceeds the gist.
In the examples, “parts” and “%” mean weight basis unless otherwise specified.

Example 1
[Production of PVA resin (B1)]
A reaction vessel equipped with a reflux condenser, a dropping funnel and a stirrer was charged with 68.0 parts of vinyl acetate, 23.8 parts of methanol, and 8.2 parts of 3,4-diacetoxy-1-butene, and azobisisobutyronitrile. Was added in an amount of 0.3 mol% (compared with vinyl acetate), and the temperature was raised under a nitrogen stream while stirring to initiate polymerization. When the polymerization rate of vinyl acetate reaches 90%, m-dinitrobenzene is added to complete the polymerization, and then unreacted vinyl acetate monomer is removed out of the system by blowing methanol vapor. A combined methanol solution was obtained.

  Next, the methanol solution was further diluted with methanol, adjusted to a concentration of 45%, charged into a kneader, and a 2% methanol solution of sodium hydroxide was added to the vinyl acetate structural unit in the copolymer while maintaining the solution temperature at 35 ° C. And saponification was performed by adding 10.5 mmol with respect to 1 mol of the total amount of 3,4-diacetoxy-1-butene structural units. When saponification progressed and saponified substances were precipitated and formed into particles, they were separated by filtration, washed well with methanol and dried in a hot air dryer to prepare the intended PVA resin (B1).

The saponification degree of the obtained PVA-based resin (B1) was 98.9 mol% when analyzed by the alkali consumption required for hydrolysis of residual vinyl acetate and 3,4-diacetoxy-1-butene. . The average degree of polymerization was 450 when analyzed according to JIS K 6726. The content of the 1,2-diol structural unit represented by the general formula (1) is ¹ H-NMR (300 MHz proton NMR, d6-DMSO solution, internal standard substance: tetramethylsilane, 50 ° C.). It was 6 mol% when computed from the measured integral value. Moreover, MFR (210 degreeC, load 2160g) was 5.5g / 10min, and melt viscosity (220 degreeC, shear rate 122sec < ^-1 >) was 1040 mPa * s.

[Production of melt-kneaded product]
Styrene / ethylene / butylene block copolymer (SEBS) having a carboxyl group as the styrenic thermoplastic elastomer (A1) (“Tough Tech M1913” manufactured by Asahi Kasei Corporation (oxidized 10 mg CH ₃ ONa / g, melt viscosity 1060 mPa · s (220 ° C. shear) Using a speed of 122 sec ^-1 )), 20 parts of the PVA resin (B1) 80 parts were driven, melt-kneaded using the twin screw extruder under the following conditions, extruded into a strand, and cut with a pelletizer As a result, a melt-kneaded pellet (diameter: about 1 mm, length: about 2 mm) was obtained.

Diameter (D) 15mm,
L / D = 60
Screw rotation speed: 200rpm
Set temperature: C1 / C2 / C3 / C4 / C5 / C6 / D = 90/205/210 /
210/210/215/220/220/220 ° C
Discharge rate: 1.5kg / hr

[Latex] 30 parts of the obtained pellets were put into 70 parts of water at room temperature, heated while stirring, and stirred at 80 ° C. for 90 minutes to obtain the styrene-based thermoplastic elastomer latex of the present invention.

(Metal adhesion)
The obtained styrene-based thermoplastic elastomer latex is coated on a copper plate (Japan Test Panel “Copper Plate for Test”, 15 cm × 7 cm × 2 mm) with a bar coater (No. 40), in a hot air dryer at 120 ° C. And dried for 10 minutes to form a film having a thickness of 10 μm.
The metal adhesion of the obtained dried film was evaluated by a pencil hardness method according to JIS K5600. The results are shown in Table 2.

(transparency)
The obtained latex was coated on a PET film using a bar coater (No. 40) so that the film thickness was about 10 μm, and air-dried in an environment of 23 ° C. and 50% RH to produce a film. The transparency of this film was measured according to JIS K 7105 using a haze meter (“HazeMeter NDH2000” manufactured by Nippon Denshoku Industries Co., Ltd.), and a haze value converted to a film thickness of 10 μm was obtained.

Example 2
Into a reaction vessel equipped with a reflux condenser, a dropping funnel and a stirrer, 68.5 parts of vinyl acetate, 20.5 parts of methanol, and 11.0 parts of 3,4-diacetoxy-1-butene were added at an initial charge rate of 10% for vinyl acetate. , Vinyl acetate, and 3,4-diacetoxy-1-butene were charged under the conditions of constant rate dropping for 9 hours, and 0.3 mol% of azoisobutyronitrile (vs. prepared vinyl acetate) was added and stirred under a nitrogen stream. The temperature was raised to start polymerization. When the polymerization rate of vinyl acetate reaches 90%, m-dinitrobenzene is added to complete the polymerization, and then unreacted vinyl acetate monomer is removed out of the system by blowing methanol vapor. A combined methanol solution was obtained.

Next, the methanol solution was further diluted with methanol, adjusted to a concentration of 45%, charged into a kneader, and a 2% methanol solution of sodium hydroxide was added to the vinyl acetate structural unit in the copolymer while maintaining the solution temperature at 35 ° C. And saponification was performed by adding 10.5 mmol with respect to 1 mol of the total amount of 3,4-diacetoxy-1-butene structural units. As saponification progressed, when saponified substances were precipitated and formed into particles, they were filtered off, washed thoroughly with methanol and dried in a hot air dryer to prepare the intended PVA resin (B2).
The degree of saponification of the obtained PVA (B2) was 98.9 mol%. The average degree of polymerization was 300. The content of 1,2-diol structural unit was 8 mol%.

  In Example 1, a melt-kneaded product and a latex with the styrenic thermoplastic elastomer (A1) were prepared in the same manner except that the above-described PVA resin (B2) was used as the PVA resin, and evaluated in the same manner. The results are shown in Table 2.

Comparative Example 1
As an elastomer, after diluting SBR latex (Nippon Zeon "Type A", concentration 45%) with water to a concentration of 30%, 80 parts thereof and 20 parts of 30% aqueous solution of PVA (B1) were mixed, An SBR latex containing the same PVA-based resin as in Example 1 at the same content ratio was obtained.
Using this SBR latex, evaluation was performed in the same manner as in Example 1. The results are shown in Table 2.

A1: Carboxyl group-containing SEBS
*: SBR latex

  Thus, the styrene thermoplastic elastomer (A) and the PVA resin (B) are melt-kneaded, the PVA resin (B) in the melt-kneaded product is dissolved in water, and the elastomer (B) is submerged in water. From the dispersed latex of the present invention (Examples 1 and 2), a dry film having excellent transparency and excellent metal adhesion was obtained, and SBR latex was used as an elastomer. From what blended the same PVA-based resin in the same ratio (Comparative Example 1), only a dry film having insufficient properties was obtained.

  The styrenic thermoplastic elastomer latex of the present invention is useful as a coating agent, binder, adhesive / adhesive, and water-soluble resin modifier, and since a film with particularly excellent transparency is obtained, cosmetics are required. It is suitable for the intended use. Moreover, since the dry film is excellent in adhesion to metals, it is suitable for coating agents and binders of various metal materials. For example, application to a negative electrode binder of a lithium secondary battery can be expected.

Claims (6)

The styrene thermoplastic elastomer (A) and the polyvinyl alcohol resin (B) are melt-kneaded, the polyvinyl alcohol resin (B) in the obtained melt-kneaded material is dissolved in water, and the styrene thermoplastic elastomer (A ) A styrene-based thermoplastic elastomer latex characterized by being dispersed in water. The styrene thermoplastic elastomer latex according to claim 1, wherein the styrene thermoplastic elastomer (A) is a styrene thermoplastic elastomer having a carboxylic acid group or a derivative group thereof in a side chain. The styrene thermoplastic elastomer latex according to claim 1 or 2, wherein the polyvinyl alcohol resin (B) is a polyvinyl alcohol resin having an α-hydroxyalkyl group in the side chain. The styrene thermoplastic elastomer latex according to claim 3, wherein the α-hydroxyalkyl group is a dihydroxyalkyl group represented by the following general formula (1).
The styrene-based heat according to any one of claims 1 to 4, wherein a blending ratio (A / B) of the styrene-based thermoplastic elastomer (A) and the polyvinyl alcohol-based resin (B) is 10/90 to 40/60 by weight. Plastic elastomer latex. The styrene thermoplastic elastomer (A) and the polyvinyl alcohol resin (B) are melt-kneaded, the polyvinyl alcohol resin (B) in the obtained melt-kneaded material is dissolved in water, and the styrene thermoplastic elastomer (A ) Is dispersed in water. A method for producing a styrene-based thermoplastic elastomer latex.