JP5260939B2 - Water dispersion - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide an aqueous dispersion which develops the excellent adhesion (adhesiveness) to molded articles of various kinds of resins of polyolefins such as polypropylene, synthetic rubbers, unsaturated polyesters, epoxy resins, polyurethane resins or the like, or to metals such as steel plates and aluminum. <P>SOLUTION: The aqueous dispersion comprises (A) a thermoplastic elastomer and (C) a urethane linkage-containing resin in the same particle; and the aqueous dispersion comprises a reaction product formed by reacting (A) the thermoplastic elastomer with (C) the urethane linkage-containing resin; and the aqueous dispersion comprises a reaction product formed by reacting (B) a functional group-modified thermoplastic elastomer with (C) the urethane linkage-containing resin; and in addition, the aqueous dispersion comprises such a copolymer of propylene-1-butene as (A) the above thermoplastic elastomer. The aqueous dispersion has a new, as never before, operational advantage that the aqueous dispersion can be used just as it is without causing a separation phenomenon in the aqueous dispersion and as a sprayable coating material, paint, a primer and an adhesive, and has the excellent adhesion to molded articles of various kinds of resins such as polyolefins and synthetic rubbers and to metals such as steel plate and aluminum. Also, this aqueous dispersion can use a curing agent reactive with an active hydrogen and/or a hydroxy group. Furthermore, the more excellent adhesive aqueous dispersion can be obtained by utilizing as (A) the thermoplastic elastomer, a propylene-1-butene random copolymer. <P>COPYRIGHT: (C)2008,JPO&amp;INPIT

Description

  The present invention relates to an aqueous dispersion in which a thermoplastic elastomer and a resin having a urethane bond are contained in the same particle (dispersed particle). More specifically, an additive such as a pigment as a coating material, a paint, a primer, and an adhesive on a non-treated polyolefin-based resin film, sheet, or molded product, or a metal such as a steel plate or aluminum by forming a coating film The present invention relates to an aqueous dispersion that is excellent in compatibility with other resins including the above-mentioned blends and curing agents, and also excellent in storage stability and coating workability.

  Conventionally, polyolefin resins are generally productive and excellent in various moldability, and have many advantages such as light weight, rust prevention, and impact resistance. Therefore, interior and exterior of automobiles and ships, and home appliances. It is widely used as furniture, miscellaneous goods, building materials, etc. Such polyolefin-based resin molded products are generally non-polar and crystalline, unlike synthetic resins having polarity typified by polyurethane resins, polyamide resins, acrylic resins, and polyester resins. For this reason, it is very difficult to perform coating and adhesion to a general-purpose resin composition.

  For this reason, when coating or adhering to a polyolefin resin molded product, the surface adhesion is improved by activating the surface with chromic acid, flame, corona discharge, plasma, solvent, etc. I have been. For example, in automotive bumpers, the surface is etched with a halogen-based organic solvent such as trichloroethane to improve adhesion to the coating film, or after pretreatment such as corona discharge treatment, plasma treatment, or ozone treatment. However, the purpose of painting and bonding has been made. In addition, a method of treating the surface of a base material such as a molded product with a primer is used. For example, a composition in which maleic acid is introduced into a polyolefin (Patent Document 1), or a composition mainly composed of a chlorinated modified polyolefin ( Patent Document 2) has also been proposed.

  Metals such as steel plates are also used in a wide range of fields such as interiors and exteriors of automobiles and ships, home appliances, furniture, sundries, and building materials. The steel sheet surface is painted mainly for the purpose of improving the appearance and imparting anticorrosion properties. In particular, it is important to suppress corrosion and cracking by suppressing deformation and peeling of the coating film due to deformation by external force and collision of objects. At present, in order to suppress these, a coating with a thick coating film or a modified propylene-ethylene copolymer (Patent Document 3) formed by graft copolymerization with maleic acid or its anhydride is used. ing. However, these contain organic solvents such as toluene and xylene, and there are concerns about problems such as safety and environmental pollution. Therefore, a composition containing chlorinated modified polyolefin as a main component is dispersed in water (Patent Document 4), and is composed of an olefin polymer and a petroleum hydrocarbon resin (Patent Document 5). ) Etc. have been proposed.

However, since these use a large amount of a surfactant to form an aqueous system, there arises a problem that the water resistance of the coating film and the adhesion to the base material are lowered, or the surface is bleed out to cause stickiness. If the amount of the surfactant that causes these problems is reduced, problems such as inability to form an aqueous system or poor stability of the aqueous resin composition occur. Moreover, many of these also have the problem that sufficient adhesiveness (adhesion) with respect to a base material is not expressed.
Japanese Patent Publication No. 62-21027 Japanese Patent Publication No. 50-10916 Japanese Patent Publication No. 6-057809 JP-A-1-256556 JP 2004-27055 A

  The subject of the present invention is an improvement of the above-mentioned problems, such as molded products of various resins consisting of polyolefin such as polypropylene, synthetic rubber, unsaturated polyester, epoxy resin, urethane resin, etc., and metals such as steel plates and aluminum, The object is to provide an aqueous dispersion that exhibits excellent adhesion (adhesiveness).

  As a result of intensive studies and studies to achieve the above object, the present inventors include a thermoplastic elastomer (A) and a resin having a urethane bond (C) in the same particle. The present inventors have found that an aqueous dispersion is extremely effective for achieving the above-mentioned target and have completed the present invention. That is, the present invention relates to the following (1) to (21), for example.

(1) An aqueous dispersion comprising a thermoplastic elastomer (A) and a resin (C) having a urethane bond in the same particle.
(2) The aqueous dispersion according to (1), which is obtained by reacting a thermoplastic elastomer (A) with a resin (C) having a urethane bond.

(3) The aqueous dispersion described in (1), which is obtained by reacting a thermoplastic elastomer (B) modified with a functional group and a resin (C) having a urethane bond.
(4) The aqueous dispersion according to (3), wherein the functional group of the thermoplastic elastomer (B) modified with the functional group reacts with the functional group of the resin (C) having a urethane bond. .

(5) The water dispersion according to any one of (1) to (4), wherein the particle diameter of the particles is in the range of 10 nm to 10 μm.
(6) A thermoplastic elastomer (A) and / or a thermoplastic elastomer (B) modified with a functional group and a resin (C) having a urethane bond are [(A) and / or (B)] / ( C) = The aqueous dispersion according to (5), comprising a weight ratio of 10/90 to 95/5.

  (7) At least one selected from the group consisting of petroleum hydrocarbon resin (D), rosin resin (E) and terpene resin (F) is contained in the same particle (1) The water dispersion in any one of-(6).

  (8) Mixing at least one selected from the group consisting of an aqueous dispersion of petroleum hydrocarbon resin (D), an aqueous dispersion of rosin resin (E), and an aqueous dispersion of terpene resin (F) The aqueous dispersion according to any one of (1) to (7), wherein

  (9) A total of 30 to 100 parts by weight of a thermoplastic elastomer (A) and / or a thermoplastic elastomer (B) modified with a functional group and a resin (C) having a urethane bond, and a petroleum hydrocarbon resin ( D), a total of 0 to 70 parts by weight of at least one selected from the group consisting of rosin resin (E) and terpene resin (F), [(A) and / or (B)], ( C), The total amount of [(D) and / or (E) and / or (F)] is 100 parts by weight, The water dispersion according to (7) or (8),

(10) A thermoplastic elastomer (B) modified with a functional group containing a carboxyl group, a resin (C) having a urethane bond containing a carboxyl group, and a petroleum hydrocarbon containing a carboxyl group in the aqueous dispersion. Resin (D), rosin resin containing carboxyl group (
(1) to (9) characterized by containing at least one substance selected from the group consisting of E) and a terpene resin (F) containing a carboxyl group and containing a basic substance. The water dispersion according to any one of the above.

(11) The thermoplastic elastomer (A) is a propylene / 1-butene copolymer, and the propylene / 1-butene copolymer is
(I) containing units derived from propylene in an amount of 60 to 90 mol% and units derived from 1-butene in an amount of 10 to 40 mol% (provided that all structural units are 100 mol%);
(Ii) the intrinsic viscosity measured in decalin at 135 ° C. is 0.1-12 dl / g,
(Iii) The water dispersion according to any one of (1) to (10), wherein the molecular weight distribution (Mw / Mn) determined by gel permeation chromatography (GPC) is in the range of 1 to 3. body.

(12) The aqueous dispersion according to any one of (1) to (11), which contains a surfactant.
(13) A coating material containing the water dispersion according to any one of (1) to (12).

(14) A paint containing the water dispersion according to any one of (1) to (12).
(15) A primer containing the aqueous dispersion according to any one of (1) to (12).
(16) An adhesive containing the water dispersion according to any one of (1) to (12).

(17) A coating film formed by applying the coating material according to (13), the paint according to (14), the primer according to (15), and the adhesive according to (16).
(18) A coating material containing a main agent containing the aqueous dispersion according to any one of (1) to (12) having active hydrogen and / or a hydroxyl group, and a curing agent capable of reacting with active hydrogen and / or a hydroxyl group. .

(19) A coating film obtained by curing the coating material according to (18).
(20) The coating film according to (17) or (19), wherein the substrate is an olefin resin.

  (21) The coating film according to (17) or (19), wherein the substrate is a metal.

  According to the present invention, the water dispersion can be used as it is without causing a separation phenomenon, and is a coating material, paint, primer and adhesive that can be spray-coated, and various resin moldings such as polyolefin and synthetic rubber It has an unprecedented effect of excellent adhesion to products, metals such as steel plates and aluminum. A curing agent capable of reacting with active hydrogen and / or a hydroxyl group can also be used. Furthermore, the water dispersion which is more excellent in adhesiveness can be obtained by using a propylene 1-butene random copolymer (PBR) as a thermoplastic elastomer (A).

The aqueous dispersion of the present invention can be obtained by the following method.
[Thermoplastic elastomer (A)]
Examples of the thermoplastic elastomer (A) used in the present invention include polyethylene, polypropylene, poly-1-butene, poly-3-methyl-1-butene, poly-3-methyl-1-pentene, and poly-4-methyl- 1-pentene, ethylene / propylene copolymer, ethylene / 1
-Butene copolymer, propylene / 1-butene copolymer, represented by ethylene / propylene / 1-butene copolymer, ethylene, propylene, 1-butene, 3-methyl-1-butene, 4-methyl- Thermoplastic elastomers of α-olefins such as 1-pentene, 3-methyl-1-pentene, 1-heptene, 1-hexene, 1-octene, 1-decene and 1-dodecene, or copolymers of two or more kinds -. In addition, polymers containing alicyclic structures such as norbornene polymers, monocyclic cyclic polyolefin polymers, cyclic conjugated diene polymers, vinyl alicyclic hydrocarbon polymers, and hydrogenated products thereof should also be used. Can do.

  Among these, ethylene-butene copolymer, ethylene-propylene copolymer, ethylene-octene copolymer, ethylene-propylene-butene copolymer, propylene / 1-butene copolymer, propylene-octene copolymer More preferably, it is a propylene / 1-butene copolymer, and these are used alone or in combination of two or more. Most preferably, it is a propylene / 1-butene random copolymer (PBR) described in detail below. Further, the weight average molecular weight (hereinafter abbreviated as Mw. The weight average molecular weight can be measured, for example, by gel permeation chromatography (GPC) using polystyrene as a standard) is usually 10,000 to 700. In the range of 30,000, preferably 30,000 to 500,000.

  Other examples of the thermoplastic elastomer (A) include hydrogenated styrene-conjugated diene block copolymers, hydrogenated styrene-conjugated diene random copolymers, and the like. Examples of the structure of the hydrogenated product include a hydrogenated product of a styrene-conjugated diene diblock copolymer, a hydrogenated product of a styrene-conjugated diene-styrene triblock copolymer, and the like. Examples of the conjugated diene used here include butadiene and isoprene. Among these, a hydrogenated product of a styrene-isoprene-styrene triblock copolymer and a hydrogenated product of a random copolymer of styrene-butadiene are preferable.

  The thermoplastic elastomer used here has a styrene content of usually 2 to 60% by weight, more preferably 3 to 45% by weight. The weight average molecular weight (hereinafter abbreviated as Mw) is preferably in the range of 10,000 to 700,000, and the hydrogenated product of styrene-isoprene-styrene copolymer is preferably 15,000 to 500,000. Moreover, in the hydrogenated product of a styrene-butadiene copolymer, 10,000-700,000, Furthermore, 50,000-500,000 are preferable.

Said thermoplastic elastomer can be used individually or in combination of 2 or more types.
(Propylene / 1-butene copolymer)
In the present invention, it is preferable to use a propylene / 1-butene copolymer as the thermoplastic elastomer (A) in order to obtain an aqueous dispersion having more excellent adhesiveness. The propylene / 1-butene copolymer satisfies the following (1) to (3), preferably satisfies (4) to (6), and more preferably satisfies (7) and / or (8). -Butene random copolymer (PBR). By using a propylene / 1-butene random copolymer (PBR), an aqueous dispersion capable of further improving adhesiveness can be obtained.

  (1) The unit derived from propylene is derived from 1-butene in an amount of 60 to 90 mol%, preferably 65 to 88 mol%, more preferably 70 to 85 mol%, still more preferably 70 to 75 mol%. The unit is contained in an amount of 10 to 40 mol%, preferably 12 to 35 mol%, more preferably 15 to 30 mol%, and still more preferably 25 to 30 mol% (provided that 100 mol% of all structural units are contained). And).

  This propylene / 1-butene copolymer may contain a small amount of structural units derived from olefins other than propylene and 1-butene, such as ethylene, for example, in an amount of 10 mol% or less.

(2) The intrinsic viscosity measured in decalin at 135 ° C. is 0.1 to 12 dl / g, preferably 0.5 to 10 dl / g, more preferably 1 to 5 dl / g.
(3) The molecular weight distribution (Mw / Mn) calculated | required by gel permeation chromatography (GPC) is the range of 1-3, Preferably it is 1.8-3.0, More preferably, it is 1.9-2 .5.

By using the propylene / 1-butene copolymer satisfying the above (1) to (3) as the material of the aqueous dispersion, the adhesiveness is further improved.
Moreover, when this propylene / 1-butene copolymer satisfies the following (4) to (6), it becomes a propylene / 1-butene random copolymer (PBR). By using this propylene / 1-butene random copolymer (PBR) as an aqueous dispersion material, molded articles of various resins made of polyolefin such as polypropylene, synthetic rubber, unsaturated polyester, epoxy resin, urethane resin, etc. In addition, adhesion to a metal such as a steel plate or aluminum is further improved.

  Furthermore, it is also preferable to use the propylene / 1-butene random copolymer (PBR) in which the propylene / 1-butene copolymer satisfies the following (7) and (8) as the material of the aqueous dispersion.

(4) Triad isotacticity (mm fraction) determined from ¹³ C-NMR spectrum measurement is 85% or more and 97.5% or less, preferably 87% or more and 97% or less, more preferably 90% or more and 97% or less. It is. In the present invention, it is important not to increase the mm fraction too much, and by providing a specific mm fraction, the melting point can be lowered with a relatively high propylene content.

The triad isotacticity (mm fraction) is an index indicating the stereoregularity of the propylene / 1-butene random copolymer (PBR), and can be determined as follows.
This mm fraction is defined as the ratio in which the branching directions of the methyl groups are the same when the three head-to-tail bonded propylene unit chains present in the polymer chain are represented by a surface zigzag structure. In ¹³ C-NMR spectrum.

When determining the mm fraction of the propylene / 1-butene random copolymer (PBR) from the ¹³ C-NMR spectrum, (i) head-to-tail, specifically, as three chains containing propylene units present in the polymer chain For propylene units and butene units, which are composed of 3 linked propylene units and (ii) head-to-tail bonded propylene units and butene units, and the second unit is a propylene unit, the mm fraction is Measured.

The mm fraction is determined from the peak intensity of the side chain methyl group of the second unit (propylene unit) in these three chains (i) and (ii). This will be described in detail below.
The ¹³ C-NMR spectrum of propylene / 1-butene random copolymer (PBR) is hexachlorobutadiene containing a small amount of deuterated benzene in the sample tube using propylene / 1-butene random copolymer (PBR) as a lock solvent. After complete dissolution, it is measured by proton complete decoupling method at 120 ° C. The measurement conditions are a flip angle of 45 ° and a pulse interval of 3.4 T1 or more (T1 is the longest value of the spin lattice relaxation time of the methyl group). Since T1 of the methylene group and methine group is shorter than that of the methyl group, the recovery of the magnetization of all the carbon in the sample is 99% or more under this condition. The chemical shift is based on tetramethylsilane, and the carbon peak of the third unit methyl group of the 5-chain (mmmm) propylene unit bonded to head-to-tail is 21.593 ppm, and the other carbon peaks are based on this. .

Of the ¹³ C-NMR spectrum of the propylene / 1-butene random copolymer (PBR) thus measured, the methyl carbon region (about 19.5 to 21.9 ppm) in which the side chain methyl group of the propylene unit is observed. ) Are classified into a first peak region (about 21.0 to 21.9 ppm), a second peak region (about 20.2 to 21.0 ppm), and a third peak region (about 19.5 to 20.2 ppm). The

  In each of these regions, a side chain methyl group peak of the second unit (propylene unit) in the trimolecular chain (i) and (ii) having head-to-tail bonds as shown in Table 1 is observed.

  In Table 1, P represents a structural unit derived from propylene, and B represents a structural unit derived from 1-butene. Of the three head-to-tail bonds (i) and (ii) shown in Table 1, (i) PPP (mm), PPP (mr), and PPP (rr) in which all three chains are composed of propylene units, The directions are shown below in a surface zigzag structure. In addition, (ii) mm, mr, and rr bonds of a triple chain (PPB, BPB) containing a butene unit conform to this PPP.

In the first region, the methyl group of the second unit (propylene unit) in the mm-bonded PPP, PPB, BPB3 chain resonates.
In the second region, the methyl group of the second unit (propylene unit) in the mr-bonded PPP, PPB, BPB3 chain and the methyl group of the second unit (propylene unit) in the rr-bonded PPB, BPB3 chain are resonant. To do.

In the third region, the methyl group of the second unit (propylene unit) of the rr-bonded PPP3 chain resonates.
Therefore, the triad isotacticity (mm fraction) of propylene / 1-butene random copolymer (PBR) is (i) three-chain propylene units linked head-to-tail, or (ii) propylene linked head-tail. 3 chain of propylene / butene consisting of a unit and a butene unit and containing a propylene unit in the second unit, and a ¹³ C-NMR spectrum (hexachloro) of the side chain methyl group of the propylene unit of the second unit in the third chain. Butadiene solution and tetramethylsilane as standard). At this time, when the total area of the peak appearing in 19.5 to 21.9 ppm (methyl carbon region) is 100%, the ratio (percentage) of the peak area appearing in 21.0 to 21.9 ppm (first region) ) Is obtained from the following formula (1).

  As described above, the propylene / 1-butene random copolymer (PBR) has a mm fraction of 85% or more and 97.5% or less, preferably 87% or more and 97% or less, more preferably as described above. It is 90% or more and 97% or less. In the present invention, it is important not to increase the mm fraction too much, and by providing a specific mm fraction, the melting point can be lowered with a relatively high propylene content. The propylene / 1-butene random copolymer (PBR) is composed of the following structures (iii), (iv) and (v) in addition to the above-described three-chain (i) and (ii) bonded to the head. ) And a peak derived from the side chain methyl group of the propylene unit due to such other bonds is also in the above methyl carbon region (19.5 to 5). 21.9 ppm).

  Among the methyl groups derived from the structures (iii), (iv) and (v), the methyl group carbon A and the methyl group carbon B resonate at 17.3 ppm and 17.0 ppm, respectively. The peak based on B does not appear in the first to third regions (19.5 to 21.9 ppm). Further, since both carbon A and carbon B are not involved in propylene trilinkage based on the head-to-tail bond, it is not necessary to consider in the above calculation of triad isotacticity (mm fraction).

The peak based on the methyl group carbon C, the peak based on the methyl group carbon D, and the peak based on the methyl group carbon D ′ appear in the second region, and the peak based on the methyl group carbon E and the peak based on the methyl group carbon E ′ are Appears in the third region.

  Therefore, in the 1st to 3rd methyl carbon regions, PPE-methyl group (side chain methyl group in propylene-propylene-ethylene chain) (around 20.7 ppm), EPE-methyl group (in ethylene-propylene-ethylene chain) Peaks based on (side chain methyl group) (around 19.8 ppm), methyl group C, methyl group D, methyl group D ′, methyl group E, and methyl group E ′ appear.

  Thus, in the methyl carbon region, peaks of methyl groups that are not based on the head-to-tail bond three linkages (i) and (ii) are also observed, but when obtaining the mm fraction by the above formula (1), Is corrected as follows.

  The peak area based on the PPE-methyl group can be obtained from the peak area of the PPE-methine group (resonant at around 30.6 ppm), and the peak area based on the EPE-methyl group is determined based on the EPE-methine group (around 32.9 ppm). Resonance) peak area.

The peak area based on the methyl group C can be determined from the peak area of the adjacent methine group (resonance near 31.3 ppm).
The peak area based on the methyl group D is ½ of the sum of the peak areas of the peaks based on the α, β-methylene carbon of the structure (iv) (resonant at around 34.3 ppm and around 34.5 ppm).
The peak area based on the methyl group D ′ can be obtained from the area of the peak (resonance around 33.3 ppm) based on the methine group adjacent to the methyl group of the methyl group E ′ in the structure (v). it can.

The peak area based on the methyl group E can be obtained from the peak area of the adjacent methine carbon (resonant at around 33.7 ppm), and the peak area based on the methyl group E ′ is determined at the adjacent methine carbon (around 33.3 ppm). Resonance) peak area.

  Therefore, by subtracting these peak areas from the total peak areas of the second region and the third region, it is possible to determine the peak area of the methyl group based on the head-to-tail three-linked propylene units (i) and (ii). it can.

  As described above, since the peak area of the methyl group based on the head-to-tail bonded propylene unit three chain (i) and (ii) can be evaluated, the mm fraction can be obtained according to the above formula (1).

Each carbon peak in the spectrum can be assigned with reference to literature (Polymer, 30, 1350 (1989)).
(5) The melting point (Tm) measured by a differential scanning calorimeter is 40 to 120 ° C, preferably 50 to 100 ° C, more preferably 55 to 90 ° C.

(6) The relationship between the melting point (Tm) and the 1-butene structural unit content M (mol%) is 146 exp (−0.022 M) ≧ Tm ≧ 125 exp (−0.032 M)
Preferably 146 exp (−0.024 M) ≧ Tm ≧ 125 exp (−0.032 M)
More preferably, 146exp (−0.0265M) ≧ Tm ≧ 125exp (−0.032M)
It is. When such a relationship between the melting point and the butene content is satisfied, the melting point can be lowered with a relatively high propylene content, whereby a high crystallization rate can be obtained even at a low melting point.

The propylene / 1-butene random copolymer (PBR) is preferably
(7) When the melting point is 75 ° C. or less, the crystallization rate (1/2 crystallization time) measured at 45 ° C. of the propylene / 1-butene random copolymer is 10 minutes or less, more preferably 7 minutes or less. .

Also preferably,
(8) The parameter B value indicating the randomness of the copolymerization monomer chain distribution of the propylene / 1-butene random copolymer (PBR) is 0.9 to 1.3, more preferably 0.95 to 1.25. Especially preferably, it is 0.95-1.2.

  This parameter B value has been proposed by Coleman et al. (BD Cole-man and TG Fox, J. Polym. Sci., Al, 3183 (1963)), and is defined as follows.

B = P ₁₂ / (2P ₁ · P ₂ )
Here, P ₁ and P ₂ are the first monomer and second monomer content fractions, respectively, and P ₁₂ is the ratio of (first monomer)-(second monomer) linkage in the chain in all two molecules.

The B value is 1 according to Bernoulli statistics, and the copolymer is block-like when B <1, is alternating when B> 1, and is a cross-copolymer when B = 2.
Further, the propylene / 1-butene random copolymer (PBR) has a structure containing a heterogeneous bond unit (position irregular unit) based on 2,1-insertion or 1,3-insertion of propylene present in a propylene chain. May have a small amount.

During polymerization, propylene is usually 1,2-inserted (methylene side is combined with the catalyst) to form a head-to-tail coupled propylene chain as described above, but rarely 2,1-inserted, or 1,3 -May be inserted. 2,1-inserted and 1,3-inserted propylene form regioregular units as shown in structures (iii), (iv) and (v) in the polymer. As for the proportion of 2,1-insertion and 1,3-insertion of propylene in the polymer structural unit, refer to Polymer, 30, 1350 (1989) using the ¹³ C-NMR spectrum in the same manner as the stereoregularity described above. In this case, the ratio of the position irregular units based on 2,1-insertion of propylene is shown.

  In addition, when it is difficult to obtain the area such as “Iαβ” in the formula (2) directly from the spectrum due to overlapping of peaks, it can be corrected with a carbon peak having a corresponding area.

  In the propylene / 1-butene random copolymer (PBR), the heterogeneous bond units based on 2,1-insertion of propylene present in the propylene chain obtained as described above are 0.01% in all propylene structural units. As mentioned above, specifically, it may be included at a ratio of about 0.01 to 1.0%.

  Moreover, the ratio of the position irregular unit based on 1,3-insertion of propylene in the propylene / 1-butene random copolymer (PBR) can be obtained from a βγ peak (resonance at around 27.4 ppm).

Further, the propylene / 1-butene random copolymer (PBR) may have a heterogeneous bond ratio of 0.05% or less based on 1,3-insertion of propylene.
Such a propylene / 1-butene random copolymer (PBR) can be produced by the method described in WO 2004/088775.

[Thermoplastic elastomer modified with functional groups (B)]
The thermoplastic elastomer (B) modified with the functional group described in the present invention is an α, β-monoethylenic polymer containing the functional group described below in the thermoplastic elastomer described above or a mixture of two or more thereof. It can be obtained by reacting a monomer having a saturated group and a copolymerizable monomer comprising a copolymerizable monomer, but there is no problem even if some of them do not react.

As the copolymerizable monomer comprising a monomer having an α, β-monoethylenically unsaturated group containing a functional group and other copolymerizable monomers used here, hydroxyethyl (meth) acrylate, hydroxy Hydroxyl-containing vinyls such as propyl (meth) acrylate, hydroxybutyl (meth) acrylate, lactone-modified hydroxyethyl (meth) acrylate, 2-hydroxy-3-phenoxypropyl acrylate, acrylic acid, methacrylic acid, maleic acid, itaconic acid , Ω-carboxy-polycaprolactone monoacrylate, carboxyl group-containing vinyls such as monohydroxyethyl phthalate, nitrogen compounds such as acrylamide, methacrylamide, methylolacrylamide, methylolmethacrylamide, anhydrous maleic , Include carboxylic anhydrides such as citraconic anhydride, it alone, can be used even more. The addition amount of the copolymerizable monomer comprising the above-mentioned functional group-containing monomer having an α, β-monoethylenically unsaturated group and other copolymerizable monomers is 0.5 to 20 in the thermoplastic elastomer. It is in the range of wt%, more preferably 1 to 15 wt%.

Moreover, description like the methyl (meth) acrylate described here shows methyl acrylate and methyl methacrylate.
The thermoplastic elastomer (B) modified with the above functional group can be obtained by various methods. For example, the thermoplastic elastomer (A) and α, β-monoethylenic acid in the organic solvent (G) described later. A method of reacting a copolymerizable monomer comprising a monomer having an unsaturated group and other copolymerizable monomers in the presence of a polymerization initiator, or a melt obtained by heating and melting the thermoplastic elastomer (A) A method of reacting a monomer having a α, β-monoethylenically unsaturated group and a copolymerizable monomer and a polymerization initiator with stirring, a thermoplastic elastomer ( A mixture of a copolymerizable monomer comprising a monomer having an α, β-monoethylenically unsaturated group and other copolymerizable monomers and a polymerization initiator is supplied to an extruder and heated and kneaded. While reacting It can be mentioned method and the like.

[Resin having urethane bond (C)]
Examples of the component constituting the resin (C) having a urethane bond used in the present invention include polyfunctional isocyanate compounds such as ethylene diisocyanate, trimethylene diisocyanate, tetramethylene diisocyanate, hexamethylene diisocyanate, and octamethylene diisocyanate. Aliphatic polyisocyanates such as various aliphatic polyisocyanates, isophorone diisocyanate, bis (isocyanatomethyl) cyclohexane, 4,4′-dicyclohexylmethane-diisocyanate, phenylene diisocyanate, tolylene diisocyanate, 4,4′-diisocyanate, etc. Aromatic polyisocyanates, sulfur-containing aliphatic isocyanates such as thiodiethyl diisocyanate, diphenyl sulfide-2,4′-diisocyanate Aromatic sulfide-based isocyanates such as diphenyl disulfide-4,4'-diisocyanate, aromatic disulfone-based isocyanates such as diphenylsulfone-4,4'-diisocyanate, 4-methyl-3 -Isocyanatobenzenesulfonyl-4'-isocyanatophenol ester and other sulfonate ester isocyanates, 4,4'-dimethylbenzenesulfonyl-ethylenediamine-4,4'-diisocyanate and other aromatic sulfonic acid amide isocyanates, And sulfur-containing heterocyclic compounds such as thiophene-2,5-diisocyanate.

  In addition, these alkyl-substituted products, alkoxy-substituted products, nitro-substituted products, prepolymer-modified products with polyhydric alcohols, carbodiimide-modified products, urea-modified products, burette-modified products, dimerization or trimerization reaction products are also used. However, polyfunctional isocyanate compounds other than the above compounds may be used. Moreover, these polyfunctional isocyanate compounds can also be used by 1 type, or 2 or more types of mixtures.

Of the above compounds, the obtained resin, and the yellowing resistance, thermal stability, and light stability of the film after coating it to form a film, or the availability of a polyfunctional isocyanate compound From these, aliphatic polyisocyanates and alicyclic polyisocyanate compounds are preferred, among which hexamethylene diisocyanate, isophorone diisocyanate, 4,4′-dicyclohexylmethane diisocyanate, 2,5-bisisocyanatomethylnorbornane, 2,6-bis. Isocyanatomethylnorbornane and derivatives thereof are particularly preferred.

  In addition, as an active hydrogen compound having at least two active hydrogen groups capable of reacting with a polyfunctional isocyanate compound, which is a component constituting the resin (C) having a urethane bond used in the present invention, For example, the following may be mentioned. Various polyol compounds include aliphatic polyols such as ethylene glycol, propylene glycol, pentaerythritol and sorbitol, aromatic polyols such as dihydroxynaphthalene and trihydroxynaphthalene, halogenated polyols such as dibromoneopentyl glycol, polyester polyol, polyethylene glycol , Polyether polyols, polythioether polyols, condensation products of organic acids such as oxalic acid and adipic acid and the polyols, addition reaction products of the polyols with alkylene oxides such as ethylene oxide and propylene oxide, alkylene Addition reaction product of polyamine and alkylene oxide, 2,2-dimethylollactic acid, 2,2-dimethylolpropionic acid, caprolactone modified product, - mercaptoethanol, 3-mercapto-1,2-propanediol. In addition, polyamino compounds such as ethylenediamine and diethylenetriamine, and α-amino acids such as serine, lysine and histidine can also be used.

  Further, the resin (C) having a urethane bond used in the present invention may contain a carboxyl group, a sulfonyl group and an ethylene oxide group in the molecule. Examples of constituents for introducing these atomic groups include 2,2-dimethylol lactic acid, 2,2-dimethylol propionic acid, 2,2-dimethylol butanoic acid, 2,2-dimethylol valeric acid, 3,4- Examples include, but are not limited to, diaminobutanesulfonic acid, 3,6-diamino-2-toluenesulfonic acid, polyethylene glycol, polyaddition product of ethylene oxide and propylene oxide, and a polymer of ethylene glycol and the active hydrogen compound. It is not something.

  Although the manufacturing method of resin (C) which has a urethane bond is not restrict | limited in particular, For example, the following methods are mentioned as an example. For example, a polyfunctional isocyanate compound, a compound having an active hydrogen group capable of reacting with an isocyanate group in the active hydrogen compound, an active hydrogen group capable of reacting with an isocyanate group in the compound, and a carboxyl in the molecule At least one compound having a group, a sulfonyl group or an ethylene oxide group, in an equivalent ratio such that an isocyanate group is excessive, or an equivalent ratio such that an active hydrogen group is excessive or in the presence of a suitable organic solvent or There is a method for producing a resin having a urethane bond in the molecule by reacting in the absence.

Although it does not specifically limit as a solvent used when obtaining the resin (C) which has the said urethane bond, The solvent described in the organic solvent (G) can be used.
[Organic solvent (G)]
Examples of the organic solvent (G) used in the present invention include aromatic hydrocarbons such as xylene, toluene, and ethylbenzene, aliphatic hydrocarbons such as hexane, heptane, octane, and decane, and alicyclic groups such as cyclohexane, cyclohexene, and methylcyclohexane. Organic solvents such as hydrocarbons, ethyl acetate, n-butyl acetate, cellosolve acetate, propylene glycol monomethyl ether acetate, propylene glycol monoethyl ether acetate, esters such as 3 methoxybutyl acetate, ketone solvents such as methyl ethyl ketone and methyl isobutyl ketone Or a mixture of two or more of these may be used. Among these, aromatic hydrocarbons can be preferably used.

[Reaction of thermoplastic elastomer (A) and / or thermoplastic elastomer (B) modified with functional group and resin (C) having urethane bond]
The reaction between the thermoplastic elastomer (A) and / or the thermoplastic elastomer (B) modified with a functional group and the resin (C) having a urethane bond is not particularly limited. In an organic solvent, the thermoplastic elastomer (A) and / or the thermoplastic elastomer (B) modified with a functional group and the resin (C) having a urethane bond are mixed, and at a high temperature and / or a high pressure, There is a method of generating a radical and performing a reaction.

In the present invention, the radical generating method in the case of carrying out the reaction by generating a radical is not particularly limited, but a known method such as a method of adding an organic peroxide can be used.
Examples of the organic peroxide include di-tert-butyl peroxide, tert-butylperoxy-2-ethylhexanoate, benzoyl peroxide, dicumylperper having a tert-butyl group and / or a benzyl group in the molecule. Examples thereof include oxide, tert-butyl peroxybenzoate, lauroyl peroxide, cumene hydroperoxide and the like. These can be used alone or in admixture of two or more.

  In the present invention, among the above-mentioned organic peroxides, di-tert-butyl peroxide and tert-butyl peroxy-2-ethylhexanoate are more preferably used. That is, an organic peroxide having a tert-butyl group and / or a benzyl group in the molecule has a relatively high hydrogen abstraction ability, and has an effect of improving the graft ratio with polyolefin.

  The organic peroxide is used in a total weight of 100 weight of the thermoplastic elastomer (A) and / or the thermoplastic elastomer (B) modified with a functional group and the resin (C) having a urethane bond. When used in a range of usually 2 to 50% by weight, more preferably 3 to 30% by weight, a great effect on stability appears. In this case, when the amount of the organic peroxide used is less than 2% by weight, the resulting composition is poorly stable in the solvent. Since the adhesiveness to the material due to gelation or molecular weight reduction is inferior, it is preferable to use an organic peroxide within the above range. Moreover, it is preferable to add this organic peroxide little by little as much as possible. That is, depending on the amount used, in general, when the organic peroxide is added all at once, the reaction solution is relatively easily gelled. It is preferable to add in small portions separately.

[Reaction between functional group of thermoplastic elastomer (B) modified with functional group and functional group of resin (C) having urethane bond]
The reaction between the functional group of the thermoplastic elastomer (B) modified with the functional group and the functional group of the resin (C) having a urethane bond is not particularly limited. For example, a carboxyl group is added to (B). A method of mixing and containing a hydroxyl group or an isocyanate group at the end of (C) and reacting under heating, or (B) containing a hydroxyl group and containing an isocyanate group at the end of (C) A method of mixing and reacting under heating, or (B) containing an acid anhydride group, and reacting with an alcohol or resin containing two or more hydroxyl groups in the molecule to contain a hydroxyl group Then, the method of mixing what contains an isocyanate group at the terminal of (C) and reacting under heating, the method of reacting the thermoplastic elastomer (B) having an active hydrogen group with a polyfunctional isocyanate compound, etc. In addition, there is a method of synthesizing a urethane resin by reacting the raw material monomer of (C) in the presence of (B) containing the carboxy group or hydroxyl group, and modifying the latter. This is preferable from the viewpoint of storage stability.

  In addition, the ratio of the thermoplastic elastomer (A) and / or the thermoplastic elastomer (B) modified with a functional group and the resin (C) having a urethane bond from the viewpoint of water dispersibility and adhesion to the substrate. Is a weight ratio of [(A) and / or (B)] / (C) = 10/90 to 95/5, preferably 20/80 to 80/20.

[Production of water dispersion]
The method for producing an aqueous dispersion of the present invention includes a thermoplastic elastomer (A) and / or a thermoplastic elastomer (B) modified with a functional group and urethane in the presence or absence of an organic solvent (G). A mixture of a resin having a bond (C), a thermoplastic elastomer (A) and / or a thermoplastic elastomer (B) modified with a functional group and a resin having a urethane bond (C), With or without the addition of the hydrophilic solvent (J) to the product obtained by reacting the functional group of the thermoplastic elastomer (B) modified with the functional group with the functional group of the resin (C) having a urethane bond, A method of removing the organic solvent (G) after forcibly emulsifying with a homomixer or the like in the presence of the surfactant (H), or in the presence or absence of the organic solvent (G), the thermoplastic elastomer (A) and A mixture of a thermoplastic elastomer (B) modified with a functional group and a resin (C) having a urethane bond, a thermoplastic elastomer (A) and / or a thermoplastic elastomer modified with a functional group (B ) And a resin (C) having a urethane bond, or a functional group of a thermoplastic elastomer (B) modified with a functional group and a functional group of a resin (C) having a urethane bond. , (B), (C) containing a carboxyl group, or having a carboxyl group remaining in the molecular chain, with or without adding a hydrophilic solvent (J) (I) is mixed to neutralize a part or all of it, and after adding water, the organic solvent (G) is removed, or the neutralization and forced emulsification are both carried out to form an aqueous system. Raised It is.

  The particle size of the aqueous dispersion (dispersed particles) is preferably in the range of 10 nm to 10 μm. If the particle size is too small, the adhesiveness is lowered, and if too large, the storage stability is not preferred.

[Surfactant (H)]
Examples of the surfactant (H) used in the present invention include alkyl naphthalene sulfonate, sodium dodecylbenzene sulfonate, sodium lauryl sulfate, sodium salt of formaldehyde condensate, sodium alkyldiphenyl ether disulfonate, sodium melanin resin sulfonate. , Special polyacrylate, potassium oleate, olefin / maleic acid copolymer, carboxymethylcellulose sodium salt, potassium stearate, sodium stearate, stearic acid triethanolamine and other anionic surfactants, fatty acid monoglyceride, sorbitan fatty acid ester, Polyglycerin fatty acid partial ester, polyoxyethylene alkylphenyl ether, polyoxyethylene sorbitan fatty acid partial ester, Nonionic series such as reoxyethylene sorbitol fatty acid partial ester, polyoxyethylene glycerin fatty acid partial ester, polyoxyethylene fatty acid amine, polyoxyethylene (hardened) castor oil, polyoxyethylene glycol fatty acid ester, hydroxyethyl cellulose, polyvinyl alcohol, and methyl cellulose Examples include surfactants, alkylammonium chloride, trimethylalkylammonium bromide, amphoteric surfactants such as alkylpyridinium chloride and casein, and water-soluble polyvalent metal salts, etc., alone or in combination of two or more. Can be used.

[Basic substance (I)]
Examples of the basic substance (I) used in the present invention include alkali metals such as sodium, potassium and calcium, inorganic amines such as hydroxylamine, ammonium hydroxide and hydrazine, ammonia, methylamine, ethylamine, ethanolamine and morpholine. Organic metal, sodium oxide, sodium peroxide, potassium oxide, calcium oxide, strontium oxide, sodium hydroxide, potassium hydroxide, calcium hydroxide, alkali metal and alkaline earth metal oxides, hydroxides, hydrogen And weak salts of alkali metals and alkaline earth metals such as sodium carbonate, potassium carbonate, sodium hydrogen carbonate, potassium hydrogen carbonate, calcium hydrogen carbonate, sodium acetate, potassium acetate and calcium acetate. Or two or more Can be mixed and used.

[Hydrophilic solvent (J)]
Examples of the hydrophilic solvent (J) used in the present invention include alcohols such as ethanol, isopropanol and butanol, glycols such as ethylene glycol monoethyl ether, ethylene glycol monoisopropyl ether and ethylene glycol monobutyl ether, methyl cellosolve, ethyl cellosolve and butyl cellosolve. Cellosolve such as cellosolve acetate can be used, and one kind can be used alone, or two or more kinds can be mixed and used.

  In the present invention, in addition to the thermoplastic elastomer and the resin having a urethane bond, the petroleum hydrocarbon resin (D) and / or the rosin resin (E) and / or the terpene resin (F) are contained in the same particle (dispersed particle). Can be contained. For example, a mixture of a thermoplastic elastomer (A) and / or a thermoplastic elastomer (B) modified with a functional group and a resin (C) having a urethane bond in the presence or absence of an organic solvent (G) Or a product obtained by reacting a thermoplastic elastomer (A) and / or a thermoplastic elastomer (B) modified with a functional group and a resin (C) having a urethane bond, or a thermoplastic elastomer modified with a functional group (B ) And the functional group of the resin (C) having a urethane bond, mixed under heating, and forcibly emulsified with a homomixer in the presence of water and a surfactant (H), and then an organic solvent. A method of removing (G), a thermoplastic elastomer (A) and / or a thermoplastic elastomer (B) modified with a functional group in the presence or absence of an organic solvent (G); What mixed resin (C) which has a retane bond, what reacted thermoplastic elastomer (A) and / or the thermoplastic elastomer (B) modified by the functional group, and resin (C) which has a urethane bond, , A functional group of a thermoplastic elastomer (B) modified with a functional group and a functional group of a resin (C) having a urethane bond, wherein at least one of (B) and (C) has a carboxyl group. Contains at least one of the petroleum hydrocarbon resin (D) and / or the rosin resin (E) and / or the terpene resin (F) that contains a carboxyl group in the molecular chain, or is mixed. With or without the hydrophilic solvent (J) added to the one containing a carboxyl group, the basic substance (I) was mixed to neutralize part or all of it, and water was added. A method of removing the organic solvent (G), a method, and the like to water by being both carried out forced emulsification and neutralization of the.

  Further, a petroleum-based hydrocarbon resin (D) and / or a rosin-based resin (E) and / or a terpene-based resin is added to an aqueous dispersion in which a thermoplastic elastomer and a resin having a urethane bond are contained in the same particle (dispersed particle). The aqueous dispersion (F) can also be mixed and used.

[Petroleum hydrocarbon resin (D)]
Examples of the petroleum hydrocarbon resin (D) used in the present invention include an aliphatic petroleum resin whose main raw material is a C5 fraction of tar naphtha, an aromatic petroleum resin whose main raw material is a C9 fraction, and their Copolymeric alicyclic. C5 petroleum resin (resin obtained by polymerizing C5 fraction of naphtha cracked oil), C9 petroleum resin (resin obtained by polymerizing C9 fraction of naphtha cracked oil), C5C9 copolymerized petroleum resin (C5 fraction of naphtha cracked oil) C9 fraction copolymerized resin), styrene, indene, coumarone, coumarone indene resin containing dicyclopentadiene, etc., and condensation of ρ-tertiarybutylphenol and acetylene. Examples thereof include alkylphenol resins typified by products, xylene resins obtained by reacting o-xylene, ρ-xylene, and m-xylene with formalin. These can be used alone or in combination of two or more. Among these, petroleum hydrocarbon resins having a weight average molecular weight of 1,000 to 50,000 as measured by GPC are preferable, and 1,500 to 30,000 are particularly preferable. Moreover, what has a polar group in these resin is still more preferable.

[Rosin resin (E)]
Examples of the rosin resin (E) used in the present invention include modified rosin modified with natural rosin, polymerized rosin, maleic acid, fumaric acid, (meth) acrylic acid and the like. Examples of the rosin derivative include esterified products, phenol-modified products and esterified products of the above rosins, and hydrogenated products thereof can also be mentioned.

[Terpene resin (F)]
Examples of the terpene resin (F) used in the present invention include resins comprising α-pinene, β-pinene, limonene, dipentene, terpene phenol, terpene alcohol, terpene aldehyde, and the like. Α-pinene, β-pinene, Examples thereof include aromatic-modified terpene resins obtained by polymerizing aromatic monomers such as styrene on limonene, dipentene, and the like, and hydrogenated products thereof can also be mentioned. Among these, terpene phenol resins, aromatic modified terpene resins, and hydrogenated products thereof are preferable.

  The present invention provides a petroleum hydrocarbon resin (D) to a resin obtained by reacting a thermoplastic elastomer (A) and / or a thermoplastic elastomer (B) modified with a functional group and a resin (C) having a urethane bond. ) And / or rosin-based resin (E) and / or terpene-based resin (F) are added in terms of adhesion to the base material from the viewpoint of adhesiveness to the thermoplastic elastomer (A) and / or functional group. The petroleum-based hydrocarbon resin (D) and / or rosin-based resin (30 to 100 parts by weight of the resin obtained by reacting the thermoplastic elastomer (B) modified with the resin having a urethane bond (C) with E) and / or terpene resin (F) is 0 to 70 parts by weight, [(A) and / or (B)], (C), [(D) and / or (E) and / or ( F)] is 100 layers Consisting of parts.

Furthermore, at least 1 or more chosen from the group which consists of fats and oils and derivatives of fats and oils can be used for the said resin.
Examples of the fats and oils include linseed oil, soybean oil, castor oil, and purified products thereof.

  As the derivatives of fats and oils, short oil alkyd resins, medium oil alkyd resins modified with fats (fatty acids) of polybasic acids such as phthalic anhydride and polyhydric alcohols such as glycerin, pentaerythritol, and ethylene glycol as a skeleton, Long oil alkyd resin or the like, or rosin modified alkyd resin modified with natural resin, synthetic resin and polymerizable monomer, phenol modified alkyd resin, epoxy modified alkyd resin, acrylated alkyd resin, urethane modified alkyd resin, etc. .

  The above fats and oils and derivatives of fats and oils can be used alone or in combination of two or more. The addition amount is usually 0.5 to 40% by weight, preferably 2 to 30% by weight, based on the resin component.

Among the aqueous dispersions of the present invention, a curing agent capable of reacting with active hydrogen and / or hydroxyl group can be used for the aqueous dispersion having active hydrogen and / or hydroxyl group.
For example, a main agent containing an aqueous dispersion having active hydrogen and / or a hydroxyl group, and a curing agent having an isocyanate group in the molecule are mixed with a curing agent capable of reacting with active hydrogen and / or a hydroxyl group. Thus, it can be used as a coating material having a urethane bond, a paint, a primer, or an adhesive. Examples of the curing agent include Takenate WB series (made by Mitsui Takeda Chemical Co., Ltd.), Elastron BN in which an isocyanate group is treated with a blocking agent such as oximes, lactams, and phenols in water. Series (Daiichi Kogyo Seiyaku Co., Ltd.) etc. are mentioned.

A resin synthesized from at least one of melamine, urea, benzoguanamine, glycoluril, and formaldehyde and formaldehyde, for example, a part of a methylol group by a lower alcohol such as methanol, ethanol, propanol, isopropanol, butanol, isobutanol, etc. Alternatively, amino resins which are all alkyl etherified can also be used as the curing agent.

  Furthermore, an oxazoline compound can also be used as a curing agent. Examples of the curing agent include 2-vinyl-2-oxazoline, 2-vinyl-4-methyl-2-oxazoline, 2-vinyl-5-methyl-2-oxazoline, 2-isopropenyl-2-oxazoline, 2- Examples thereof include isopropenyl-4-methyl-2-oxazoline.

The aqueous dispersion of the present invention and the curing agent capable of reacting with active hydrogen and / or hydroxyl group can be used in an arbitrary ratio.
When the curing agent capable of reacting with active hydrogen and / or a hydroxyl group is a curing agent having an isocyanate group, the mixing ratio is 95 / weight ratio of the solid of the aqueous dispersion / the curing agent having an isocyanate group of the present invention. It is preferably used in the range of 5 to 10/90, more preferably in the range of 90/10 to 20/80.

  Further, when the curing agent capable of reacting with active hydrogen and / or hydroxyl group is an amino resin, the weight ratio of the aqueous dispersion / amino resin solid of the present invention is 95/5 to 20/80. The range of 90/10 to 60/40 is more preferable.

  Furthermore, when the curing agent capable of reacting with active hydrogen and / or hydroxyl group is an oxazoline compound, the weight ratio of the aqueous dispersion / amino resin solid of the present invention is used in the range of 95/5 to 20/80. Is preferable, and the range of 90/10 to 60/40 is more preferable.

The mixture of the curing agents described above can be coated and cured as it is, but a reactive catalyst can be used in combination as necessary.
In addition, if necessary, lubricity-imparting agents (for example, synthetic wax, natural wax, etc.), crosslinking agents, film-forming aids, leveling agents, viscoelasticity adjusting agents, wetting agents, flame retardants (for example, ammonium polyphosphate) Phosphorus-containing resins such as phosphate esters, melamine, zinc borate, magnesium hydroxide, etc.), stabilizers, rust inhibitors, fungicides, UV absorbers, weathering stabilizers, heat stabilizers, antioxidants, Foaming agent, antifoaming agent, wetting agent, coagulant, gelling agent, anti-aging agent, softening agent, plasticizer, flavoring agent, anti-sticking agent, mold release agent, anti-settling agent, antioxidant, antistatic Additives such as additives, conductivity imparting agents (eg, carbon black, ferrite), dyes, pigments, fillers, organic solvents, oils (eg, mineral lubricating oils, mineral oils, synthetic oils, vegetable oils) You may add in the range which does not impair the objective of invention. These additives may be used alone or in combination of two or more.

  The coating method of the aqueous dispersion of the present invention or a mixture of the aqueous dispersion of the present invention mixed with a curing agent capable of reacting with active hydrogen and / or a hydroxyl group is not particularly limited, but is preferably performed by spray coating. Yes, for example, it can be applied by spraying onto the surface to be coated with a spray gun. The application can usually be carried out easily at room temperature, and the drying method after application is not particularly limited, and it can be dried by an appropriate method such as natural drying or heat forced drying.

In addition, the water dispersion of the present invention or the water dispersion of the present invention mixed with a curing agent capable of reacting with active hydrogen and / or a hydroxyl group is characterized by polyolefins such as polyethylene and polypropylene, and ethylene-propylene copolymer. Molded products composed of olefin copolymers such as polymers, ethylene-butene copolymers, propylene-butene copolymers, ethylene-propylene-butene copolymers, molded products composed of polypropylene and rubber components, polyamide resins, It can be suitably used as a coating material such as saturated polyester, polycarbonate, epoxy resin, urethane resin, steel plate, electrodeposition-treated steel plate, paint, primer, or adhesive. In addition, paints mainly composed of urethane paints, polyester paints, melamine paints, and epoxy paints can be used for the top coating, improving the adhesion to the surface of various objects to be coated, and improving the vividness. It can also be used to form a coating film.

  And what mixed the active hydrogen and / or the hardening | curing agent which can react with a hydroxyl group in the water dispersion of this invention or the water dispersion of this invention is metal, polyolefin, or metal and polyolefin from the characteristic. As an adhesive such as a heat sealant, the coating film has no stickiness and exhibits excellent adhesion performance and adhesion performance. In heat sealing, it is a coating agent that exhibits its performance at low temperatures. These can also be used as an adhesive for PTP packaging and an adhesive for laminating.

  In addition to the above, the water dispersion of the present invention, or the mixture of the water dispersion of the present invention mixed with a curing agent capable of reacting with active hydrogen and / or a hydroxyl group, has an aqueous epoxy resin and an aqueous acrylic resin. , Aqueous urethane resins, aqueous polyesters, aqueous alkyd resins, paints containing these resins, and the like can be mixed and used.

Furthermore, when a propylene / 1-butene copolymer is used as the thermoplastic elastomer (A), the resulting aqueous dispersion is more excellent in adhesion, and further, a propylene / 1-butene random copolymer (PBR). ), The resulting aqueous dispersion is further excellent in adhesiveness. 〔Example〕
Hereinafter, the manufacturing method and various test examples of the aqueous dispersion of the present invention will be described and further described. In the following, parts and percentages are by weight unless otherwise specified.

(Production Example 1)
A 2 liter autoclave thoroughly purged with nitrogen was charged with 900 cm ^{3 of} hexane and 90 g of 1-butene, 1 mmol of triisobutylaluminum was added, the temperature was raised to 70 ° C., and then propylene and ethylene were supplied to bring the total pressure to 0 .69 MPaG, 0.30 mmol of methylaluminoxane, 0.001 mmol of rac-dimethylsilylene-bis {1- (2-methyl-4-phenylindenyl)} zirconium dichloride in terms of Zr atom was added, and propylene was continuously added. The polymerization was carried out for 30 minutes while maintaining the total pressure at 0.69 MPaG. After the polymerization, the polymer was deaerated and the polymer was recovered in a large amount of methanol, and dried under reduced pressure at 110 ° C. for 12 hours to obtain 39.7 g of a thermoplastic elastomer. The polymerization activity was 79 kg · polymer / mmol Zr · hr.

(Production Example 2)
In a four-necked flask equipped with a stirrer, thermometer, reflux condenser, and nitrogen introduction tube, 60 parts of toluene, 46.3 parts of PTG2000 (trade name, manufactured by Hodogaya Chemical Co., Ltd.), 1,6-hexane 1.2 parts of diol, 3.1 parts of 2,2-dimethylolbutanoic acid, 9.3 parts of 1,6-hexamethylene diisocyanate, 0.09 part of dibutyltin laurate were charged at 90 ° C. in a nitrogen gas atmosphere. It was made to react for 8 hours and the urethane resin solution was obtained.

(Production Example 3)
In a four-necked flask equipped with a stirrer, thermometer, reflux condenser, and nitrogen inlet tube, 60 parts of toluene, 42.2 parts of PTG2000 (trade name, manufactured by Hodogaya Chemical Co., Ltd.), 1,6-hexane 0.75 parts of diol, 5.7 parts of 2,2-dimethylolbutanoic acid, 11.4 parts of 1,6-hexamethylene diisocyanate and 0.11 part of dibutyltin laurate were charged at 90 ° C. in a nitrogen gas atmosphere. It was made to react for 8 hours and the urethane resin solution was obtained.

(Production Example 4)
In a four-necked flask equipped with a stirrer, thermometer, reflux condenser, and nitrogen inlet tube, 60 parts of toluene, 44.1 parts of PTG2000, 1.2 parts of 1,6-hexanediol, 2,2-diethyl 3.7 parts of methylol butanoic acid, 11.1 parts of 1,6-hexamethylene diisocyanate and 0.11 part of dibutyltin laurate were charged and reacted at 90 ° C. for 8 hours in a nitrogen gas atmosphere to obtain a urethane resin solution. It was.

(Production Example 5)
In a four-necked flask equipped with a stirrer, thermometer, reflux condenser, and nitrogen inlet tube, 60 parts of toluene, 39.2 parts of PTG2000, 0.6 parts of 1,6-hexanediol, 2,2-diethyl 6.7 parts of methylol butanoic acid, 13.5 parts of 1,6-hexamethylene diisocyanate and 0.13 part of dibutyltin laurate were charged and reacted at 90 ° C. for 8 hours in a nitrogen gas atmosphere to obtain a urethane resin solution. It was.

(Production Example 6)
A four-necked flask equipped with a stirrer, thermometer, reflux cooling device, and nitrogen inlet tube was charged with 300 parts of hexane and 300 parts of petroleum resin (manufactured by Mitsui Chemicals, Hilets T-480X), and heated under reflux. Dissolved. 500 parts of this solution, 250 parts of ion-exchanged water, and 1.5 parts of sodium dodecylbenzenesulfonate (manufactured by Kao Corporation, Neopelex F-25) were mixed and stirred at a rotational speed of 10,000 rpm for 15 minutes. Next, 0.7 part of polyacrylic acid (manufactured by Wako Pure Chemical Industries, Ltd., Hibiswaco 304) was added and mixed by stirring to obtain an emulsion. The hexane in this emulsion was distilled off under reduced pressure using an evaporator to obtain an aqueous dispersion of petroleum hydrocarbon resin (D) having a solid content of 50%.

(Production Example 7 (synthesis of PBR-1))
In a 2000 ml polymerization apparatus sufficiently purged with nitrogen, 900 ml of dry hexane, 60 g of 1-butene and triisobutylaluminum (1.0 mmol) were charged at room temperature, and then the internal temperature of the polymerization apparatus was raised to 70 ° C. with propylene. Pressurized to 0.7 MPa. Next, a toluene solution in which 0.002 mmol of dimethylmethylene (3-tert-butyl-5-methylcyclopentadienyl) fluorenylzirconium dichloride and 0.6 mmol of methylaluminoxane (produced by Tosoh Finechem) in contact with aluminum were contacted. Was added to the inside of the polymerization vessel and polymerized for 30 minutes while maintaining an internal temperature of 70 ° C. and a propylene pressure of 0.7 MPa, and 20 ml of methanol was added to terminate the polymerization. After depressurization, the polymer was precipitated from the polymerization solution in 2 L of methanol and dried under vacuum at 130 ° C. for 12 hours. The obtained polymer (PBR-1) was 9.2 g. The melting point of the polymer was 80.6 ° C., and the intrinsic viscosity [η] was 1.18 dl / g. Table 2 shows the measured physical properties of the obtained polymer.

(Production Example 8 (synthesis of PBR-2))
817 ml of hexane, 50 g of 1-butene, dimethylmethylene (3-tert-butyl-5-methylcyclopentadienyl) fluorenylzirconium dichloride and diphenylmethylene (3-tert-butyl-5-methylcyclopentadiene) Polymerization was carried out in the same manner as in Production Example 7 except that it was changed to (enyl) 2,7-di-tert-butylfluorenylzirconium dichloride. The obtained polymer was 11.5 g. Further, the melting point of the polymer was 86.3 ° C., and the intrinsic viscosity [η] was 2.11 dl / g. Table 2 shows the measured physical properties of the obtained polymer (PBR-2).

(Production Example 9 (synthesis of PBR-3))
Polymerization was carried out in the same manner as in Production Example 7, except that hexane was charged in 800 ml, 1-butene was 120 g, and the polymerization vessel internal temperature was 60 ° C. The obtained polymer was 10.8 g. Further, the melting point of the polymer was 69.0 ° C., and the intrinsic viscosity [η] was 2.06 dl / g. The physical properties measured for the obtained polymer (PBR-3) are shown in Table 2. The physical properties of the propylene / 1-butene random copolymer (PBR) in Production Examples 7 to 9 were measured as follows.
<1-butene content>
^It calculated | required using < ¹³ > C-NMR.
<Intrinsic viscosity [η]>
Measured in 135 ° C decalin and expressed in dl / g.
<Molecular weight distribution (Mw / Mn)>
The molecular weight distribution (Mw / Mn) was measured as follows using GPC-150C manufactured by Millipore.

The separation column is TSK GNH HT, the column size is 27 mm in diameter and 600 mm in length, the column temperature is 140 ° C., the mobile phase is o-dichlorobenzene (Wako Pure Chemical Industries) and BHT ( (Takeda Pharmaceutical Co., Ltd.) was used at 0.025% by weight, moved at 1.0 ml / min, the sample concentration was 0.1% by weight, the sample injection amount was 500 microliters, and a differential refractometer was used as the detector. The standard polystyrene used was manufactured by Tosoh Corporation for molecular weights of Mw <1000 and Mw> 4 × 10 ⁶ , and used by Pressure Chemical Co. for 1000 ≦ Mw ≦ 4 × 10 ⁶ .
<B value>
The B value is a ¹³ C-NMR spectrum of a sample in which about 200 mg of copolymer is uniformly dissolved in 1 ml of hexachlorobutadiene in a 10 mmφ sample tube, usually at a measurement temperature of 120 ° C., a measurement frequency of 25.05 MHz, Measurement was performed under the measurement conditions of a spectral width of 1500 Hz, a filter width of 1500 Hz, a pulse repetition time of 4.2 sec., And an integration number of 2000 to 5000. From this spectrum, P ₁ , P ₂ , P ₁₂ (P ₁ is the ethylene content fraction) , P ₂ is 1-butene content fraction, P ₁₂ is in in the chain all bimolecular (ethylene) - was calculated by determining the (1-butene), the amount of the chain).
<Triad Isotactic City>
The ¹³ C-NMR spectrum was measured with a hexachlorobutadiene solution (based on tetramethylsilane), and the area of the peak appearing at 21.0 to 21.9 ppm relative to the total area (100%) of the peak appearing at 19.5 to 21.9 ppm. The ratio (%) was obtained.
<Percentage of heterogeneous bonds based on 2,1-insertion>
Polymer, 30, 1350 (1989) was used as a reference, and was determined using the ¹³ C-NMR spectrum by the method described above.
<Melting point (Tm)>
About 5 mg of sample is packed in an aluminum pan, heated to 200 ° C. at 10 ° C./minute, held at 200 ° C. for 5 minutes, then cooled to room temperature at 20 ° C./minute, and then endothermic when heated at 10 ° C./minute. Obtained from the curve. For the measurement, a DSC-7 type apparatus manufactured by Perkin Elmer was used.
<Crystallinity>
It was determined by X-ray diffraction measurement of a 1.0 mm thick press sheet that had passed at least 24 hours after molding.
<Crystalization rate>
Using the DSC apparatus, the ½ crystallization time at 45 ° C. was determined.

Example 1
A four-necked flask equipped with a stirrer, a thermometer, a reflux cooling device, and a nitrogen introduction tube was charged with 140 parts of best plast 792 and 700 parts of toluene as a thermoplastic elastomer, heated and dissolved, and then obtained in Production Example 2. 200 parts of a urethane resin solution was slowly added over 1 hour. To this, 2 g of sodium dodecylbenzenesulfonate and 500 parts of ion-exchanged water were mixed and stirred at a rotational speed of 10,000 rpm for 15 minutes to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure using an evaporator to obtain an aqueous dispersion having a solid content of 40% and a particle size of 0.5 μm.
(Example 2)
In a pressurized reaction vessel, 140 parts of Bestplast 792 and 700 parts of toluene were charged and dissolved by heating. 46.3 parts of PTG2000, 1.2 parts of 1,6-hexanediol, and 2,2-dimethylolbutanoic acid were added. 3.1 parts, 9.3 parts of 1,6-hexamethylene diisocyanate and 0.09 part of dibutyltin laurate were charged and reacted at 90 ° C. for 8 hours in a nitrogen gas atmosphere. The obtained polymer was heated to 140 ° C. in a pressure reaction vessel, and 1.0 part of di-tert-butyl peroxide was added dropwise over 2 hours, and held at 140 ° C. for 2 hours. This was cooled to 60 ° C., 2 g of sodium dodecylbenzenesulfonate and 500 parts of ion-exchanged water were mixed, and stirred for 15 minutes at a rotational speed of 10,000 rpm to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 3)
A four-necked flask equipped with a stirrer, a thermometer, a reflux cooling device, and a nitrogen inlet tube was charged with 140 parts of best plast 792 and 700 parts of toluene as a thermoplastic elastomer, heated and dissolved, and then obtained in Production Example 3. 200 parts of a urethane resin solution was slowly added over 1 hour. This was cooled to 60 ° C., 4.26 parts of triethylamine was added and stirred for 30 minutes, and 300 parts of ion-exchanged water was further added and stirred for 30 minutes to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
Example 4
In a pressurized reaction vessel, 140 parts of Bestplast 792 and 700 parts of toluene are charged, dissolved by heating, 42.2 parts of PTG2000, 0.75 part of 1,6-hexanediol, and 2,2-dimethylolbutanoic acid. 5.7 parts, 11.4 parts of 1,6-hexamethylene diisocyanate and 0.11 part of dibutyltin laurate were charged and reacted at 90 ° C. for 8 hours in a nitrogen gas atmosphere. The obtained polymer was heated to 140 ° C. in a pressure reaction vessel, 1.0 part of di-tert-butyl peroxide was added dropwise over 2 hours, and held at a temperature of 140 ° C. for 2 hours. This was cooled to 60 ° C., 4.26 parts of triethylamine was added and stirred for 30 minutes, and 300 parts of ion-exchanged water was further added and stirred for 30 minutes to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 5)
A four-necked flask equipped with a stirrer, a thermometer, a reflux cooling device, and a nitrogen introduction tube was charged with 140 parts of best plast 792 and 700 parts of toluene as a thermoplastic elastomer, heated and dissolved, and then obtained in Production Example 2. 200 parts of a urethane resin solution was slowly added over 1 hour. This was cooled to 60 ° C., 2.34 parts of triethylamine was added and stirred for 30 minutes, 300 parts of ion-exchanged water was further added and stirred for 30 minutes, and 300 parts of ion-exchanged water and sodium dodecylbenzenesulfonate were added. 0.5 g was mixed and stirred for 15 minutes at a rotational speed of 10,000 rpm to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.

(Example 6)
In a pressurized reaction vessel, 140 parts of Bestplast 792 and 700 parts of toluene were charged and dissolved by heating. 46.3 parts of PTG2000, 1.2 parts of 1,6-hexanediol, and 2,2-dimethylolbutanoic acid were added. 3.1 parts, 9.3 parts of 1,6-hexamethylene diisocyanate and 0.09 part of dibutyltin laurate were charged and reacted at 90 ° C. for 8 hours in a nitrogen gas atmosphere. The obtained polymer was heated to 140 ° C. in a pressure reaction vessel, 1.0 part of di-tert-butyl peroxide was added dropwise over 2 hours, and held at a temperature of 140 ° C. for 2 hours. This was cooled to 60 ° C., 2.34 parts of triethylamine was added and stirred for 30 minutes, and 300 parts of ion-exchanged water and 0.5 g of sodium dodecylbenzenesulfonate were mixed and stirred for 15 minutes at a rotational speed of 10,000 rpm. Thus, an emulsion was obtained. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 7)
Except having changed the thermoplastic elastomer into the manufacture example 1, it synthesize | combined by the method similar to Example 6, and obtained the water dispersion of 40% of solid content.
(Example 8)
Synthesis was performed in the same manner as in Example 6 except that the thermoplastic elastomer was changed to Toughmer S4020 (trade name, manufactured by Mitsui Chemicals Co., Ltd.) to obtain an aqueous dispersion having a solid content of 40%.
Example 9
Synthesis was performed in the same manner as in Example 6 except that the thermoplastic elastomer was changed to Tuftec H1041 (trade name, manufactured by Asahi Kasei Chemicals Corporation) to obtain an aqueous dispersion having a solid content of 40%. (Example 10)
Synthesis was performed in the same manner as in Example 6 except that the thermoplastic elastomer was changed to Dynalon 1320P (trade name, manufactured by JSR Corporation) to obtain an aqueous dispersion having a solid content of 40%.
(Example 11)
A pressurized reaction vessel is charged with 60 parts of Best Plast 792 and 300 parts of toluene, heated and dissolved, 108.1 parts of PTG2000, 2.9 parts of 1,6-hexanediol, and 2,2-dimethylolbutanoic acid. 7.2 parts, 21.8 parts of 1,6-hexamethylene diisocyanate and 0.22 parts of dibutyltin laurate were charged and reacted at 90 ° C. for 8 hours in a nitrogen gas atmosphere. The obtained polymer was heated to 140 ° C. in a pressure reaction vessel, 1.0 part of di-tert-butyl peroxide was added dropwise over 2 hours, and held at a temperature of 140 ° C. for 2 hours. This was cooled to 60 ° C., added with 3.27 parts of triethylamine, stirred for 30 minutes, further mixed with 300 parts of ion-exchanged water and 0.5 g of sodium dodecylbenzenesulfonate, and stirred for 15 minutes at a rotational speed of 10,000 rpm. Thus, an emulsion was obtained. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 12)
A pressurized reaction vessel was charged with 140 parts of Bestplast 792 as a thermoplastic elastomer and 680 parts of toluene, and the interior of the container was heated to 145 ° C. while purging with nitrogen, and then 1.6 parts of 2-hydroxyethyl acrylate and 20 parts of toluene were added. After mixing, 1.1 parts of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of dropping, the mixture was kept at 140 ° C. for 2 hours and then cooled, and 200 parts of the urethane resin solution obtained in Production Example 4 was slowly added over 1 hour. To this, 2 g of sodium dodecylbenzenesulfonate and 500 parts of ion-exchanged water were mixed and stirred at a rotational speed of 10,000 rpm for 15 minutes to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.

(Example 13)
A pressurized reaction vessel was charged with 140 parts of Bestplast 792 as a thermoplastic elastomer and 680 parts of toluene, and the interior of the container was heated to 145 ° C. while purging with nitrogen, and then 1.6 parts of 2-hydroxyethyl acrylate and 20 parts of toluene were added. After mixing, 1.1 parts of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of the dropwise addition, the mixture was kept at 140 ° C. for 2 hours and then cooled, 44.1 parts of PTG2000, 1.2 parts of 1,6-hexanediol, 3.7 parts of 2,2-dimethylolbutanoic acid, 11.1 parts of 6-hexamethylene diisocyanate and 0.11 parts of dibutyltin laurate were charged and reacted at 90 ° C. for 8 hours in a nitrogen gas atmosphere. The obtained polymer was heated to 140 ° C. in a pressure reaction vessel, 1.0 part of di-tert-butyl peroxide was added dropwise over 2 hours, and held at a temperature of 140 ° C. for 2 hours. This was cooled to 60 ° C., 2 g of sodium dodecylbenzenesulfonate and 500 parts of ion-exchanged water were mixed, and stirred for 15 minutes at a rotational speed of 10,000 rpm to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 14)
A pressurized reaction vessel was charged with 140 parts of Bestplast 792 as a thermoplastic elastomer and 680 parts of toluene, and the interior of the container was heated to 145 ° C. while purging with nitrogen, and then 1.6 parts of 2-hydroxyethyl acrylate and 20 parts of toluene were added. After mixing, 1.1 parts of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of dropping, the mixture was kept at 140 ° C. for 2 hours and then cooled, and 200 parts of the urethane resin solution obtained in Production Example 5 was slowly added over 1 hour. This was cooled to 60 ° C., 5.07 parts of triethylamine was added and stirred for 30 minutes, and 300 parts of ion-exchanged water was further added and stirred for 30 minutes to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 15)
A pressurized reaction vessel was charged with 140 parts of Bestplast 792 as a thermoplastic elastomer and 680 parts of toluene, and the interior of the container was heated to 145 ° C. while purging with nitrogen, and then 1.6 parts of 2-hydroxyethyl acrylate and 20 parts of toluene were added. After mixing, 1.1 parts of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of dropping, the mixture was kept at 140 ° C. for 2 hours and then cooled, 39.2 parts of PTG2000, 0.6 part of 1,6-hexanediol, 6.7 parts of 2,2-dimethylolbutanoic acid, 13.5 parts of 6-hexamethylene diisocyanate and 0.13 parts of dibutyltin laurate were charged and reacted at a temperature of 90 ° C. for 8 hours in a nitrogen gas atmosphere. The obtained polymer was heated to 140 ° C. in a pressure reaction vessel, 1.0 part of di-tert-butyl peroxide was added dropwise over 2 hours, and held at a temperature of 140 ° C. for 2 hours. This was cooled to 60 ° C., 5.07 parts of triethylamine was added and stirred for 30 minutes, and 300 parts of ion-exchanged water was further added and stirred for 30 minutes to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 16)
A pressurized reaction vessel was charged with 140 parts of Bestplast 792 as a thermoplastic elastomer and 680 parts of toluene, and the interior of the container was heated to 145 ° C. while purging with nitrogen, and then 1.6 parts of 2-hydroxyethyl acrylate and 20 parts of toluene were added. After mixing, 1.1 parts of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of dropping, the mixture was kept at 140 ° C. for 2 hours and then cooled, and 200 parts of the urethane resin solution obtained in Production Example 4 was slowly added over 1 hour. This was cooled to 60 ° C., 2.77 parts of triethylamine was added and stirred for 30 minutes, 300 parts of ion-exchanged water and 0.5 g of sodium dodecylbenzenesulfonate were mixed, and stirred for 15 minutes at a rotation speed of 10,000 rpm. To obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 17)
A pressurized reaction vessel was charged with 140 parts of Bestplast 792 as a thermoplastic elastomer and 680 parts of toluene, and the interior of the container was heated to 145 ° C. while purging with nitrogen, and then 1.6 parts of 2-hydroxyethyl acrylate and 20 parts of toluene were added. After mixing, 1.1 parts of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of the dropwise addition, the mixture was kept at 140 ° C. for 2 hours and then cooled, 44.1 parts of PTG2000, 1.2 parts of 1,6-hexanediol, 3.7 parts of 2,2-dimethylolbutanoic acid, 11.1 parts of 6-hexamethylene diisocyanate and 0.11 parts of dibutyltin laurate were charged and reacted at 90 ° C. for 8 hours in a nitrogen gas atmosphere. The obtained polymer was heated to 140 ° C. in a pressure reaction vessel, 1.0 part of di-tert-butyl peroxide was added dropwise over 2 hours, and held at a temperature of 140 ° C. for 2 hours. This was cooled to 60 ° C., 2.77 parts of triethylamine was added and stirred for 30 minutes, 300 parts of ion-exchanged water and 0.5 g of sodium dodecylbenzenesulfonate were mixed, and stirred for 15 minutes at 10,000 rpm. To obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 18)
Except having changed the thermoplastic elastomer into what was obtained in manufacture example 1, it synthesize | combined by the method similar to Example 17, and obtained the water dispersion of 40% of solid content.
(Example 19)
Synthesis was performed in the same manner as in Example 17 except that the thermoplastic elastomer was changed to Toughmer S4020 to obtain an aqueous dispersion having a solid content of 40%.
(Example 20)
Synthesis was performed in the same manner as in Example 17 except that the thermoplastic elastomer was changed to Tuftec H1041, and an aqueous dispersion having a solid content of 40% was obtained.
(Example 21)
Synthesis was performed in the same manner as in Example 17 except that the thermoplastic elastomer was changed to Dynalon 1320P to obtain an aqueous dispersion having a solid content of 40%.

(Example 22)
A pressurized reaction vessel was charged with 140 parts of the thermoplastic elastomer obtained in Production Example 1 and 680 parts of toluene, and the interior of the vessel was heated to 145 ° C. while purging with nitrogen, and then 1.4 parts of maleic anhydride and 20 parts of toluene were added. After mixing, 1.0 part of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of dropping, the mixture was kept at 150 ° C. for 2 hours, and then 0.76 part of 1,6-hexanediol was mixed and reacted for 3 hours. This was cooled, 55.0 parts PTG2000, 1.6 parts 1,6-hexanediol, 3.7 parts 2,2-dimethylolbutanoic acid, 11.1 parts 1,6-hexamethylene diisocyanate. Then, 0.11 part of dibutyltin laurate was charged and reacted at a temperature of 90 ° C. for 8 hours under a nitrogen gas atmosphere. The obtained polymer was cooled to 60 ° C., 2.77 parts of triethylamine was added and stirred for 30 minutes, and 300 parts of ion-exchanged water was further added and stirred for 30 minutes to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 23)
A pressurized reaction vessel was charged with 60 parts of Bestplast 792 as a thermoplastic elastomer and 280 parts of toluene, heated to 145 ° C. while purging with nitrogen, and then 0.8 parts of 2-hydroxyethyl acrylate and 20 parts of toluene. After mixing, 0.5 part of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of the dropwise addition, the mixture was kept at 140 ° C. for 2 hours and then cooled, PTG2000 was 106.8 parts, 1,6-hexanediol was 2.83 parts, 2,2-dimethylolbutanoic acid was 7.47 parts, 23.0 of 6-hexamethylene diisocyanate
Part, 0.23 part of dibutyltin laurate was charged and reacted at a temperature of 90 ° C. for 8 hours in a nitrogen gas atmosphere. The obtained polymer was heated to 140 ° C. in a pressure reaction vessel, 1.0 part of di-tert-butyl peroxide was added dropwise over 2 hours, and held at a temperature of 140 ° C. for 2 hours. This was cooled to 60 ° C., 3.38 parts of triethylamine was added and stirred for 30 minutes, 300 parts of ion-exchanged water and 0.5 g of sodium dodecylbenzenesulfonate were mixed, and stirred for 15 minutes at a rotation speed of 10,000 rpm. To obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 24)
A pressurized reaction vessel was charged with 60 parts of Bestplast 792 as a thermoplastic elastomer and 280 parts of toluene, heated to 145 ° C. while purging with nitrogen, and then 0.8 parts of 2-hydroxyethyl acrylate and 20 parts of toluene. After mixing, 0.5 part of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of the dropwise addition, the mixture was kept at 140 ° C. for 2 hours and then cooled, and 40 parts of Bestplast 792 was added and dissolved by heating. To this, 76.0 parts of PTG2000, 2.0 parts of 1,6-hexanediol, , 2-dimethylolbutanoic acid 5.4 parts, 1,6-hexamethylene diisocyanate 16.6 parts, dibutyltin laurate 0.17 parts were charged and reacted at 90 ° C. for 8 hours in a nitrogen gas atmosphere. The obtained polymer was heated to 140 ° C. in a pressure reaction vessel, 1.0 part of di-tert-butyl peroxide was added dropwise over 2 hours, and held at a temperature of 140 ° C. for 2 hours. This was cooled to 60 ° C., 4.08 parts of triethylamine was added and stirred for 30 minutes, 300 parts of ion-exchanged water and 0.5 g of sodium dodecylbenzenesulfonate were mixed, and stirred for 15 minutes at a rotation speed of 10,000 rpm. To obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 25)
Synthesis was performed in the same manner as in Example 24 except that 60 parts of the thermoplastic elastomer initially charged was changed to 60 parts of the resin obtained in Production Example 1 to obtain an aqueous dispersion having a solid content of 40%.
(Example 26)
80 parts of Preparation Example 1 and 380 parts of toluene were charged as a thermoplastic elastomer into a pressurized reaction vessel, and the inside of the vessel was heated to 145 ° C. while purging with nitrogen, and then 1.0 part of 2-hydroxyethyl acrylate and 20 parts of toluene were added. After mixing, 0.7 part of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of the dropwise addition, the mixture was kept at 140 ° C. for 2 hours and then cooled. To this, 91.1 parts of PTG2000, 2.4 parts of 1,6-hexanediol, 6.5 parts of 2,2-dimethylolbutanoic acid, 20.0 parts of 1,6-hexamethylene diisocyanate and 0.20 parts of dibutyltin laurate were charged and reacted at a temperature of 90 ° C. for 8 hours in a nitrogen gas atmosphere. The obtained polymer was heated to 140 ° C. in a pressure reaction vessel, 1.0 part of di-tert-butyl peroxide was added dropwise over 2 hours, and held at a temperature of 140 ° C. for 2 hours. 60 parts of high resin T-480X (Mitsui Chemicals Co., Ltd.), which is a petroleum resin, is added and dissolved by heating. Then, 4.91 parts of triethylamine is added at 60 ° C. and stirred for 30 minutes. 300 parts and 0.5 g of sodium dodecylbenzenesulfonate were mixed and stirred for 15 minutes at 10,000 rpm to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Example 27)
Synthesis was performed in the same manner as in Example 26 except that the petroleum resin was changed to 60 parts of Pencel A (Arakawa Chemical Industries, Ltd.), which is a rosin resin, to obtain an aqueous dispersion having a solid content of 40%.
(Example 28)
Synthesis was performed in the same manner as in Example 26 except that the petroleum resin was changed to 60 parts of Clearon P85 (Yasuhara Chemical Co., Ltd.), which is a terpene resin, to obtain an aqueous dispersion having a solid content of 40%.

(Example 29)
100 parts of the aqueous dispersion obtained in Example 18 were mixed with 24 parts of the aqueous dispersion described in Production Example 6 and ion-exchanged water to obtain an aqueous dispersion having a solid content of 40%.
(Example 30)
To 100 parts of the aqueous dispersion obtained in Example 18, 24 parts of super ester E720 (made by Arakawa Chemical Industries, Ltd.), which is an aqueous resin composition of rosin resin, and ion-exchanged water were mixed to obtain a solid content of 40. % Aqueous dispersion was obtained.
(Example 31)
To 100 parts of the aqueous dispersion obtained in Example 18, 24 parts of Nanolet R1050 (manufactured by Yasuhara Chemical Co., Ltd.), which is an aqueous resin composition of a terpene resin, and ion-exchanged water were mixed to give water with a solid content of 40%. A dispersion was obtained.
(Example 32)
Synthesis was carried out in the same manner as in Example 26 except that 60 parts of petroleum resin was changed to 20 parts of Highlett T-480X and 40 parts of Clearon P85 to obtain an aqueous dispersion having a solid content of 40%. (Example 33)
Synthesis was performed in the same manner as in Example 26 except that 60 parts of petroleum resin was changed to 20 parts of Pencel A and 40 parts of Clearon P85, and an aqueous dispersion having a solid content of 40% was obtained.
(Example 34)
Synthesis was performed in the same manner as in Example 26 except that 60 parts of petroleum resin was changed to 20 parts of Highlett T-480X, 20 parts of Pencel A, and 20 parts of Clearon P85, and water dispersion with a solid content of 40% was performed. Got the body.
(Examples 35-42)
80 parts of the aqueous dispersion obtained in Examples 1, 2, 4, 6, 17, 24, 28, and 31 were mixed with 10 parts of Takenate WD-720 (manufactured by Mitsui Chemicals Polyurethane Co., Ltd.) as a curing agent. A dispersion was obtained.
(Examples 43 to 50)
In 85 parts of the aqueous dispersion obtained in Examples 1, 2, 4, 6, 17, 24, 28 and 31, 10 parts of Cymel 236 (manufactured by Cytec Co., Ltd.) as a curing agent and 0 catalyst of Catalyst 500 are used. 8 parts were mixed to obtain an aqueous dispersion.
(Examples 51 to 58)
20 parts of Epocros K-2020E (manufactured by Nippon Shokubai Co., Ltd.) as a curing agent was mixed with 85 parts of the aqueous dispersion obtained in Examples 1, 2, 4, 6, 17, 24, 28, and 31 and dispersed in water. Got the body.
(Example 59)
Synthesis was performed in the same manner as in Example 6 except that the thermoplastic elastomer was changed to that obtained in Production Example 7 to obtain an aqueous dispersion having a solid content of 40% and a particle size of 0.5 μm.
(Example 60)
Synthesis was performed in the same manner as in Example 6 except that the thermoplastic elastomer was changed to that obtained in Production Example 8, and an aqueous dispersion having a solid content of 40% was obtained.
(Example 61)
Synthesis was performed in the same manner as in Example 6 except that the thermoplastic elastomer was changed to that obtained in Production Example 9 to obtain an aqueous dispersion having a solid content of 40%.
(Example 62)
Synthesis was performed in the same manner as in Example 17 except that the thermoplastic elastomer was changed to that obtained in Production Example 7 to obtain an aqueous dispersion having a solid content of 40%.
(Example 63)
Synthesis was performed in the same manner as in Example 17 except that the thermoplastic elastomer was changed to that obtained in Production Example 8, and an aqueous dispersion having a solid content of 40% was obtained.
(Example 64)
Synthesis was performed in the same manner as in Example 17 except that the thermoplastic elastomer was changed to that obtained in Production Example 9 to obtain an aqueous dispersion having a solid content of 40%.
(Example 65)
Except having changed the thermoplastic elastomer into what was obtained in manufacture example 7, it synthesize | combined by the method similar to Example 22, and obtained the water dispersion of 40% of solid content.
(Examples 66 to 72)
To 80 parts of the aqueous dispersion obtained in Examples 59 to 65, 10 parts of Takenate WD-720 (manufactured by Mitsui Chemicals Polyurethane Co., Ltd.) was mixed as a curing agent to obtain an aqueous dispersion.
(Examples 73 to 79)
To 85 parts of the aqueous dispersion obtained in Examples 59 to 65, 10 parts of Cymel 236 (manufactured by Cytec Co., Ltd.) as a curing agent and 0.8 part of catalyst 500 as a catalyst were mixed to obtain an aqueous dispersion. .

(Examples 80 to 86)
20 parts of Epocros K-2020E (manufactured by Nippon Shokubai Co., Ltd.) as a curing agent were mixed with 85 parts of the aqueous dispersion obtained in Examples 59 to 65 to obtain an aqueous dispersion.
(Comparative Example 1)
In a four-necked flask equipped with a stirrer, a thermometer, a reflux cooling device, and a nitrogen introduction tube, 200 parts of Best Plast 792 and 800 parts of toluene as a thermoplastic elastomer were charged and dissolved by heating. To this, 2 g of sodium dodecylbenzenesulfonate and 500 parts of ion-exchanged water were mixed and stirred at a rotational speed of 10,000 rpm for 15 minutes to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure using an evaporator to obtain an aqueous dispersion having a solid content of 40% and a particle size of 0.6 μm.
(Comparative Example 2)
An aqueous dispersion having a nonvolatile content of 30% was obtained in the same manner as in Comparative Example 1 except that the thermoplastic elastomer was changed to that obtained in Production Example 1.
(Comparative Example 3)
An aqueous dispersion having a nonvolatile content of 30% was obtained in the same manner as in Comparative Example 1 except that the thermoplastic elastomer was changed to Toughmer S4020.
(Comparative Example 4)
An aqueous dispersion having a nonvolatile content of 30% was obtained in the same manner as in Comparative Example 1 except that the thermoplastic elastomer was changed to Tuftec H1041.
(Comparative Example 5)
An aqueous dispersion having a nonvolatile content of 30% was obtained in the same manner as in Comparative Example 1 except that the thermoplastic elastomer was changed to Dynalon 1320P.
(Comparative Example 6)
400 parts of the urethane resin solution obtained by the method of Production Example 2 is heated to 60 ° C., 7.79 parts of triethylamine is added and stirred for 30 minutes, and 300 parts of ion-exchanged water is further added and stirred for 30 minutes to emulsify. A liquid was obtained. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Comparative Example 7)
An aqueous dispersion having a nonvolatile content of 40% was obtained in the same manner as in Comparative Example 6, except that Production Example 2 was changed to the urethane resin solution of Production Example 3 and triethylamine to be added was changed to 14.22 g.
(Comparative Example 8)
An aqueous dispersion having a non-volatile content of 40% was obtained in the same manner as in Comparative Example 6 except that Production Example 2 was changed to 9.25 g of the triethylamine added to the urethane resin solution of Production Example 4.
(Comparative Example 9)
An aqueous dispersion having a nonvolatile content of 40% was obtained in the same manner as in Comparative Example 6 except that Production Example 2 was changed to the urethane resin solution of Production Example 5 and triethylamine to be added was changed to 16.88 g.
(Comparative Example 10)
200 parts of Bestplast 792 and 780 parts of toluene as a thermoplastic elastomer are charged into a pressurized reaction vessel, and the inside of the vessel is heated to 145 ° C. while purging with nitrogen, and then 2.3 parts of 2-hydroxyethyl acrylate and 20 parts of toluene are added. After mixing, 1.6 parts of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of dropping, the mixture was kept at 140 ° C. for 2 hours and then cooled. To this, 2 g of sodium dodecylbenzenesulfonate and 500 parts of ion-exchanged water were mixed and stirred at a rotational speed of 10,000 rpm for 15 minutes to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Comparative Example 11)
An aqueous dispersion having a nonvolatile content of 40% was obtained in the same manner as in Comparative Example 10, except that the thermoplastic elastomer was changed to that obtained in Production Example 1.
(Comparative Example 12)
An aqueous dispersion having a nonvolatile content of 40% was obtained in the same manner as in Comparative Example 10 except that the thermoplastic elastomer was changed to Toughmer S4020.
(Comparative Example 13)
An aqueous dispersion having a nonvolatile content of 40% was obtained in the same manner as in Comparative Example 10, except that the thermoplastic elastomer was changed to Tuftec H1041.
(Comparative Example 14)
An aqueous dispersion having a nonvolatile content of 40% was obtained in the same manner as in Comparative Example 10 except that the thermoplastic elastomer was changed to Dynalon 1320P.

(Comparative Example 15)
In a pressurized reaction vessel, 200 parts of the thermoplastic elastomer obtained in Production Example 1 and 780 parts of toluene were charged, and the inside of the container was heated to 145 ° C. while purging with nitrogen. Then, 2.0 parts of maleic anhydride and 20 parts of toluene were added. After mixing, 1.4 parts of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of dropping, the mixture was kept at 150 ° C. for 2 hours and then cooled. To this, 2 g of sodium dodecylbenzenesulfonate and 500 parts of ion-exchanged water were mixed and stirred at a rotational speed of 10,000 rpm for 15 minutes to obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.
(Comparative Example 16)
In a pressurized reaction vessel, 200 parts of the thermoplastic elastomer obtained in Production Example 1 and 780 parts of toluene were charged, and the inside of the container was heated to 145 ° C. while purging with nitrogen. Then, 2.0 parts of maleic anhydride and 20 parts of toluene were added. After mixing, 1.4 parts of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of dropping, the mixture was kept at 150 ° C. for 2 hours and then cooled. To this, 2.1 parts of triethylamine was added for emulsification.
(Comparative Example 17)
In a pressurized reaction vessel, 200 parts of the thermoplastic elastomer obtained in Production Example 1 and 780 parts of toluene were charged, and the inside of the container was heated to 145 ° C. while purging with nitrogen. Then, 2.0 parts of maleic anhydride and 20 parts of toluene were added. After mixing, 1.4 parts of di-tert-butyl peroxide was added dropwise over 2 hours. After completion of dropping, the mixture was kept at 150 ° C. for 2 hours. This was cooled to 60 ° C., 2.1 parts of triethylamine was added and stirred for 30 minutes, 300 parts of ion-exchanged water and 0.5 g of sodium dodecylbenzenesulfonate were mixed and stirred for 15 minutes at a rotational speed of 10,000 rpm. To obtain an emulsion. Toluene in the emulsion was distilled off under reduced pressure with an evaporator to obtain an aqueous dispersion having a solid content of 40%.

[Evaluation and results]
<Stability of water dispersion>
The aqueous dispersions obtained in Examples and Comparative Examples were allowed to stand for 1 month under the respective conditions of 40% nonvolatile content, room temperature and 40 ° C., and the state of the solution was evaluated. After the elapse of one month, the water dispersion, in which neither separation nor precipitation was confirmed, was evaluated as ○, while separation and / or precipitation was observed and was easily dispersible by stirring. Or the thing which cannot be disperse | distributed easily by stirring by which precipitation was observed was set as x. In addition, about the thing which mixed the hardening | curing agent, the test only of storage at room temperature was done. Moreover, about what could not be emulsified, it was set as xx.
<Sprayability of water dispersion>
Paint gun (Wider spray gun manufactured by Iwata Co., Ltd. (trade name; W-88-13)
H5G)), atomization pressure 4kg / cm ² , nozzle 1 rotation open, temperature in painting booth 3
Spray the aqueous dispersions obtained in Examples and Comparative Examples at 0 ° C. and observe whether or not stringing occurs. did.
<< Physical properties of coating film >>
The coating liquid used for the evaluation was added with 3 parts of a 50% aqueous solution of Orphin E1010 (manufactured by Nissin Chemical Industry Co., Ltd.) as a wetting agent to the resin of the aqueous dispersion obtained in each of the Examples and Comparative Examples And created.
The above-mentioned water is applied so that the film thickness after drying is 10 μm on a polypropylene plate (product name: X708) made of polypropylene whose surface is wiped with isopropyl alcohol. After each dispersion was applied, it was treated in an oven at 80 ° C. for 30 minutes. On this coating film, a white top coat paint (manufactured by Nippon Bee Chemical Co., Ltd., trade name: R278 (main agent) / R271 (curing agent) = mixed at 8/2) so that the film thickness after drying is 80 μm. A coating film was formed by coating, and allowed to stand at room temperature for 10 minutes, and then placed in an oven at 80 ° C. for 30 minutes to prepare a test piece. For these specimens, a cross-cut peel test after 24 hours, a peel strength measurement, a gloss retention after a weather resistance test and a cross-cut peel test, and an appearance and a cross-cut peel test after a hot water resistance test It was. In addition, about the thing peeled by the cross-cut peel test, or the thing whose strength of 800 g / cm or more did not appear in the peel strength after 24 hours, each test of weather resistance and warm water resistance was not implemented. Moreover, only the cross-cut peel test was performed on the coating film on which the top coating was not applied.
Base material made of olefinic thermoplastic elastomer

After the coating liquid is dried as an olefinic thermoplastic elastomer whose surface is wiped with isopropyl alcohol, a square plate of Toughmer A4070 (manufactured by Mitsui Chemicals) and a square plate of Miralastomer 8030 (manufactured by Mitsui Chemicals) are dried. Each of the aqueous dispersions was applied so that the film thickness was 10 μm, and then was placed in an oven at 80 ° C. for 30 minutes. On this coating film, a white top coat paint (manufactured by Nippon Bee Chemical Co., Ltd., trade name: R278 (main agent) / R271 (curing agent) = mixed at 8/2) so that the film thickness after drying is 80 μm. A coating film was formed by coating, and allowed to stand at room temperature for 10 minutes, and then placed in an oven at 80 ° C. for 30 minutes to prepare a test piece. These test pieces were subjected to a cross-cut peel test after 24 hours. Moreover, only the cross-cut peel test was performed on the coating film on which the top coating was not applied.
The coating thickness of the steel sheet coating solution is 10 μm after drying on the surface of the electrodeposition paint of the steel sheet that has been surface-treated (thickness: about 20 μm) with a known electrodeposition epoxy paint whose surface is wiped with isopropyl alcohol. After each coating material was applied, it was placed in an oven at 150 ° C. for 30 minutes. On this coating film, a white top coat paint (manufactured by Nippon Bee Chemical Co., Ltd., trade name: R278 (main agent) / R271 (curing agent) = mixed at 8/2) so that the film thickness after drying is 80 μm. A coating film was formed by coating, and allowed to stand at room temperature for 10 minutes, and then placed in an oven at 80 ° C. for 30 minutes to prepare a test piece. These test pieces were subjected to a cross-cut peel test after 24 hours. Moreover, only the cross-cut peel test was performed on the coating film on which the top coating was not applied.
The polypropylene film coating solution was applied to # 500T-T (manufactured by Tosero Co., Ltd.), which is a polypropylene film, with the above aqueous dispersion applied to a film thickness of 3 μm after drying, and then placed in an oven at 80 ° C. Treated for 10 minutes. On this coating film, the PET film was heat-sealed by applying a pressure of 0.098 MPa at 100 ° C. for 1 second by a method based on JISZ1707. The peel strength was measured with the test piece thus obtained.
<Cross-cut peel test>
In accordance with the cross-cut peel test method described in JIS-K-5400, a test piece with a cross cut is prepared, and an adhesive tape (Nichiban Co., Ltd. product) is pasted on the cross cut, immediately. It was peeled by pulling in the direction of 90 °, and evaluation was performed based on the number of grids that were not peeled out of 100 grids.
<Measurement of peel strength>
After making a cut with a width of 1 cm in the coated substrate and peeling off the end portion, the end portion is pulled in the direction of 180 ° at a speed of 50 mm / min, and the peel strength is measured, and the peel strength is 1200 g / cm or more. The product was evaluated as ◎, from 1000 g / cm to less than 1200 g / cm as ○, from 800 g / cm to less than 1000 g / cm as Δ, and from 800 g / cm as ×.

The peel strength of the film is determined by cutting the test piece into a 1.5 cm strip, measuring the peel strength by pulling the end in the 180 ° direction at a speed of 50 mm / min, and the peel strength is 500 g / cm or more. Were evaluated as ◎, those with 300 g / cm or more and less than 500 g / cm as ◯, and those with less than 300 g / cm as x.
<Weather resistance test>
In accordance with the accelerated weather resistance test method described in JIS-K-5400, a grid-peeling test and gloss retention were evaluated for those evaluated for 1000 hours with a sunshine carbon arc lamp type.
<Measurement of gloss retention>
From the 60-degree specular gloss before and after the test (JIS-K-5400), the measured value retention rate (%) = (glossiness after test / initial glossiness) × 100 was calculated, and the gloss retention rate was 80%. In the above, the case where no discoloration was observed was evaluated as ◯, the case where the discoloration was 60% or more and less than 80% was evaluated as Δ, and the case where it was less than 60% was evaluated as ×.
<Warm water resistance test>
The test piece obtained above was immersed in warm water adjusted to 40 ° C. for 240 hours, and the appearance of the coating film and the cross-cut peel test were evaluated.
<Appearance of coating film>
About the coating film after a test, the presence or absence of a swelling is evaluated, and what has a change in coating films, such as (circle) and a swelling, is set to x.

The obtained aqueous dispersion was evaluated according to the description in the section of the physical property measurement method.
The evaluation results are shown in Tables 3 to 6 below.

Claims (17)

The thermoplastic elastomer (A) and the resin (C) having a urethane bond are contained in the same particle,
The thermoplastic elastomer (A) is a propylene / 1-butene copolymer,
The propylene / 1-butene copolymer is
(1) A unit derived from propylene is contained in an amount of 60 to 90 mol% and a unit derived from 1-butene is contained in an amount of 10 to 40 mol% (provided that all structural units are 100 mol%),
(2) The intrinsic viscosity measured in decalin at 135 ° C. is 0.1-12 dl / g,
(3) An aqueous dispersion characterized by having a molecular weight distribution (Mw / Mn) determined by gel permeation chromatography (GPC) in the range of 1 to 3. The propylene / 1-butene copolymer is further (4) Triad isotacticity (mm fraction) determined from ¹³ C-NMR spectrum measurement is 85% or more and 97.5% or less,
(5) The melting point (Tm) measured by a differential scanning calorimeter is 40 to 120 ° C.
(6) The relationship between the melting point (Tm) and the 1-butene constituent unit content M (mol%) is 146exp (−0.022M) ≧ Tm ≧ 125exp (−0.032M). Item 4. The aqueous dispersion according to Item 1. The aqueous dispersion according to claim 1, characterized by comprising reacting a resin (C) having a urethane bond and the thermoplastic elastomer (A). Obtained by reacting the thermoplastic elastomer (A) with a copolymerizable monomer comprising a monomer having an α, β-monoethylenically unsaturated group containing a functional group and another copolymerizable monomer. The aqueous dispersion according to claim 1, wherein the thermoplastic elastomer (B) modified with a functional group is reacted with the resin (C) having a urethane bond. Aqueous dispersion according to claim 4, characterized in that the functional group of the resin (C) having an urethane bond with a functional group of the modified thermoplastic elastomer (B) in the functional group is reacted. The particle size of the particles is
It is the range of 10 nm-10 micrometers, The water dispersion of any one of Claims 1-5 characterized by the above-mentioned. The thermoplastic elastomer (A) and / or the thermoplastic elastomer (A) comprises a monomer having an α, β-monoethylenically unsaturated group containing a functional group and other copolymerizable monomers. reacting a copolymerizable monomer obtained, the heat modified with functional groups thermoplastic elastomer (B), the resin (C) having a urethane bond, but
The aqueous dispersion according to any one of claims 1 to 6, comprising a weight ratio of [(A) and / or (B)] / (C) = 10/90 to 95/5.   A surfactant is contained, The water dispersion of any one of Claims 1-7 characterized by the above-mentioned.   The coating material containing the water dispersion of any one of Claims 1-8.   The coating material containing the water dispersion of any one of Claims 1-8.   The primer containing the water dispersion of any one of Claims 1-8.   The adhesive agent containing the water dispersion of any one of Claims 1-8. A coating film formed by applying the coating material according to claim 9, the paint according to claim 10, the primer according to claim 11, or the adhesive according to claim 12.   A coating material containing a main agent containing the aqueous dispersion according to any one of claims 1 to 8 having active hydrogen and / or hydroxyl groups, and a curing agent capable of reacting with active hydrogen and / or hydroxyl groups.   The coating film formed by hardening | curing the coating material of Claim 14.   The coating film according to claim 13 or 15, wherein the substrate is an olefin resin.   The coating film according to claim 13 or 15, wherein the substrate is a metal.