Aqueous liquid dispersion, method for producing same, composition, adhesive, and coating material

Technical Field

The present invention relates to an aqueous liquid dispersion, a method for producing the same, as well as a composition, an adhesive and a coating material. More particularly, the present invention relates to (1) an aqueous liquid dispersion composed of polymer particles comprising a specific crosslinkable unsaturated monomer unit, a specific vinyl alcohol polymer comprising an ethylene unit, a vinyl alcohol polymer having a carboxyl group and a crosslinking agent, or (2) an aqueous liquid dispersion composed of polymer particles comprising a specific crosslinkable unsaturated monomer unit, a vinyl alcohol copolymer having an ethylene unit and a carboxyl group-containing monomer unit and a crosslinking agent, and a method for producing the same, as well as a composition, an adhesive and a coating material. The aqueous liquid dispersion and the composition of the present invention are excellent in water resistance, especially boiling water resistance and shelf viscosity stability (have a long pot life), and thus are suitable for an adhesive and a coating material.

Background Art

Polyvinyl alcohol (hereinafter, sometimes abbreviated as PVA) is widely used as a protective colloid for emulsion polymerization of ethylenically unsaturated monomers, particularly vinyl ester monomers typified by vinyl acetate. Vinyl ester aqueous emulsions obtained by emulsion polymerization using this as the protective colloid are widely used in various fields of various adhesives for paper, woodworking and plastics, various binders for impregnated paper and nonwoven products, admixtures, placing joint materials, paints, paper coating and textile processing. Such an aqueous emulsion exerts its effect on the above various usages under a dry condition by forming a film having a firm mechanical strength, but is problematic under a high humidity or water-wet condition in that PVA is easily eluted or absorbs water to remarkably diminish the mechanical strength because PVA forming a continuous phase in the film is water soluble.

From these circumstances, various procedures have been attempted in order to enhance water resistance and hot water resistance of the film obtained from the emulsion using PVA as a dispersant. As their representative, a method for combining a polyvalent isocyanate compound with the emulsion using PVA as the dispersant is known. In this method, the remarkable water resistance is realized because isocyanate is firmly reacted with a hydroxyl group in PVA, but at the same time, since isocyanate is reacted with water, the pot life of the composition is very short and its workability is problematic.

Various adhesives using the aqueous emulsion using a PVA polymer as the dispersant have been proposed. For example, the adhesives composed of the aqueous emulsion using PVA as the dispersant and aliphatic aldehyde such as glyoxal (Patent Document 1), the adhesives composed of PVA, the aqueous emulsion, a crosslinking agent, an amino compound such as chitosan (Patent Document 2), the adhesives composed of PVA, the aqueous emulsion, the crosslinking agent such as aluminum chloride and a polyvalent isocyanate compound (Patent Document 3), the adhesives mainly composed of the emulsion using PVA having an α-olefin unit having 4 or less carbon atoms as the dispersant (Patent Document 4), the composition composed of the emulsion obtained by emulsion polymerization in the presence of carboxyl group-modified PVA and a react ion product of polyamide and an epoxy group-containing compound (Patent Document 5), and the composition composed of the aqueous emulsion using a PVA polymer having an α-olefin unit and a PVA polymer having a carboxyl group in a molecule as the dispersants and a water resistant additive selected from epoxy compounds, amino group-containing aqueous resins, aluminum compounds and titanium compounds (Patent Document 6) are known. <ul id="ul0001" list-style="none" compact="compact"><li>Patent Document 1: <patcit id="pcit0001" dnum="JPS5594937A"><text>Japanese Published Unexamined Patent Application No. S55-94937</text></patcit></li><li>Patent Document 2: <patcit id="pcit0002" dnum="JPH345678A"><text>Japanese Published Unexamined Patent Application No. H3-45678</text></patcit></li><li>Patent Document 3: <patcit id="pcit0003" dnum="JPS5716150B"><text>Japanese Published Examined Patent Application No. S57-16150</text></patcit></li><li>Patent Document 4: <patcit id="pcit0004" dnum="JP3466316B"><text>Japanese Patent No. 3466316</text></patcit></li><li>Patent Document 5: <patcit id="pcit0005" dnum="JP3311086B"><text>Japanese Patent No. 3311086</text></patcit></li><li>Patent Document 6: <patcit id="pcit0006" dnum="JP2001040231A"><text>Japanese Published Unexamined Patent Application No. 2001-40231</text></patcit></li></ul>

However, although the water resistance is improved in the aforementioned adhesives, the boiling water resistance is not necessarily sufficient. In the adhesive described in Patent Document 3, the shelf viscosity stability is poor (the pot life is short) and its workability is problematic. Therefore, it is not an exaggeration to say that at the present technical level, there is no aqueous liquid dispersion, composition, adhesive and coating material which balance the high water resistance, especially boiling water resistance and the shelf viscosity stability. There is still room to further improve them.

Disclosure of the Invention

Problems to be Solved by the Invention

Under such circumstances, the present invention aims at providing an aqueous liquid dispersion which is excellent in both water resistance, especially boiling water resistance and shelf viscosity stability and a method for producing the same as well as a composition, an adhesive and a coating material.

Means for Solving the Problems

As a result of an extensive study, the present inventors have found that the above object can be accomplished by the following aqueous liquid dispersion (1) or (2), and have completed the present invention. <ol id="ol0001" compact="compact" ol-style=""><li>(1) An aqueous liquid dispersion comprising (A) polymer particles mainly composed of at least one monomer unit selected from ethylenically unsaturated monomers and diene unsaturated monomers while containing 0.1 to 10% by weight of at least one crosslinkable unsaturated monomer unit selected from carboxyl group-containing unsaturated monomers, N-methylol (meth)acrylamide, N-butoxymethyl (meth)acrylamide, diacetone acrylamide and acetoacetoxyethyl (meth)acrylate, (B) a vinyl alcohol polymer containing 1 to 10% by mole of an ethylene unit, (C) a vinyl alcohol polymer having a carboxyl group and (D) a crosslinking agent, and comprising these at a specific solid content weight ratio; and</li><li>(2) an aqueous liquid dispersion comprising (A) polymer particles mainly composed of at least one monomer unit selected from ethylenically unsaturated monomers and diene unsaturated monomers while containing 0.1 to 10% by weight of at least one crosslinkable unsaturated monomer unit selected from carboxyl group-containing unsaturated monomers, N-methylol (meth)acrylamide, N-butoxymethyl (meth)acrylamide, diacetone acrylamide and acetoacetoxyethyl (meth)acrylate, (E) a vinyl alcohol copolymer having 1 to 10% by mole of an ethylene unit and 0.1 to 10% by mole of a carboxyl group-containing monomer unit and (D) a crosslinking agent, and comprising these at specific solid content weight ratios.</li></ol>

That is, a first invention of the present invention is the aqueous liquid dispersion comprising (A) polymer particles mainly composed of at least one monomer unit selected from ethylenically unsaturated monomers and diene unsaturated monomers while containing 0.1 to 10% by weight of at least one crosslinkable unsaturated monomer unit selected from carboxyl group-containing unsaturated monomers, N-methylol (meth)acrylamide, N-butoxymethyl (meth)acrylamide, diacetone acrylamide and acetoacetoxyethyl (meth)acrylate, (B) a vinyl alcohol polymer containing 1 to 10% by mole of an ethylene unit, (C) a vinyl alcohol polymer having a carboxyl group and (D) a crosslinking agent, and comprising them at solid content weight ratios of (B)/(C)=90/10 to 10/90, (A)/{(B)+(C)}=99/1 to 80/20 and {(A)+(B)+(C)}/(D)=99.9/0.1 to 90/10.

Also, a second invention of the present invention is the aqueous liquid dispersion comprising (A) polymer particles mainly composed of at least one monomer unit selected from ethylenically unsaturated monomers and diene unsaturated monomers while containing 0.1 to 10% by weight of at least one crosslinkable unsaturated monomer unit selected from carboxyl group-containing unsaturated monomers, N-methylol (meth)acrylamide, N-butoxymethyl (meth)acrylamide, diacetone acrylamide and acetoacetoxyethyl (meth)acrylate, (E) a vinyl alcohol copolymer having 1 to 10% by mole of an ethylene unit and 0.1 to 10% by mole of a carboxyl group-containing monomer unit and (D) a crosslinking agent, and comprising them at solid content weight ratios of (A)/(E)=99/1 to 80/20 and {(A)+(E)}/(D)=99.9/0.1 to 90/10.

Furthermore, a third invention of the present invention is a method for producing the aqueous liquid dispersion, characterized by combining (D) the crosslinking agent with the aqueous emulsion obtained by emulsion polymerization using (B) the vinyl alcohol polymer containing 1 to 10% by mole of the ethylene unit and (C) the vinyl alcohol polymer having the carboxyl group as dispersion stabilizers and using (A) polymer mainly composed of at least one monomer unit selected from ethylenically unsaturated monomers and diene unsaturated monomers while containing 1 to 10% by mole of at least one crosslinkable unsaturated monomer unit selected from carboxyl group-containing unsaturated monomers, N-methylol (meth)acrylamide, N-butoxymethyl(meth)acrylamide, diacetone acrylamide and acetoacetoxyethyl (meth)acrylate as a dispersoid.

Also, a fourth invention of the present invention is a method for producing the aqueous liquid dispersion, characterized by combining (D) the crosslinking agent with the aqueous emulsion obtained by emulsion polymerization using (E) the vinyl alcohol copolymer having 1 to 10% bymole of the ethylene unit and 0.1 to 10% by mole of the carboxyl group-containing monomer unit as the dispersant and using (A) the polymer mainly composed of at least one monomer unit selected from ethylenically unsaturated monomers and diene unsaturated monomers while containing 1 to 10% by mole of at least one crosslinkable unsaturated monomer unit selected from carboxyl group-containing unsaturated monomers, N-methylol (meth)acrylamide, N-butoxymethyl (meth)acrylamide, diacetone acrylamide and acetoacetoxyethyl (meth)acrylate as a dispersoid.

And a fifth invention of the present invention is a composition obtained by combining a filler with these aqueous liquid dispersions, a sixth invention of the present invention is an adhesive composed of these aqueous liquid dispersions or the composition, and a seventh invention of the present invention is a coating material composed of these aqueous liquid dispersions or the composition.

Effects of the Invention

The aqueous liquid dispersion and the composition combining the filler with the aqueous liquid dispersion of the present invention have both the high water resistance, especially the excellent boiling water resistance and the excellent shelf viscosity stability, and thus, are suitably used as an adhesive and a coating material with high performance.

Best Modes for Carrying Out the Invention

The polymer particles (A) in the aqueous liquid dispersions (1) and (2) of the present invention are mainly composed of at least one monomer unit selected from ethylenically unsaturated monomers and diene unsaturated monomers, and contain at least one crosslinkable unsaturated monomer unit selected from carboxyl group-containing unsaturated monomers, N-methylol (meth)acrylamide, N-butoxymethyl (meth)acrylamide, diacetone acrylamide and acetoacetoxyethyl (meth)acrylate.

Various monomers can be used as the ethylenically unsaturated monomer unit and the diene unsaturated monomer unit which mainly compose the polymer particles. Olefin such as ethylene, propylene and isobutylene, halogenated olefin such as vinyl chloride, vinyl fluoride, vinylidene chloride and vinylidene fluoride, vinyl ester such as vinyl formate, vinyl acetate, vinyl propionate and vinyl versatate, acrylate ester such as methyl acrylate, ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, dodecyl acrylate and 2-hydroxyethyl acrylate, methacrylate ester such as methyl methacrylate, ethyl methacrylate, butyl methacrylate, 2-ethylhexyl methacrylate, dodecyl methacrylate and 2-hydroxyethyl methacrylate, dimethylaminoethyl acrylate, dimethylaminoethyl methacrylate and quaternized products thereof, further, acrylamide based monomers such as acrylamide, methacrylamide, N,N-dimethyl acrylamide, acrylamide-2-methylpropane sulfonic acid and sodium salts thereof and methylenebisacrylamide, styrene based monomers such as styrene, α-methylstyrene, p-styrene sulfonic acid and sodium and potassium salts, additionally N-vinyl pyrrolidone, and diene monomers such as butadiene, isoprene and chloroprene are included.

Crosslinkable unsaturated monomers having an alkoxysilane group such as vinyltrimethoxysilane and methacryloxypropyltrimethoxysilane, crosslinkable unsaturated monomers having an epoxy group such as glycidyl methacrylate and allyl glycidyl ether, and crosslinkable unsaturated monomers having an oxazoline group such as vinyloxazoline and 2-propenyl-2-oxazoline can be used in the range in which performances of the present invention are not impaired.

Among the above unsaturated monomers, the vinyl ester monomer, the combinations of ethylene and the vinyl ester monomer, and the combination of vinyl ester and the (meth)acrylate ester monomer are suitable, and vinyl acetate is particularly preferable as the vinyl ester monomer unit in terms of industrial application and initial adhesive performance when the aqueous liquid dispersion is used as the adhesive. When as the vinyl ester monomer, vinyl ester of a branched higher fatty acid is used at 30% by weight or less relative to total monomers, hydrolysis in storage of the aqueous liquid dispersion is inhibited and the more preferable performance is exerted in the combination with vinyl acetate. Such vinyl ester of the branched higher fatty acid can include vinyl versatate.

As the unsaturated monomer having the carboxyl group, which composes the polymer particles (A) of the present invention, acrylic acid, methacrylic acid, crotonic acid, itaconic acid, fumaric acid, maleic acid (anhydride), phthalic acid (anhydride) and cinnamic acid are used. These can also be used in forms of neutralized products such as sodium salts and half ester.

In the present invention, the polymer particle (A) is necessary to contain at least one crosslinkable unsaturated monomer unit selected from the carboxyl group-containing unsaturated monomers, N-methylol acrylamide, N-methylol methacrylamide, N-butoxymethyl acrylamide, N-butoxymethyl methacrylamide, diacetone acrylamide, acetoacetoxyethyl acrylate and acetoacetoxyethyl methacrylate at 0.1 to 10% by weight, preferably 0.2 to 8 % by weight and more preferably 0.3 to 6% by weight relative to the total monomer units.

When a content of the crosslinkable unsaturated monomer unit is less than 0.1% by weight, a crosslink density is low when a film is formed from the resulting aqueous liquid dispersion, and thus, the water resistance, particularly the boiling water resistance is insufficient. When this content exceeds 10% by weight, the shelf viscosity stability of the resulting aqueous liquid dispersion is diminished. Among these crosslinkable unsaturated monomers, the unsaturated monomer having the carboxyl group is suitable, and among the unsaturated monomers having the carboxyl group, acrylic acid and methacrylic acid are suitable. A particle diameter of the polymer particle (A) is suitably about 0.05 to 10 µm, more suitably 0.1 to 7 µm and still more suitably 0.1 to 5 µm as a measurement by a dynamic light scattering method.

The vinyl alcohol polymer (B) containing 1 to 10% by mole of the ethylene unit in the aqueous liquid dispersion (1) of the present invention can be obtained by saponifying a copolymer of vinyl ester and ethylene. Vinyl ester includes vinyl formate, vinyl acetate, vinyl propionate and vinyl pivalate, and vinyl acetate is economically preferable.

In the present invention, the content of the ethylene unit in the vinyl alcohol polymer (B) containing the ethylene unit is necessary to be 1 to 10% by mole, and is preferably 2 to 8% by mole. When the content of the ethylene unit is less than 1% by mole, the water resistance is insufficient when the film is formed from the resulting aqueous liquid dispersion. When it exceeds 10% by mole, the stable aqueous liquid dispersion is not obtained in some cases because the water solubility of the vinyl alcohol polymer is diminished.

In the present invention, the vinyl alcohol polymer (B) containing the ethylene unit may be a product obtained by copolymerizing a polymerizable ethylenically unsaturated monomer in the range in which the effect of the present invention is not impaired. Such an ethylenically unsaturated monomer includes, for example, acrylic acid, methacrylic acid, phthalic acid (anhydride), maleic acid (anhydride), itaconic acid, crotonic acid, fumaric acid, acrylonitrile, methacrylonitrile, acrylamide, methacrylamide, trimethyl-(3-acrylamide-3-dimethylpropyl)-ammonium chloride, acrylamide-2-methylpropane sulfonic acid and sodium salts thereof, ethyl vinyl ether, butyl vinyl ether, N-vinyl pyrrolidone, vinyl chloride, vinyl bromide, vinyl fluoride, vinylidene chloride, vinylidene fluoride, tetrafluoroethylene, sodium vinyl sulfonate, and sodium allyl sulfonate. It is also possible to use end-modified products obtained by copolymerizing ethylene with the vinyl ester monomer such as vinyl acetate in the presence of a thiol compound such as thiol acetic acid and mercaptopropionic acid and saponifying it.

A saponification degree of the vinyl alcohol polymer (B) having the ethylene unit is suitably 85 to 99.5% by mole, more preferably 88 to 99.5% by mole and still more preferably 90 to 99.5% by mole. When the saponification degree is in this range, the water resistance, particularly the boiling water resistance and the shelf viscosity stability of the aqueous liquid dispersion of the present invention are well kept.

A polymerization degree of the polymer is preferably in the range of 100 to 4000 and more preferably 200 to 3000. When the polymerization degree is in this range, the dispersion stability of the aqueous liquid dispersion of the present invention and the water resistance of its film are well kept.

The vinyl alcohol polymer (C) having the carboxyl group in the aqueous liquid dispersion (1) of the present invention is obtained by various methods, and representatively, can be obtained by saponifying a copolymer of vinyl ester and the unsaturated monomer having the carboxyl group as described in <patcit id="pcit0007" dnum="JPS6031844B"><text>Japanese Published Examined Patent Application No. S60-31844</text></patcit>. Vinyl ester includes vinyl formate, vinyl acetate, vinyl propionate and vinyl pivalate, and vinyl acetate is economically preferable.

In this case, the content of the carboxyl group in the polymer is not particularly limited, and typically 0.1 to 10% by mole, preferably 0.2 to 8% by mole, and more preferably 0.25 to 7% by mole. Here, as the unsaturated monomer having the carboxyl group, acrylic acid, methacrylic acid, phthalic acid (anhydride), maleic acid (anhydride), itaconic acid, crotonic acid and fumaric acid are exemplified, and among them, dicarboxylic acid and half ester or anhydride thereof are suitable.

In the present invention, the vinyl alcohol polymer (C) having the carboxyl group can contain a polymerizable ethylenically unsaturated monomer unit in the range in which the effect of the present invention is not impaired. Such an ethylenically unsaturated monomer includes, for example, α-olefin such as ethylene and propylene, acrylonitrile, methacrylonitrile, acrylamide, methacrylamide, trimethyl(3-acrylamide-3-dimethylpropyl)-ammonium chloride, acrylamide-2-methylpropane sulfonic acid and sodium salts thereof, ethyl vinyl ether, butyl vinyl ether, N-vinyl pyrrolidone, vinyl chloride, vinyl bromide, vinyl fluoride, vinylidene chloride, vinylidene fluoride, tetrafluoroethylene, sodium vinyl sulfonate and sodium allyl sulfonate. It is also possible to use end-modified products obtained by copolymerizing an ethylenic monomer having the carboxyl group with the vinyl ester monomer such as vinyl acetate in the presence of the thiol compound such as thiol acetic acid and mercaptopropionic acid and saponifying it.

The saponification degree of the vinyl alcohol polymer (C) having the carboxyl group in the present invention is preferably 70% by mole or more, more preferably 80% by mole or more and still more preferably 85% by mole or more in terms of its water solubility and stability of the resulting aqueous liquid dispersion.

The polymerization degree of the polymer is preferably in the range of 100 to 4000 and more preferably 200 to 3000. When the polymerization degree is in this range, the dispersion stability of the aqueous liquid dispersion of the present invention and the water resistance of its film are well kept.

In the present invention, the vinyl alcohol polymer (C) having the carboxyl group includes, in addition to the above, block polymers of a polymer having the carboxyl group with a vinyl alcohol polymer obtained by radical polymerization of an unsaturated monomer having the carboxyl group such as acrylic acid using a conventionally and publicly known initiator in an aqueous solution of a vinyl alcohol polymer having a thiol group at an end, and further those obtained by adding an aldehyde compound having the carboxyl group to a vinyl alcohol polymer by conventionally and publicly known methods.

In the present invention, the crosslinking agent (D) can be selected from those performing a crosslinking reaction with a carboxyl group and a hydroxyl group, and includes methylol group-containing compounds (resins), epoxy compounds (resins), aziridine group-containing compounds (resins), oxazoline group-containing compounds (resins), carbodiimide compounds, aldehyde compounds (resins), and various water soluble or colloidal metal salts in terms of crosslinking reactivity with the above functional groups in the aqueous liquid dispersion from a view point of the crosslink and pot life or the like. Preferably, water soluble epoxy compounds, polyamide amine epichlorohydrin adducts, urea-glyoxal resins, aluminum salts, zirconium salts and titanium salts are included.

In terms of crosslinkability and pot life, particularly preferably, the polyamide amine epichlorohydrin adducts, water soluble aluminum salts such as aluminum chloride and aluminum nitrate and the glyoxal based resins such as urea-glyoxal resins are included. One or two or more are suitably used as the crosslinking agent (D). In particular, when two or more selected from the water soluble aluminum salts, the polyamide amine epichlorohydrin adducts and the glyoxal based resins are combined, it is preferable because high effects of the water resistance and initial adhesiveness are realized by forming the high crosslink.

Quantitative relationships of (A), (B), (C) and (D) included in the aqueous liquid dispersion of the present invention are (B)/(C)=90/10 to 10/90, (A)/{(B)+(C)}=99/1 to 80/20 and {(A)+(B)+(C)}/(D)=99.9/0.1 to 90/10 as solid content weight ratios. The ratio of (B)/(C) is necessary to be 90/10 to 10/90, is preferably 85/15 to 20/80 and more preferably 80/20 to 30/70. In this case, when the content of (B) is too high, the sufficient crosslink does not occur and the water resistance is diminished when the film is formed from the aqueous liquid dispersion. When the content of (B) is too low, the shelf viscosity stability is deteriorated simultaneously with the decrease in the water resistance, particularly the boiling water resistance.

The ratio of (A)/{(B)+(C)} is necessary to be 99/1 to 80/20, is preferably 98.5/1.5 to 87/13 and more preferably 98/2 to 85/15. In this case, when the content of (A) is too high, the shelf viscosity stability and the mechanical stability of the aqueous liquid dispersion are diminished. When the content of (A) is too low, the water resistance, particularly the boiling water resistance is diminished when the film is formed from the aqueous liquid dispersion, and simultaneously, the shelf viscosity stability is sometimes deteriorated.

Furthermore, the content ratio of the crosslinking agent (D) is necessary to be {(A)+(B)+(C)}/(D)=99.9/0.1 to 90/10, is preferably 99.8/0.2 to 91/9 and more preferably 99.7/0.3 to 92/8. When the content of (D) is too low, due to the decrease in the crosslink density, the water resistance, particularly the boiling water resistance is not sufficiently exhibited when the film is formed from the aqueous liquid dispersion. When the content of (D) is too high, the shelf viscosity stability of the aqueous liquid dispersion is deteriorated.

In the aqueous liquid dispersion (2) of the present invention, the vinyl alcohol copolymer (E) having the ethylene unit at 1 to 10% bymole and the carboxyl group-containingmonomer unit at 0.1 to 10% by mole can be obtained by saponifying the copolymer of vinyl ester with ethylene and the monomer having the carboxyl group. Vinyl ester includes vinyl formate, vinyl acetate, vinyl propionate and vinyl pivalate, and vinyl acetate is preferable from economical viewpoint.

In the present invention, the content of the ethylene unit in the vinyl alcohol copolymer (E) having the ethylene unit and the carboxyl group-containing monomer unit is necessary to be 1 to 10% by mole, and is preferably 2 to 8% by mole. When the content of the ethylene unit is less than 1% by mole, the water resistance is not sufficient when the film is formed from the resulting aqueous liquid dispersion. When it exceeds 10% by mole, the stable aqueous liquid dispersion is not sometimes obtained because the water solubility of the vinyl alcohol copolymer is diminished.

The content of the carboxyl group-containing monomer unit in the vinyl alcohol copolymer is necessary to be 0.1 to 10 % by mole, is preferably 0.2 to 8% by mole and more preferably 0.25 to 7% by mole. When the content of the carboxyl group-containing monomer unit is less than 0.1% by mole, crosslinking points are diminished and the performances such as boiling water resistance are not sufficiently exhibited. When it exceeds 10% by mole, the viscosity stability is lowered upon addition of the crosslinking agent. Here, as the unsaturated monomer having the carboxyl group, acrylic acid, methacrylic acid, phthalic acid (anhydride), maleic acid (anhydride), itaconic acid, crotonic acid and fumaric acid are exemplified, and among them, dicarboxylic acid and half ester or anhydride thereof are suitable.

In the present invention, the vinyl alcohol copolymer (E) having the ethylene unit and the carboxyl group-containing monomer unit may be those obtained by copolymerizing a copolymerizable ethylenically unsaturated monomer in the range in which the effects of the present invention are not impaired. Such an ethylenically unsaturated monomer includes, for example, acrylonitrile, methacrylonitrile, acrylamide, methacrylamide, trimethyl-(3-acrylamide-3-dimethylpropyl)-ammonium chloride, acrylamide-2-methylpropane sulfonic acid and sodium salts thereof, ethyl vinyl ether, butyl vinyl ether, N-vinyl pyrrolidone, vinyl chloride, vinyl bromide, vinyl fluoride, vinylidene chloride, vinylidene fluoride, tetrafluoroethylene, sodium vinyl sulfonate and sodium allyl sulfonate. It is also possible to use end-modified products obtained by copolymerizing ethylene and the monomer having the carboxyl group with the vinyl ester monomer such as vinyl acetate in the presence of a thiol compound such as thiol acetic acid and mercaptopropionic acid and saponifying it.

The saponification degree of the vinyl alcohol copolymer (E) having the ethylene unit and the carboxyl group-containing monomer unit in the present invention is suitably 80 to 99.5% by mole, more preferably 85 to 99.5% by mole and still more preferably 86 to 99.5% by mole. When the saponification degree is within this range, the water resistance, particularly the boiling water resistance and the shelf viscosity stability of the aqueous liquid dispersion of the present invention are well kept.

The polymerization degree of the polymer is preferably in the range of 100 to 4000 and more preferably 200 to 3000. When the polymerization degree is within this range, the dispersion stability of the aqueous liquid dispersion and the water resistance of its film are well kept.

The crosslinking agent (D) in the aqueous liquid dispersion (2) in the present invention is the same as the crosslinking agent (D) described in the aqueous liquid dispersion (1). For the quantitative relationships in the crosslinkable aqueous liquid dispersion composition containing (A), (E) and (D), the solid content weight ratio (A)/(E) is 99/1 to 80/20, preferably 98.5/1.5 to 87/13 and more preferably 98/2 to 85/15. In this case, when the content of (A) is too high, the shelf viscosity stability and the mechanical stability of the crosslinkable aqueous liquid dispersion composition are diminished. When the content of (A) is too low, the water resistance, particularly the boiling water resistance is diminished when the film is formed from the crosslinkable aqueous liquid dispersion composition, and simultaneously, the shelf viscosity stability is deteriorated.

Furthermore, for the content ratio of the crosslinking agent (D), {(A)+(E)}/(D) is 99.9/0.1 to 90/10, preferably 99.8/0.2 to 91/9 and more preferably 99.7/0.3 to 92/8. When the content of (D) is too low, the water resistance, particularly the boiling water resistance is not sufficiently exhibited due to the decrease in the crosslink density when the film is formed from the crosslinkable aqueous liquid dispersion composition. When the content of (D) is too high, the shelf viscosity stability of the crosslinkable aqueous liquid dispersion composition is deteriorated.

The aqueous liquid dispersion of the present invention is obtained by various methods. The aqueous liquid dispersion (1) can be obtained representatively by combining the crosslinking agent (D), with an aqueous emulsion using the vinyl alcohol polymer (B) having the ethylene unit at 1 to 10% by mole and the vinyl alcohol polymer (C) having the carboxyl group as the dispersant, and using the polymer (A) mainly composed of at least one monomer unit selected from ethylenically unsaturated monomers and diene unsaturated monomers while containing at least one crosslinkable unsaturated monomer unit at 1 to 10% by weight selected from carboxyl group-containing unsaturated monomers, N-methylol (meth)acrylamide, N-butoxymethyl (meth)acrylamide, diacetone acrylamide and acetoacetoxyethyl (meth)acrylate as the dispersoid. This aqueous emulsion is obtained by emulsion polymerization of the above monomers using the above dispersant.

The aqueous liquid dispersion (2) of the present invention is likewise obtained by various methods, and can be preferably produced by combining the crosslinking agent (D) with the aqueous emulsion obtained by emulsion polymerization using the vinyl alcohol copolymer (E) having the ethylene unit at 1 to 10% by mole and the carboxyl group-containing monomer unit at 0.1 to 10% by mole as the dispersant, and using the polymer (A) mainly composed of at least one monomer unit selected from ethylenically unsaturated monomers and diene unsaturated monomers while containing at least one crosslinkable unsaturated monomer unit at 1 to 10% by mole selected from carboxyl group-containing unsaturated monomers, N-methylol (meth)acrylamide, N-butoxymethyl (meth)acrylamide, diacetone acrylamide and acetoacetoxyethyl (meth)acrylate as the dispersoid.

The emulsion polymerization using the above (A), (B) and (C), or (A) and (E) is not particularly limited, and can be performed under conventionally and publicly known conditions (temperature, pressure, stirring speed) for the emulsion polymerization by addition methods of the monomers (initial bulk addition, continuous addition, monomer pre-emulsified liquid addition (continuous addition of monomers emulsified in the aqueous solution of the dispersant) using the conventionally and publicly known initiator. Alternatively, the technique in which any of the vinyl alcohol polymer (B) or (C), or the vinyl alcohol copolymer (E) is used as the dispersant, the emulsion polymerization of the monomer which composes the polymer particles (A) is initiated, and remaining (B) or (C), or (E) is added during or after the polymerization can be employed.

Various adhesiveness, water resistance, the boiling water resistance and the like can be enhanced by combining a filler to the aqueous liquid dispersion of the present invention to make a composition. The filler can include organic fillers and inorganic fillers. The organic fillers include wood powders, wheat flour and starch. The inorganic fillers include clay, kaolin, talc, calcium carbonate and titanium oxide. When the inorganic filler is combined, the enhancement effect of the water resistance, particularly the boiling water resistance is remarkably preferable. A combination ratio of the filler to the aqueous liquid dispersion of the present invention is not particularly limited, and can be appropriately set depending on the usage and the purpose. The amount of the filler to be combined is suitably 5 to 200 parts by weight and more suitably 10 to 150 parts by weight relative to 100 parts by weight of {(A)+(E)}.

The aqueous liquid dispersion and the composition of the present invention may contain various organic solvents such as toluene, perchlene, dichlorobenzene and trichlorobenzene, various plasticizers such as dibutyl phthalate, various film forming aids such as glycol ethers, water soluble polymers such as ester starch, modified starch, oxidized starch, soda alginate, carboxymethylcellulose, methylcellulose, hydroxymethylcellulose, maleic acid anhydride/isobutene copolymers, maleic acid anhydride/styrene copolymers, maleic acid anhydride/methyl vinyl ether copolymers and polyvinyl alcohols other than the above (B) and (C), nonionic, anionic and cationic surfactants, various additives such as anti-foaming agents, dispersants, anti-freezing agents, preservatives and antirusts if necessary in order to control their drying property, setting property, viscosity and film forming property.

The present invention will be described in more detail below by Examples and Comparative Examples, but the present invention is not limited thereto. In Examples and Comparative Examples, "parts" and "%" mean weight basis unless otherwise specified. The composition and the dispersion stability of aqueous liquid dispersion of Examples and Comparative Examples are summarized in Tables 1 and 3. Signs and the like in Table 3 are as follows.

Example 1

In a one-liter glass polymerization vessel equipped with a reflux cooler, a dropping funnel, a thermometer and a nitrogen blowing inlet, 350 g of ion-exchanged water, 20.7 g of PVA-1 (content of ethylene unit: 4.5% by mole, saponification degree: 98.1% by mole, polymerization degree: 1500) and 8.9 g of PVA-2 (content of maleic acid anhydride unit: 2.0% by mole, saponification degree: 97.8% by mole, polymerization degree: 1700) were placed and completely dissolved at 95°C. Subsequently, this aqueous solution of PVA was cooled, and then replaced with nitrogen. While stirring at 200 rpm, 36.6 g of vinyl acetate and 0.4 g of acrylic acid were added, the temperature was raised to 60°C, and then the polymerization was initiated by hydrogen peroxide/tartaric acid based redox initiators. From 15 minutes after initiating the polymerization, the mixture of 329.7 g of vinyl acetate and 3.3 g of acrylic acid was continuously added over 3 hours to complete the polymerization. A polyvinyl acetate emulsion having a solid content concentration of 50.1% and a particle diameter of 1 µm was obtained. To 100 parts by weight of the solid content of this emulsion, 5 parts of dibutyl phthalate was added and mixed as a plasticizer, and further 2.7 parts of polyamide amine epichlorohydrin adduct (25% aqueous solution, WS-4020 supplied by Seiko PMC Corporation) and 2.0 parts of aluminum nitrate were added to yield an aqueous liquid dispersion. The resulting aqueous liquid dispersion had high dispersion stability without aggregation and gelation. A film water resistance, a water resistant adhesive force and the shelf viscosity stability (pot life) were evaluated as follows.

Results are shown in Table 2.

(Evaluation of aqueous liquid dispersion and composition)

(a) Water resistance of film

The resulting aqueous liquid dispersion or the composition was flow cast on a PET film at 20°C 65% RH, and dried for 7 days to yield a dry film of 500 µm. This film was punched out into a piece with a diameter of 2.5 cm to use as a sample. The sample was immersed in water at 20°C for 24 hours, and then a water absorption rate (%) [{(Weight after immersion - Weight before immersion)/Weight before immersion} × 100] was calculated.

(b) Initial adhesiveness

The resulting aqueous liquid dispersion or composition was applied on hemlock firs (straight grain) at 150 g/m², which were then attached and pressed with a load of 7 kg/m² for 2 hours. Subsequently, the compressive shear strength was measured.

(c) Water resistant adhesive force

The resulting aqueous liquid dispersion or composition was applied on hemlock firs (straight grain) at 150 g/m², which were then attached and pressed with a load of 7 kg/m² for 16 hours. Subsequently, the pressure was released, and the hemlock firs were placed under the condition at 20°C 65% RH for 5 days, then immersed in boiling water for 4 hours, dried at 60°C for 20 hours, and further immersed in the boiling water for 4 hours. Subsequently, the compressive shear strength was measured in a wet state.

(d) Shelf viscosity stability (pot life)

The resulting aqueous liquid dispersion or composition was left to stand at 30°C, and after 30 days, the change in the viscosity was observed.

(e) Hydrolysis resistance (decrease in adhesive force with time)

The resulting aqueous liquid dispersion or composition was left to stand at 30°C for 30 days, then was applied on hemlock firs (straight grain) at 150 g/m², which were then attached and pressed with a load of 7 kg/m² for 16 hours. Subsequently, the pressure was released, and the hemlock firs were placed under the condition at 20°C 65% RH for 5 days, then immersed in boiling water for 4 hours, dried at 60°C for 20 hours, and further immersed in the boiling water for 4 hours. Subsequently, the compressive shear strength was measured in the wet state. The strength was compared with the strength measured above (3), and determined as follows. <ul id="ul0002" list-style="none" compact="compact"><li>⊚: No change: no problem although tended to be slightly lowered</li><li>×: Remarkably lowered</li></ul>

Example 2

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that the polyamide amine epichlorohydrin adduct was not added. The results are shown in Table 2.

Example 3

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that aluminum nitrate was not added. The results are shown in Table 2.

Example 4

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that 2.4 parts of a glyoxal based resin (42% aqueous solution, Cartabond TSI supplied by Clariant) was added in place of the polyamide amine epichlorohydrin adduct and aluminum nitrate. The results are shown in Table 2.

Comparative Example 1

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that the polyamide amine epichlorohydrin adduct and aluminum nitrate were not added. The results are shown in Table 2.

Example 5

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that the 351.5 g of vinyl acetate (initial addition: 35.2 g, sequential addition: 316.3 g) and 18.5 g of acrylic acid (initial addition: 1.9 g, sequential addition: 16.6 g) were used. The results are shown in Table 2.

Comparative Example 2

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that the 329.3 g of vinyl acetate (initial addition: 32.9 g, sequential addition: 296.4 g) and 40.7 g of acrylic acid (initial addition: 4.1 g, sequential addition: 36.6 g) were used. The dispersion stability was poor and aggregates were formed.

Example 6

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that N-methylol acrylamide at the same weight was used in place of acrylic acid. The results are shown in Table 2.

Example 7

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that N-butoxymethyl methacrylamide was used in place of acrylic acid. The results are shown in Table 2.

Example 8

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that acetoacetoxyethyl methacrylate at the same weight was used in place of acrylic acid. The results are shown in Table 2.

Example 9

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that diacetone acrylamide at the same weight was used in place of acrylic acid. The results are shown in Table 2.

Comparative Example 3

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that acrylic acid was not used. The results are shown in Table 2.

Example 10

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that 8.9 g of PVA-3 (content of ethylene unit: 2.5% by mole, saponification degree: 92.5% by mole, polymerization degree: 1650) and 20.7 g of PVA-4 (content of itaconic acid unit: 0.8% by mole, saponification degree: 87.8% by mole, polymerization degree: 1700) were used in place of PVA-1 and PVA-2. The results are shown in Table 2.

Example 11

An aqueous liquid dispersion was obtained in the same way as in Example 10 except that 18.5 g of PVA-5 (content of ethylene unit: 8.1% by mole, saponification degree: 99.1% by mole, polymerization degree: 500) was used in place of PVA-3. The results are shown in Table 2.

Example 12

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that 14.8 g of PVA-6 (content of ethylene unit: 1.4% by mole, saponification degree: 87.3% by mole, polymerization degree: 2000) and 3.7 g of PVA-7 (content of itaconic acid unit: 4.2% by mole, saponification degree: 95.4% by mole, polymerization degree: 600) were used in place of PVA-1 and PVA-2. The results are shown in Table 2.

Comparative Example 4

An aqueous liquid dispersion was obtained in the same way as in Example 12 except that 14.8 g of PVA-8 (content of ethylene unit: 12.0% by mole, saponification degree: 99.2% by mole, polymerization degree: 400) was used in place of PVA-6. The aqueous liquid dispersion was unstable and the aggregates were formed.

Comparative Example 5

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that PVA-2 was not used. The results are shown in Table 2.

Comparative Example 6

An aqueous liquid dispersion was obtained in the same way as in Example 10 except that PVA-3 was not used. The results are shown in Table 2.

Comparative Example 7

An aqueous liquid dispersion was obtained in the same way as in Example 10 except that 20.7g of unmodified polyvinyl alcohol PVA-9 (saponification degree: 88.2% by mole, polymerization degree: 1750) was used in place of PVA-1 and PVA-2 in Example 1. The results are shown in Table 2.

Example 13

In 290 g of ion-exchanged water, 5.4 g of PVA-3 (content of ethylene unit: 2.5% by mole, saponification degree: 92.5% by mole, polymerization degree: 1650) and 5.4 g of PVA-4 (content of itaconic acid unit: 0.8% by mole, saponification degree: 87.8% by mole, polymerization degree: 1700) were dissolved by heating, and the mixture was placed in a pressure resistant autoclave equipped with a nitrogen blowing inlet and a thermometer. After adjusting the pH to 4.0 with diluted sulfuric acid, 288 g of vinyl acetate and 3.6 g of methacrylic acid were placed. Then, the pressure was raised to 42 kg/cm² G using ethylene (corresponding to 68.4 g of ethylene). After raising the temperature to 60°C, the polymerization was initiated by adding a hydrogen peroxide-Rongalite based redox initiator. After 2 hours, when the concentration of residual vinyl acetate was 0.7%, the polymerization was terminated to yield a vinyl acetate-ethylene copolymer emulsion having a solid content concentration of 52.5% and a particle diameter of 1 µm. To 100 parts by weight of the solid content of this emulsion, 50 parts by weight of calcium carbonate was added and mixed, and further 5.0 parts of aluminum nitrate was added to yield an aqueous liquid dispersion composition. Using this composition, the same evaluation as in Example 1 was performed. The results are shown in Table 2.

Example 14

In a one-liter glass polymerization vessel equipped with a reflux cooler, a dropping funnel, a thermometer and a nitrogen blowing inlet, 350 g of ion-exchanged water, 11.1 g of PVA-1 (content of ethylene unit: 4.5% by mole, saponification degree: 98.1% by mole, polymerization degree: 1500) and 22.2 g of PVA-7 (content of itaconic acid unit: 4.2% by mole, saponification degree: 95.4% by mole, polymerization degree: 600) were placed and completely dissolved at 95°C. Subsequently, this aqueous solution of PVA was cooled, and then replaced with nitrogen. While stirring at 200 rpm, 25.9 g of vinyl acetate and 10.4 g of butyl acrylate were added, the temperature was raised to 60°C, and then the polymerization was initiated by adding 10 g of an aqueous solution of 2% potassium persulfate. From 15 minutes after initiating the polymerization, the mixture of 233.1 g of vinyl acetate, 93.2 g of N-butyl acrylate and 7.4 g of N-isobutoxymethyl methacrylamide was continuously added over 4 hours to complete the polymerization. A vinyl acetate-butyl acrylate copolymer emulsion having a solid content concentration of 49.5% and a particle diameter of 0.8 µm was obtained. To 100 parts by weight of the solid content of this emulsion, 50 parts by weight of wheat flour was added and mixed, and 5.0 parts of aluminum nitrate was added to yield an aqueous liquid dispersion composition. Using this composition, the same evaluation as in Example 1 was performed. The results are shown in Table 2.

Example 15

In 290 g of ion-exchanged water, 1.5 g of an anionic surfactant (Sundet BL supplied by Sanyo Chemical Industries, Ltd.) and 3.0 g of a nonionic surfactant (Nonipol 200 supplied by Sanyo Chemical Industries, Ltd.) were dissolved by heating, and the mixture was placed in a pressure resistant autoclave equipped with a nitrogen blowing inlet and a thermometer. After adjusting the pH to 4.0 with diluted sulfuric acid, 120 g of styrene and 3.0 g of methacrylic acid were placed. Then, 177 g of butadiene was placed from a pressure proof measurer, and after raising the temperature to 70°C, the polymerization was initiated by adding 10 g of the aqueous solution of 2% potassium persulfate with pressure. The internal pressure was decreased from 4.8 kg/cm² G with progress of the polymerization, and the polymerization was terminated when the pressure was decreased to 0.4 kg/cm² G after 15 hours. The resulting emulsion was adjusted to pH 6.0 with ammonia water to yield a styrene-butadiene copolymer emulsion having a solid content concentration of 48.5% and a particle diameter of 0.5 µm. To 100 parts by weight of the solid content of this emulsion, the mixture obtained by dissolving, by heating, 3 parts by weight of PVA- 5 (content of ethylene unit: 8.1% by mole, saponification degree: 99.1% by mole, polymerization degree: 500) and 3 parts by weight of PVA-7 (content of itaconic acid unit: 4.2% by mole, saponification degree: 95.4% by mole, polymerization degree: 600) in 34 parts by weight of ion-exchanged water was added and mixed, and further 2.7 parts of the polyamide amine epichlorohydrin adduct (25% aqueous solution, WS-4020 supplied by Seiko PMC Corporation) and 2.0 parts of aluminum nitrate were added to yield an aqueous liquid dispersion. The resulting aqueous liquid dispersion had high dispersion stability without aggregation and gelation, and was evaluated in the same way as in Example 1. The results are shown in Table 2.

Example 16

An aqueous liquid dispersion was obtained in the same way as in Example 1 except that 10% of vinyl acetate was changed to vinyl versatate (VeoVa-10). The results are shown in Table 2. It has been found in the above Examples and Comparative Examples that the aqueous liquid dispersion of the present invention exerts excellent performances as adhesives and the coating materials.

<tables id="tabl0001" num="0001"><table frame="all"><title>[Table 1]</title><tgroup cols="7"><colspec colnum="1" colname="col1" colwidth="25mm" /><colspec colnum="2" colname="col2" colwidth="25mm" /><colspec colnum="3" colname="col3" colwidth="22mm" /><colspec colnum="4" colname="col4" colwidth="22mm" /><colspec colnum="5" colname="col5" colwidth="26mm" /><colspec colnum="6" colname="col6" colwidth="21mm" /><colspec colnum="7" colname="col7" colwidth="28mm" /><thead><row><entry morerows="2" align="center" valign="middle" /><entry namest="col2" nameend="col5" align="center" valign="top">Aqueous liquid dispersion</entry><entry morerows="2" align="center" valign="top">Filler</entry><entry morerows="2" align="center" valign="top">Dispersion stability</entry></row><row><entry rowsep="0" align="right" valign="top">*1)</entry><entry rowsep="0" align="right" valign="top">*2)</entry><entry rowsep="0" align="right" valign="top">*2)</entry><entry rowsep="0" align="right" valign="top">*3)</entry></row><row><entry align="center" valign="top">(A)</entry><entry align="center" valign="top">(B)</entry><entry align="center" valign="top">(C)</entry><entry align="center" valign="top">(D)</entry></row></thead><tbody><row><entry valign="middle">Example 1</entry><entry align="center">VAC (99) AA(1)</entry><entry align="center">PVA-1(5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 2</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-1(5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 3</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-1 (5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">PAEpi (0.67)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 4</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-1 (5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">GOX (1.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 1</entry><entry align="center">VAC (99) AA(1)</entry><entry align="center">PVA-1 (5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">-</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 5</entry><entry align="center">VAC (95) AA (5)</entry><entry align="center">PVA-1(5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 2</entry><entry align="center">VAC (89) AA (11)</entry><entry align="center">PVA-1(5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">Aggregation</entry></row><row><entry valign="middle">Example 6</entry><entry align="center">VAC (99) NMA (1)</entry><entry align="center">PVA-1(5.6)</entry><entry align="center">PVA-2(2.4)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 7</entry><entry align="center">VAC (99) BMA (1)</entry><entry align="center">PVA-1(5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 8</entry><entry align="center">VAC (99) AAEM (1)</entry><entry align="center">PVA-1(5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 9</entry><entry align="center">VAC (99) DAA (1)</entry><entry align="center">PVA-1(5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 3</entry><entry align="center">VAC (100)</entry><entry align="center">PVA-1 (5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 10</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-3 (2.4)</entry><entry align="center">PVA-4 (5.6)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 11</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-5 (5)</entry><entry align="center">PVA-4 (5.6)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 12</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-6 (4)</entry><entry align="center">PVA-7 (1)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 4</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-8 (4)</entry><entry align="center">PVA-7 (1)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">Aggregation</entry></row><row><entry valign="middle">Comparative Example 5</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-1(5.6)</entry><entry align="center">-</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 6</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">-</entry><entry align="center">PVA-4 (5.6)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 7</entry><entry align="center">VAC (99) AA (1)</entry><entry namest="col3" nameend="col4" align="center">PVA-9 (5.6)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 13</entry><entry align="center">VAC (80) Et (19) MAA (1)</entry><entry align="center">PVA-3 (1.5)</entry><entry align="center">PVA-4 (1.5)</entry><entry align="center">Al(NO₃)₃ (5.0)</entry><entry align="center">CaCO₃</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 14</entry><entry align="center">VAC (70) BA (28) BMA (2)</entry><entry align="center">PVA-1 (3)</entry><entry align="center">PVA-7 (6)</entry><entry align="center">Al(NO₃)₃ (5.0)</entry><entry align="center">Wheat flour</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 15</entry><entry align="center">St (40) Bd (59) MAA (1)</entry><entry align="center">PVA-5 (3)</entry><entry align="center">PVA-7 (3)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 16</entry><entry align="center">VAC (89) VeoVa-10 (10) AA (1)</entry><entry align="center">PVA-1 (5.6)</entry><entry align="center">PVA-2 (2.4)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row></tbody></tgroup><tgroup cols="7" rowsep="0"><colspec colnum="1" colname="col1" colwidth="25mm" /><colspec colnum="2" colname="col2" colwidth="25mm" /><colspec colnum="3" colname="col3" colwidth="22mm" /><colspec colnum="4" colname="col4" colwidth="22mm" /><colspec colnum="5" colname="col5" colwidth="26mm" /><colspec colnum="6" colname="col6" colwidth="21mm" /><colspec colnum="7" colname="col7" colwidth="28mm" /><tbody><row><entry namest="col1" nameend="col7" align="justify">*1) Numbers in parentheses denote % by weight. *2) Numbers in parentheses denote parts by weight relative to 100 parts by weight of (A). *3) Numbers in parentheses denote parts by weight relative to 100 parts by weight of [(A)+(B)+(C)] VAC: vinyl acetate Et: ethylene BA: butyl acrylate St: styrene Bd: butadiene AA: acrylic acid MAA: methacrylic acid NMA: N-methylol acrylamide BMA: N-butoxymethyl methacrylamide AAEM: acetoacetoxyethyl methacrylate DAA: diacetone acrylamide VeoVa-10: vinyl versatate PVA-1: vinyl alcohol polymer having the ethylene content of 4.5% by mole, the saponification degree of 98.1% by mole and the polymerization degree of 1500. PVA-2: vinyl alcohol polymer having the maleic acid anhydride content of 2.0% by mole, the saponification degree of 97.8% by mole and the polymerization degree of 1700. PVA-3: vinyl alcohol polymer having the ethylene content of 2.5% by mole, the saponification degree of 92.5% by mole and the polymerization degree of 1650. PVA-4: vinyl alcohol polymer having the itaconic acid content of 0.8% by mole, the saponification degree of 87.8% by mole and the polymerization degree of 1700. PVA-5: vinyl alcohol polymer having the ethylene content of 8.1% by mole, the saponification degree of 99.1 % by mole and the polymerization degree of 500. PVA-6: vinyl alcohol polymer having the ethylene content of 1.4% by mole, the saponification degree of 87.3% by mole and the polymerization degree of 2000. PVA-7: vinyl alcohol polymer having the itaconic acid content of 4.2% by mole, the saponification degree of 95.4% by mole and the polymerization degree of 600. PVA-8: vinyl alcohol polymer having the ethylene content of 12.0% by mole, the saponification degree of 99.2% by mole and the polymerization degree of 400. PVA-9: vinyl alcohol polymer having the saponification degree of 88.2 % by mole and the polymerization degree of 1750. PAEpi: polyamide amine epichlorohydrin resin (25% aqueous solution, WS-4020 supplied by Seiko PMC Corporation) GOX: glyoxal based resin (42% aqueous solution, Cartabond TSI supplied by Clariant)</entry></row></tbody></tgroup></table></tables>

<tables id="tabl0002" num="0002"><table frame="all"><title>[Table 2]</title><tgroup cols="6"><colspec colnum="1" colname="col1" colwidth="27mm" /><colspec colnum="2" colname="col2" colwidth="29mm" /><colspec colnum="3" colname="col3" colwidth="28mm" /><colspec colnum="4" colname="col4" colwidth="27mm" /><colspec colnum="5" colname="col5" colwidth="28mm" /><colspec colnum="6" colname="col6" colwidth="29mm" /><thead><row><entry morerows="1" valign="middle" /><entry align="center" valign="top">Film water resistance</entry><entry align="center" valign="top">Initial adhesiveness</entry><entry align="center" valign="top">Boiling water resistant adhesive force on wood</entry><entry align="center" valign="top">Viscosity stability</entry><entry align="center" valign="top">Hydrolysis resistance</entry></row><row><entry align="center" valign="top">Water absorption rate (%)</entry><entry align="center" valign="top">Compressive shear strength (kg/cm2)</entry><entry align="center" valign="top">Compressive shear strength (kg/cm2) Numbers in parentheses denote material breaking rates (%)</entry><entry align="center" valign="top">Observation of state</entry><entry align="center" valign="top">Change in adhesive force</entry></row></thead><tbody><row><entry valign="middle">Example 1</entry><entry align="char" char=".">22.0</entry><entry align="char" char=".">30.0</entry><entry align="center">60 (100)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 2</entry><entry align="char" char=".">24.5</entry><entry align="char" char=".">25.0</entry><entry align="center">58 (90)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 3</entry><entry align="char" char=".">25.0</entry><entry align="char" char=".">25.0</entry><entry align="center">50 (80)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 4</entry><entry align="char" char=".">25.4</entry><entry align="char" char=".">26.0</entry><entry align="center">50 (70)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 1</entry><entry align="char" char=".">39.0</entry><entry align="char" char=".">24.0</entry><entry align="center">0 (0)</entry><entry align="center">No change</entry><entry align="center" /></row><row><entry valign="middle">Example 5</entry><entry align="char" char=".">22.9</entry><entry align="char" char=".">29.0</entry><entry align="center">65 (100)</entry><entry align="center">Slightly increased viscosity</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 2</entry><entry namest="col2" nameend="col6" align="center">Immeasurable due to aggregation</entry></row><row><entry valign="middle">Example 6</entry><entry align="char" char=".">23.2</entry><entry align="char" char=".">28.0</entry><entry align="center">55 (90)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 7</entry><entry align="char" char=".">24.1</entry><entry align="char" char=".">28.0</entry><entry align="center">60 (90)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 8</entry><entry align="char" char=".">24.0</entry><entry align="char" char=".">27.0</entry><entry align="center">50 (80)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 9</entry><entry align="char" char=".">25.8</entry><entry align="char" char=".">27.0</entry><entry align="center">45 (50)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 3</entry><entry align="char" char=".">30.1</entry><entry align="char" char=".">27.0</entry><entry align="center">5 (0)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 10</entry><entry align="char" char=".">24.0</entry><entry align="char" char=".">27.0</entry><entry align="center">55 (80)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 11</entry><entry align="char" char=".">25.6</entry><entry align="char" char=".">27.0</entry><entry align="center">50 (60)</entry><entry align="center">Slightly increased viscosity</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 12</entry><entry align="char" char=".">25.0</entry><entry align="char" char=".">27.0</entry><entry align="center">50 (50)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 4</entry><entry namest="col2" nameend="col6" align="center">Immeasurable due to aggregation</entry></row><row><entry valign="middle">Comparative Example 5</entry><entry align="char" char=".">29.5</entry><entry align="char" char=".">25.0</entry><entry align="center">5 (0)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 6</entry><entry align="char" char=".">31.5</entry><entry align="char" char=".">25.0</entry><entry align="center">10 (0)</entry><entry align="center">Slightly increased viscosity</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 7</entry><entry align="char" char=".">43.0</entry><entry align="char" char=".">25.0</entry><entry align="center">0 (0)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 13</entry><entry align="char" char=".">19.2</entry><entry align="char" char=".">22.0</entry><entry align="center">65 (100)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 14</entry><entry align="char" char=".">20.1</entry><entry align="char" char=".">21.0</entry><entry align="center">50 (70)</entry><entry align="center">No change</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 15</entry><entry align="char" char=".">21.5</entry><entry align="char" char=".">18.0</entry><entry align="center">40 (30)</entry><entry align="center">Slightly increased viscosity</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 16</entry><entry align="char" char=".">21.0</entry><entry align="char" char=".">28.0</entry><entry align="center">58 (100)</entry><entry align="center">No change</entry><entry align="center">⊚</entry></row></tbody></tgroup></table></tables>

Example 17

In a one-liter glass polymerization vessel equipped with a reflux cooler, a dropping funnel, a thermometer and a nitrogen blowing inlet, 350 g of ion-exchanged water, 29.6 g of PVA-10 (content of ethylene unit: 4.5% by mole, content of itaconic acid unit: 1.0% by mole, saponification degree: 98.1% by mole, polymerization degree: 1300) were placed and completely dissolved at 95°C. Subsequently, this aqueous solution of PVA was cooled, and then replaced with nitrogen. While stirring at 200 rpm, 36.6 g of vinyl acetate and 0.4 g of acrylic acid were added, the temperature was raised to 60°C, and then the polymerization was initiated by the hydrogen peroxide/tartaric acid based redox initiator.

From 15 minutes after initiating the polymerization, the mixture of 329.7 g of vinyl acetate and 3.3 g of acrylic acid was continuously added over 3 hours to complete the polymerization. A polyvinyl acetate emulsion having a solid content concentration of 50.0% and a particle diameter of 0.9 µm was obtained. To 100 parts of the solid content of this emulsion, 5 parts of dibutyl phthalate was added and mixed as the plasticizer, and further 2.7 parts of polyamide amine epichlorohydrin adduct (25% aqueous solution, WS-4020 supplied by Seiko PMC Corporation) and 2.0 parts of aluminum nitrate were added to yield a crosslinkable aqueous liquid dispersion composition. The resulting composition had the high dispersion stability without aggregation and gelation. The film water resistance, the water resistant adhesive force and the shelf viscosity stability (pot life) were evaluated. The results are shown in Table 4.

Example 18

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that the polyamide amine epichlorohydrin adduct was not added. The results are shown in Table 4.

Example 19

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that aluminum nitrate was not added. The results are shown in Table 4.

Example 20

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that 2.4 parts of the glyoxal based resin (42% aqueous solution, Cartabond TSI supplied by Clariant) was added in place of the polyamide amine epichlorohydrin adduct and aluminum nitrate. The results are shown in Table 4.

Comparative Example 8

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that the polyamide amine epichlorohydrin adduct and aluminum nitrate were not added. The results are shown in Table 4.

Example 21

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that the 351.5 g of vinyl acetate (initial addition: 35.2 g, sequential addition: 316.3 g) and 18.5 g of acrylic acid (initial addition: 1.9 g, sequential addition: 16.6 g) were used. The results are shown in Table 4.

Comparative Example 9

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that the 329.3 g of vinyl acetate (initial addition: 32.9 g, sequential addition: 296.4 g) and 40.7 g of acrylic acid (initial addition: 4.1 g, sequential addition: 36. 6 g) were used. The dispersion stability was poor and aggregates were formed.

Example 22

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that N-methylol acrylamide at the same weight was used in place of acrylic acid. The results are shown in Table 4.

Example 23

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that N-butoxymethyl methacrylamide at the same weight was used in place of acrylic acid. The results are shown in Table 4.

Example 24

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that acetoacetoxyethyl methacrylate at the same weight was used in place of acrylic acid. The results are shown in Table 4.

Example 25

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that diacetone acrylamide at the same weight was used in place of acrylic acid. The results are shown in Table 4.

Comparative Example 10

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that acrylic acid was not used. The results are shown in Table 4.

Example 26

An aqueous liquid dispersion was obtained in the same way as in Example 17 except that 29.6 g of PVA-11 (content of ethylene unit: 2.0% by mole, content of itaconic acid unit: 0.5% by mole, saponification degree: 89.9% by mole, polymerization degree: 2050) was used in place of PVA-10. The results are shown in Table 4.

Example 27

An aqueous liquid dispersion was obtained in the same way as in Example 26 except that 29.6 g of PVA-12 (content of ethylene unit: 8.1% by mole, content of maleic acid unit: 5.1% by mole, saponification degree: 99. 1% by mole, polymerization degree: 500) was used in place of PVA-11. The results are shown in Table 4.

Comparative Example 11

A crosslinkable aqueous liquid dispersion composition was obtained in the same way as in Example 27 except that 29.6 g of PVA-13 (content of ethylene unit: 12.0% by mole, content of maleic acid unit: 5.1% by mole, saponification degree: 99.2% by mole, polymerization degree: 480) was used in place of PVA-12. The composition was unstable and the aggregates were formed.

Comparative Example 12

An aqueous liquid dispersion was obtained in the same way as in Example 27 except that 29.6 g of PVA-14 (content of ethylene unit: 4.5% by mole, saponification degree: 98.1% by mole, polymerization degree: 1500) was used in place of PVA-12. The results are shown in Table 4.

Comparative Example 13

An aqueous liquid dispersion was obtained in the same way as in Example 27 except that 29.6 g of PVA-15 (content of itaconic acid unit: 1.2% by mole, saponification degree: 89.2% by mole, polymerization degree: 1700) was used in place of PVA-12. The results are shown in Table 4.

Comparative Example 14

An aqueous liquid dispersion was obtained in the same way as in Example 27 except that 29.6 g of unmodified polyvinyl alcohol PVA-16 (saponification degree: 88.2% by mole, polymerization degree: 1750) was used in place of PVA-12. The results are shown in Table 4.

Example 28

In 290 g of ion-exchanged water, 10.8 g of PVA-17 (content of ethylene unit: 1.5% by mole, content of itaconic acid unit: 2.2% by mole, saponification degree: 92.0% by mole, polymerization degree: 700) was dissolved by heating, and the mixture was placed in a pressure resistant autoclave equipped with a nitrogen blowing inlet and a thermometer. After adjusting the pH to 4.0 with diluted sulfuric acid, 288 g of vinyl acetate and 3.6 g of methacrylic acid were placed. Then, the pressure was raised to 42 kg/cm² G using ethylene (corresponding to 68.4 g of ethylene). After raising the temperature to 60°C, the polymerization was initiated by adding the hydrogen peroxide-Rongalite based redox initiator.

After 2 hours, when the concentration of residual vinyl acetate was 0.7%, the polymerization was terminated to yield a vinyl acetate-ethylene copolymer emulsion having a solid content concentration of 52.3 % and a particle diameter of 0.8 µm. To 100 parts of the solid content of this emulsion, 50 parts of calcium carbonate was added and mixed, and further 5.0 parts of aluminum nitrate was added to yield an aqueous liquid dispersion composition. Using this composition, the same evaluation as in Example 17 was performed. The results are shown in Table 4.

Example 29

In a one-liter glass polymerization vessel equipped with a reflux cooler, a dropping funnel, a thermometer and a nitrogen blowing inlet, 350 g of ion-exchanged water, 33.3 g of PVA-10 (content of ethylene unit: 4.5% by mole, content of itaconic acid unit: 1.0% by mole, saponification degree: 98.1% by mole, polymerization degree: 1300) were placed and completely dissolved at 95°C. Subsequently, this aqueous solution of PVA was cooled, and then replaced with nitrogen. While stirring at 200 rpm, 25.9 g of vinyl acetate and 10.4 g of butyl acrylate were added, the temperature was raised to 60°C, and then the polymerization was initiated by adding 10 g of an aqueous solution of 2% potassium persulfate.

From 15 minutes after initiating the polymerization, the mixture of 233.1 g of vinyl acetate, 93.2 g of N-butyl acrylate and 7.4 g of isobutoxymethyl methacrylamide was continuously added over 4 hours to complete the polymerization. A vinyl acetate-butyl acrylate copolymer emulsion having a solid content concentration of 49.6% and a particle diameter of 0.8 µm was obtained. To 100 parts by weight of the solid content of this emulsion, 50 parts by weight of wheat flour was added and mixed, and further 5.0 parts of aluminum nitrate was added to yield an aqueous liquid dispersion composition. Using this composition, the same evaluation as in Example 17 was performed. The results are shown in Table 4.

Example 30

In 290 g of ion-exchanged water, 1.5 g of an anionic surfactant (Sundet BL supplied by Sanyo Chemical Industries, Ltd.) and 3.0 g of a nonionic surfactant (Nonipol 200 supplied by Sanyo Chemical Industries, Ltd.) were dissolved by heating, and the mixture was placed in a pressure resistant autoclave equipped with a nitrogen blowing inlet and a thermometer. After adjusting the pH to 4.0 with diluted sulfuric acid, 120 g of styrene and 3.0 g of methacrylic acid were placed. Then, 177 g of butadiene was placed from the pressure proof measurer, and after raising the temperature to 70°C, the polymerization was initiated by adding 10 g of the aqueous solution of 2% potassium persulfate with pressure. The internal pressure was decreased from 4.8 kg/cm² G with progress of the polymerization, and the polymerization was terminated when the internal pressure was decreased to 0.4 kg/cm² G after 15 hours.

The resulting emulsion was adjusted to pH 6.0 with ammonia water to yield a styrene-butadiene copolymer emulsion having a solid content concentration of 48.5% and a particle diameter of 0.5 µm. To 100 parts of the solid content of this emulsion, the mixture obtained by dissolving, by heating, 6 parts by weight of PVA-12 (content of ethylene unit: 8.1% by mole, content of maleic acid unit: 5.1% by mole, saponification degree: 99.1% by mole, polymerization degree: 500) in 34 parts by weight of ion-exchanged water was added and mixed, and further 2.7 parts of polyamide amine epichlorohydrin adduct (25% aqueous solution, WS-4020 supplied by Seiko PMC Corporation) and 2.0 parts of aluminum nitrate were added to yield an aqueous liquid dispersion. The resulting aqueous liquid dispersion had high dispersion stability without aggregation and gelation, and was evaluated in the same way as in Example 17. The results are shown in Table 2. From the above results, it is obvious that the aqueous liquid dispersion of the present invention is excellent as an adhesive or a coating material.

<tables id="tabl0003" num="0003"><table frame="all"><title>[Table 3]</title><tgroup cols="6"><colspec colnum="1" colname="col1" colwidth="30mm" /><colspec colnum="2" colname="col2" colwidth="31mm" /><colspec colnum="3" colname="col3" colwidth="23mm" /><colspec colnum="4" colname="col4" colwidth="31mm" /><colspec colnum="5" colname="col5" colwidth="21mm" /><colspec colnum="6" colname="col6" colwidth="31mm" /><thead><row><entry morerows="1" valign="middle" /><entry namest="col2" nameend="col5" align="center" valign="top">Crosslinkable aqueous liquid dispersion composition</entry><entry morerows="1" align="center" valign="top">Dispersion stability</entry></row><row><entry align="center" valign="top">*1) (A)</entry><entry align="center" valign="top">*2) (D)</entry><entry align="center" valign="top">*3) (D)</entry><entry align="center" valign="top">Filler</entry></row></thead><tbody><row><entry valign="middle">Example 17</entry><entry align="center">VAC (99) AA(1)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 18</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 19</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">PAEpi (0.67)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 20</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">GOX (1.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 8</entry><entry align="center">VAC (99) AA(1)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">-</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 21</entry><entry align="center">VAC (95) AA (5)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 9</entry><entry align="center">VAC (89) AA (11)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">Aggregation</entry></row><row><entry valign="middle">Example 22</entry><entry align="center">VAC (99) NMA (1)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 23</entry><entry align="center">VAC (99) BMA (1)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 24</entry><entry align="center">VAC (99) AAEM (1)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 25</entry><entry align="center">VAC (99) DAA (1)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 10</entry><entry align="center">VAC (100)</entry><entry align="center">PVA-10 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 26</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-11 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 27</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-12 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 11</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-13 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">Aggregation</entry></row><row><entry valign="middle">Comparative Example 12</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-14 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 13</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-15 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Comparative Example 14</entry><entry align="center">VAC (99) AA (1)</entry><entry align="center">PVA-16 (8.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 28</entry><entry align="center">VAC (80) Et (19) MAA (1)</entry><entry align="center">PVA-17 (3.0)</entry><entry align="center">Al(NO₃)₃ (5.0)</entry><entry align="center">CaCO₃</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 29</entry><entry align="center">VAC (70) BA (28) BMA (2)</entry><entry align="center">PVA-10 (9.0)</entry><entry align="center">Al(NO₃)₃ (5.0)</entry><entry align="center">Wheat flour</entry><entry align="center">○</entry></row><row><entry valign="middle">Example 30</entry><entry align="center">St (40) Bd (59) MAA (1)</entry><entry align="center">PVA-12 (6.0)</entry><entry align="center">PAEpi (0.67) Al(NO₃)₃ (2.0)</entry><entry align="center">-</entry><entry align="center">○</entry></row></tbody></tgroup><tgroup cols="6" rowsep="0"><colspec colnum="1" colname="col1" colwidth="30mm" /><colspec colnum="2" colname="col2" colwidth="31mm" /><colspec colnum="3" colname="col3" colwidth="23mm" /><colspec colnum="4" colname="col4" colwidth="31mm" /><colspec colnum="5" colname="col5" colwidth="21mm" /><colspec colnum="6" colname="col6" colwidth="31mm" /><tbody><row><entry namest="col1" nameend="col6" align="justify">*1) Numbers in parentheses denote % by weight. *2) Numbers in parentheses denote parts by weight relative to 100 parts by weight of (A). *3) Numbers in parentheses denote parts by weight relative to 100 parts by weight of [(A)+(B)]. VAC: vinyl acetate Et: ethylene BA: butyl acrylate St: styrene Bd: butadiene AA: acrylic acid MAA: methacrylic acid NMA: N-methylol acrylamide BMA: N-butoxymethyl methacrylamide AAEM: acetoacetoxyethyl methacrylate DAA: diacetone acrylamide PAEpi: polyamide amine epichlorohydrin resin (25% aqueous solution, WS-4020 supplied by Seiko PMC Corporation) GOX: glyoxal based resin (42% aqueous solution, Cartabond TSI supplied by Clariant)</entry></row></tbody></tgroup></table></tables>

<tables id="tabl0004" num="0004"><table frame="all"><title>[Table 4]</title><tgroup cols="4"><colspec colnum="1" colname="col1" colwidth="41mm" /><colspec colnum="2" colname="col2" colwidth="41mm" /><colspec colnum="3" colname="col3" colwidth="43mm" /><colspec colnum="4" colname="col4" colwidth="42mm" /><thead><row><entry morerows="1" valign="middle" /><entry align="center" valign="top">Film water resistance</entry><entry align="center" valign="top">Boiling water resistant adhesive force on wood</entry><entry align="center" valign="top">Viscosity stability</entry></row><row><entry align="center" valign="top">Water absorption rate (%)</entry><entry align="center" valign="top">Compressive shear strength (kg/cm2) Numbers in parentheses denote material breaking rates (%)</entry><entry align="center" valign="top">Observation of state</entry></row></thead><tbody><row><entry valign="middle">Example 17</entry><entry align="char" char=".">20.0</entry><entry align="center">55 (90)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 18</entry><entry align="char" char=".">24.5</entry><entry align="center">50 (70)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 19</entry><entry align="char" char=".">26.0</entry><entry align="center">50 (70)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 20</entry><entry align="char" char=".">25.5</entry><entry align="center">45 (60)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Comparative Example 8</entry><entry align="char" char=".">35.0</entry><entry align="center">0 (0)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 21</entry><entry align="char" char=".">21.7</entry><entry align="center">60 (90)</entry><entry align="center">Slightly increased viscosity</entry></row><row><entry valign="middle">Comparative Example 9</entry><entry namest="col2" nameend="col4" align="center">Immeasurable due to aggregation</entry></row><row><entry valign="middle">Example 22</entry><entry align="char" char=".">22.1</entry><entry align="center">50 (80)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 23</entry><entry align="char" char=".">24.0</entry><entry align="center">50 (70)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 24</entry><entry align="char" char=".">24.2</entry><entry align="center">45 (70)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 25</entry><entry align="char" char=".">25.0</entry><entry align="center">40 (50)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Comparative Example 10</entry><entry align="char" char=".">29.5</entry><entry align="center">5 (0)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 26</entry><entry align="char" char=".">25.0</entry><entry align="center">55 (80)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 27</entry><entry align="char" char=".">25.2</entry><entry align="center">50 (60)</entry><entry align="center">Slightly increased viscosity</entry></row><row><entry valign="middle">Comparative Example 11</entry><entry namest="col2" nameend="col4" align="center">Immeasurable due to aggregation</entry></row><row><entry valign="middle">Comparative Example 12</entry><entry align="char" char=".">27.5</entry><entry align="center">5 (0)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Comparative Example 13</entry><entry align="char" char=".">32.2</entry><entry align="center">10 (0)</entry><entry align="center">Slightly increased viscosity</entry></row><row><entry valign="middle">Comparative Example 14</entry><entry align="char" char=".">42.0</entry><entry align="center">0 (0)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 28</entry><entry align="char" char=".">18.0</entry><entry align="center">60 (90)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 29</entry><entry align="char" char=".">21.0</entry><entry align="center">50 (70)</entry><entry align="center">No change</entry></row><row><entry valign="middle">Example 30</entry><entry align="char" char=".">21.0</entry><entry align="center">40 (30)</entry><entry align="center">Slightly increased viscosity</entry></row></tbody></tgroup></table></tables>

Industrial Applicability

The aqueous liquid dispersion of the present invention is excellent in water resistance, particularly boiling water resistance and is further excellent in shelf viscosity stability (pot life is long), and thus, is extremely useful for usage as various adhesives for woodwork and paper coating, paints and various coating materials for paper coating and textile processing by exploiting its properties.