Vinyl alcohol polymers, powders containing the same, methods for producing the same, paper processing agents, and dispersants for emulsion polymerization.

Abstract

This vinyl alcohol polymer contains a structural unit derived from at least one selected from the group consisting of a carboxy group-containing monomer and a derivative thereof, wherein the vinyl alcohol polymer has: a minimum degree of branching of at most 0.93 in the absolute molecular weight range of 200,000 to 800,000; a viscosity average degree of polymerization of at most 750; and a degree of saponification of at least 65 mol%.

Description

[Technical Field]

[0001] The present invention relates to vinyl alcohol polymers, powders containing the same, methods for producing the same, paper processing agents, and dispersants for emulsion polymerization. [Background technology]

[0002] Vinyl alcohol polymers (hereinafter sometimes referred to as "PVA") are known as water-soluble synthetic polymers and are widely used in applications such as paper processing, textile processing, adhesives, stabilizers for emulsion polymerization and suspension polymerization, inorganic binders, and films.

[0003] As a type of modified PVA, PVA containing structural units derived from carboxylic acids or their derivatives is known (see Patent Document 1). Such PVA is used in sizing agents for acidic paper containing aluminum sulfate, water-resistant coatings in combination with crosslinking agents, adhesives, etc., by utilizing the reactivity of carboxylic acids. Furthermore, because of its good water solubility, it is also useful as a packaging film for water-soluble substances such as pesticides, laundry detergents, and industrial chemicals, and is widely used. [Prior art documents] [Patent Documents]

[0004] [Patent Document 1] International Publication No. 2018 / 061272 [Overview of the project] [Problems that the invention aims to solve]

[0005] In the industrial production of PVA films, it is common practice to use an aqueous PVA solution with water as the solvent as the film-forming solution, taking into consideration environmental and economic factors. Similarly, when PVA is used as a component of coatings or adhesives, water is often used as the solvent. When using an aqueous PVA solution as a film-forming solution, coating, adhesive, or paper processing agent, it is preferable to prepare and use a high concentration of PVA to shorten drying time and reduce the energy required for drying. Similarly, when using PVA as a dispersant for emulsion polymerization, it is sometimes prepared and used at a high concentration. However, conventional aqueous PVA solutions have the disadvantage that their viscosity increases significantly when the concentration is high, resulting in a decrease in coating properties.

[0006] The present invention has been made to solve the above problems, and aims to provide PVA in which the increase in viscosity when prepared as a high-concentration aqueous solution is suppressed, a powder containing such PVA, a method for producing the same, and a paper processing agent and an emulsion polymerization dispersant containing such PVA. [Means for solving the problem]

[0007] The above purpose is, [1] PVA comprising a structural unit selected from the group consisting of monomers having a carboxyl group and derivatives thereof, wherein the minimum degree of branching in the range of absolute molecular weight from 200,000 to 800,000 is 0.93 or less, the viscosity-average degree of polymerization is 750 or less, and the degree of saponification is 65 mol% or more; [2] The PVA of [1], wherein at least one selected from the group consisting of monomers having a carboxyl group and derivatives thereof is at least one selected from the group consisting of ethylenically unsaturated dicarboxylic acids and their monoesters, diesters and anhydrides; [3] At least one selected from the group consisting of monomers having a carboxyl group and derivatives thereof is at least one selected from the group consisting of maleic acid, monoalkyl maleic acid, dialkyl maleic acid, maleic anhydride, fumaric acid, monoalkyl fumaric acid, and dialkyl fumaric acid, the PVA of [1]; [4] Any one of the PVAs of [1] to [3] that satisfies the following formula (I); S×P>250 ···(I) In formula (I), S is the content ratio (mol%) of the structural unit derived from at least one selected from the group consisting of the monomer having a carboxy group and its derivative with respect to all structural units. P is the viscosity average degree of polymerization. [5] Any one of the PVAs of [1] to [4] that satisfies the following formula (II); 1.0 < g A / g B <9.0 ···(II) In formula (II), g A is the branching degree at an absolute molecular weight of 200,000. g B is the branching degree at an absolute molecular weight of 800,000. [6] Any one of the PVAs of [1] to [5] in which the insoluble matter when 4 parts by mass of the above PVA is added to 96 parts by mass of water and stirred at 60°C for 1 hour is 0.1 ppm or more and less than 2000 ppm; [7] A powder containing any one of the PVAs of [1] to [6]; [8] The powder of [7] in which the content of the powder passing through a sieve with an opening of 180 μm is 12% by mass or less; [9] The powder of [7] or [8] in which the content of the powder passing through a sieve with an opening of 1.00 mm is 97% by mass or more and the content of the powder passing through a sieve with an opening of 500 μm is 40% by mass or more;

[10] A method for producing any one of the PVAs of [1] to [6], comprising a step (1) of obtaining a copolymer of at least one selected from the group consisting of a monomer having a carboxy group and its derivative and a vinyl ester, a step (2) of obtaining a saponified product of the copolymer, and a step (3) of heat-treating the saponified product, wherein the heat treatment temperature in the step (3) is 110°C or higher and the heat treatment time is 1 hour or longer; A method for producing a powder of any one of

[11] [7] to [9], comprising: a step (1) of obtaining a copolymer of at least one selected from the group consisting of a monomer having a carboxy group and its derivatives and a vinyl ester; a step (2) of obtaining a saponified product of the copolymer; and a step (3) of heat-treating the saponified product, wherein the content of the powder passing through a sieve with an aperture of 180 μm in the saponified product at the end of the step (3) is 12% by mass or less; A paper processing agent containing any one of

[12] [1] to [6] of PVA; A dispersant for emulsion polymerization containing any one of

[13] [1] to [6] of PVA; is achieved by providing any of the above.

Effects of the Invention

[0008] According to the present invention, it is possible to provide a PVA in which an increase in viscosity when made into a high-concentration aqueous solution is suppressed, a powder containing such a PVA, a method for producing these, and a paper processing agent and a dispersant for emulsion polymerization containing such a PVA.

Brief Description of the Drawings

[0009] [Figure 1] FIG. 1 is a graph showing the relationship between the absolute molecular weight and intrinsic viscosity ([η]branch and [η]linear) of PVA-1 and PVA-1' in the examples. [Figure 2] FIG. 2 is a graph showing the relationship between the absolute molecular weight and degree of branching (gm) of PVA-1 in the examples.

Modes for Carrying Out the Invention

[0010] Hereinafter, embodiments for carrying out the present invention will be described. In this specification, the upper and lower limit values of numerical ranges (such as the content of each component, values calculated from each component, and physical properties) can be combined as appropriate.

[0011] <pva> The PVA (vinyl alcohol polymer) of the present invention is a PVA containing structural units derived from at least one selected from the group consisting of monomers having a carboxyl group and derivatives thereof, wherein the minimum branching degree in the absolute molecular weight range of 200,000 to 800,000 is 0.93 or less, the viscosity-average degree of polymerization is 750 or less, and the degree of saponification is 65 mol% or more. Hereinafter, "at least one selected from the group consisting of monomers having a carboxyl group and derivatives thereof" may be referred to as "monomer (a)".

[0012] The PVA of the present invention contains vinyl alcohol units and structural units derived from monomer (a). This PVA is typically obtained by saponifying a vinyl ester polymer (a copolymer of monomer (a) and a vinyl ester) containing structural units derived from monomer (a). Examples of monomer derivatives having a carboxyl group include esters and anhydrides of monomers having a carboxyl group. The carboxyl group (-COOH) may exist in the form of a salt (-COONa, etc.). Structural units derived from monomer (a) may form crosslinked structures and bond to other structural units. Examples of monomer (a) include ethylenically unsaturated monocarboxylic acids, ethylenically unsaturated dicarboxylic acids, and their derivatives.

[0013] Examples of ethylenically unsaturated monocarboxylic acids and their derivatives include acrylic acid, methacrylic acid, methyl acrylate, ethyl acrylate, methyl methacrylate, and ethyl methacrylate.

[0014] Examples of ethylenically unsaturated dicarboxylic acids and their derivatives include ethylenically unsaturated dicarboxylic acids, their monoesters, their diesters, and their anhydrides. Examples of ethylenically unsaturated dicarboxylic acids include maleic acid, fumaric acid, citraconic acid, mesaconic acid, and itaconic acid. Examples of monoesters of ethylenically unsaturated dicarboxylic acids include monoalkyl unsaturated dicarboxylic acid esters such as monomethyl maleate, monoethyl maleate, monomethyl fumarate, monoethyl fumarate, monomethyl citraconic acid, monoethyl citraconic acid, monomethyl mesaconic acid, monoethyl mesaconic acid, monomethyl itaconic acid, and monoethyl itaconic acid. Examples of diesters of ethylenically unsaturated dicarboxylic acids include dialkyl unsaturated dicarboxylic acid esters such as dimethyl maleate, diethyl maleate, dimethyl fumarate, diethyl fumarate, dimethyl citraconic acid, diethyl citraconic acid, dimethyl mesaconic acid, diethyl mesaconic acid, dimethyl itaconic acid, and diethyl itaconic acid. Examples of ethylenically unsaturated dicarboxylic acid anhydrides include maleic anhydride and citraconic anhydride.

[0015] From the viewpoint of industrial availability and reactivity with vinyl esters, ethylenically unsaturated dicarboxylic acids, as well as their monoesters, diesters, and anhydrides, are preferred as monomer (a). Maleic acid, monoalkyl maleic acid, dialkyl maleic acid, maleic anhydride, fumaric acid, monoalkyl fumarate, and dialkyl fumarate are more preferred, and monomethyl maleic acid, dimethyl maleic acid, maleic anhydride, monomethyl fumarate, and dimethyl fumarate are particularly preferred. Monomer (a) can be used in the form of one or more types.

[0016] The lower limit of the content (S) of structural units derived from monomer (a) relative to the total structural units of the PVA of the present invention is preferably 0.1 mol%, more preferably 0.5 mol%, even more preferably 1.0 mol%, and particularly preferably 1.5 mol%. On the other hand, the upper limit of the above content (S) is preferably 15 mol%, more preferably 10 mol%, even more preferably 5 mol%, and even more preferably 3 mol%. By setting the above content (S) within the above range, the effect of carboxylic acid modification, that is, the effect of introducing structural units derived from monomer (a), can be fully exhibited, and the increase in viscosity when a high-concentration aqueous solution is prepared can be sufficiently suppressed. Furthermore, by setting the above content (S) below the above upper limit, the formation of excessive crosslinking is suppressed. The portion where excessive crosslinking occurs has reduced solubility in water and becomes an insoluble portion. Such insoluble portions cause uneven coating when used as an aqueous solution and make it difficult to prepare a high-concentration aqueous solution. Therefore, by keeping the above water content (S) below the above upper limit, the amount of insoluble matter tends to decrease, and the coating properties when prepared as an aqueous solution are improved. The above content (S) is the vinyl ester polymer before saponification of the PVA of the present invention. 1 This can be determined by 1H-NMR analysis.

[0017] In the PVA of the present invention, the minimum branching degree in the absolute molecular weight range of 200,000 to 800,000 is 0.93 or less. The branching degree is an index that represents the degree of branching structure of a polymer. A linear polymer, i.e., a polymer without a branched structure, has a branching degree of 1, and a value closer to 0 indicates a greater branching structure. For the PVA to be measured, the branching degree for each absolute molecular weight in the absolute molecular weight range of 200,000 to 800,000 is determined. The smallest branching degree in the above range is then defined as the minimum branching degree. Note that if the absolute molecular weight of the PVA is not distributed across the entire range of 200,000 to 800,000, for example, if it only contains PVA with an absolute molecular weight of 600,000 or less, the smallest branching degree in the absolute molecular weight range of 200,000 to 600,000 will be the minimum branching degree. In other words, the PVA of the present invention, which consists of multiple molecules, contains molecules with an absolute molecular weight in the range of 200,000 to 800,000, but the absolute molecular weight does not need to be distributed across the entire range of 200,000 to 800,000.

[0018] The branching degree g at each absolute molecular weight of the PVA of the present invention m is determined from the following formulas (1) and (2). g m ’ = [η] branch / [η] linear ···(1) g m = g m ’ (1 / ε) ···(2) In formula (1), [η] branch is the intrinsic viscosity at the absolute molecular weight x (x is 200,000 or more and 800,000 or less) of the PVA (branched PVA) of the present invention having a branched structure, and is a value calculated from a differential refractive index detector, a light scattering detector, and a viscosity detector. [η] linear is the intrinsic viscosity at the above absolute molecular weight x of linear PVA, and is similarly a value calculated from a differential refractive index detector, a light scattering detector, and a viscosity detector. Note that as the linear PVA, an unmodified PVA (saponified product of a vinyl acetate homopolymer) having a 4 mass% aqueous solution viscosity within ±20% of the PVA of the present invention to be measured and a saponification degree within ±3 mol% is used. The intrinsic viscosity at each absolute molecular weight of the PVA of the present invention and the linear PVA can be specifically measured by the method described in the examples. The ratio g m ’ of the intrinsic viscosity represented by the above formula (1) and the branching degree g m have the relationship of the above formula (2). In formula (2), ε is a structure factor, and ε = 0.7 is assumed.

[0019] In the PVA of the present invention, the minimum branching degree is 0.93 or less, and a sufficient branched structure (crosslinking) is formed. Therefore, according to the PVA of the present invention, an increase in viscosity when a high-concentration aqueous solution is prepared is suppressed. In order to further enhance such an effect, the upper limit of the above minimum branching degree is preferably 0.8, more preferably 0.6, and may be further preferably 0.4, 0.25, or 0.18 in some cases.

[0020] On the other hand, the lower limit of the minimum branching degree may be, for example, 0.01 or 0.05, with 0.11 being preferred and 0.20 being more preferred. By setting the minimum branching degree to or above the lower limit, the amount of insoluble matter resulting from excessive crosslinking can be reduced, and the coating properties of the aqueous solution can be improved.

[0021] The branching in the PVA is presumed to be formed by ester bonding between the carboxyl and hydroxyl groups of the PVA during heat treatment. Therefore, the minimum degree of branching can be adjusted by heat treatment conditions such as heat treatment temperature and time, the content of structural units derived from monomer (a), and the degree of saponification.

[0022] The PVA of the present invention includes PVA having an absolute molecular weight in the range of 200,000 to 800,000. Preferably, the PVA of the present invention includes PVA with an absolute molecular weight of 200,000 and PVA with an absolute molecular weight of 800,000, and more preferably, the absolute molecular weight is distributed across the entire range of at least 200,000 to 800,000.

[0023] The upper limit of the viscosity-average degree of polymerization (P) of the PVA of the present invention is 750, preferably 700, more preferably 600, and even more preferably 500. If the viscosity-average degree of polymerization (P) is as high as 750, the effect of suppressing the increase in viscosity when prepared as a high-concentration aqueous solution does not occur, and on the contrary, the viscosity tends to be higher than that of unmodified PVA. The lower limit of the viscosity-average degree of polymerization (P) may be, for example, 100, 150, or 200. The viscosity-average degree of polymerization (P) is a value measured in accordance with JIS K6726:1994. Specifically, it can be determined by the method described in the examples.

[0024] The lower limit of the vinyl alcohol unit content relative to the total structural units in the PVA of the present invention is preferably 65 mol%, more preferably 70 mol%, and in some cases even more preferably 80 mol% or 85 mol%. On the other hand, the upper limit of the vinyl alcohol unit content is preferably 99.9 mol%, and more preferably 99 mol%.

[0025] The lower limit of the degree of saponification of the PVA in this invention is 65 mol%, preferably 80 mol%, and more preferably 85 mol%. By setting the degree of saponification to above the lower limit, water solubility is increased and insoluble matter is reduced, making it easier to prepare a high-concentration, uniform PVA aqueous solution. On the other hand, the upper limit of the degree of saponification may be 100 mol%, but preferably 99.9 mol%, more preferably 99 mol%, and even more preferably 92 mol%. Setting the degree of saponification to below the upper limit tends to facilitate the formation of a sufficient branched structure by heat treatment. The degree of saponification is a value measured by the method described in JIS K6726:1994.

[0026] The PVA of the present invention preferably satisfies the following formula (I). S×P>250 ···(I) In formula (I), S is the percentage (mol%) of structural units derived from monomer (a) relative to the total structural units. P is the viscosity-average degree of polymerization.

[0027] When formula (I) is satisfied, a balance is struck between the degree of effect due to carboxylic acid modification (such as the formation of branched structures) and the degree of effect due to the degree of polymerization, resulting in improved coatability and other properties. Specifically, for example, when formula (I) is satisfied, uneven coating during application is suppressed, and the strength of the resulting film tends to increase. The lower limit of S×P is more preferably 300, and may be even more preferably 400, 500, 600, or 700. On the other hand, the upper limit of S×P is preferably 4,000, more preferably 3,000, and even more preferably 2,000.

[0028] With regard to the degree of branching described above, it is preferable that the PVA of the present invention satisfies the following formula (II). 1.0 <g A / g B <9.0 ···(II) In formula (II), g A This is the degree of branching at an absolute molecular weight of 200,000 (the degree of branching of the PVA in the present invention that has an absolute molecular weight of 200,000). B This is the degree of branching at an absolute molecular weight of 800,000 (the degree of branching of the PVA in the present invention whose absolute molecular weight is 800,000).

[0029] As described above, sufficient heat treatment promotes crosslinking, resulting in PVA with a small minimum branching degree. However, if there are inconsistencies in the degree of crosslinking due to differences in molecular weight, the excessively crosslinked PVA (usually the component with a larger molecular weight) tends to become insoluble in water, affecting the water solubility of PVA and the coating properties of the PVA aqueous solution. Furthermore, if the inconsistencies in crosslinking due to differences in molecular weight are large, the ratio g in equation (II) becomes A / g B The ratio g becomes larger. From this perspective, the above ratio g A / g B It is more preferable that the value be less than 7.0, even more preferable that it be less than 6.0, and even more preferable that it be less than 5.0, less than 4.0, less than 3.5, or less than 3.0.

[0030] When 4 parts by mass of the PVA of the present invention are added to 96 parts by mass of water and stirred at 60°C for 1 hour, the insoluble content is preferably 0.1 ppm or more and less than 2000 ppm. The above insoluble content may be more preferably less than 1,500 ppm, and even more preferably less than 1,000 ppm. By having a low amount of insoluble content, the coating properties of the aqueous PVA solution can be improved. On the other hand, the above insoluble content may be 1 ppm or more, 10 ppm or more, or 100 ppm or more. Note that "ppm" is based on mass, and the above insoluble content (ppm) indicates the percentage of insoluble content in the PVA. Specifically, the insoluble content can be determined by the method described in the examples.

[0031] The above ratio g A / g B The value and the content of the above-mentioned insoluble matter tend to increase as the proportion of PVA that is excessively heated and undergoes excessive crosslinking increases. Therefore, as described later, when heat-treating saponified vinyl ester polymers (copolymers), the above ratio g can be improved by removing fine powders that are easily overheated beforehand, performing heat treatment while removing fine powders, or removing fine powders after heat treatment. A / g B Furthermore, the proportion of the above-mentioned insoluble matter can be reduced.

[0032] The PVA of the present invention may contain structural units other than vinyl alcohol units, vinyl ester units, and structural units derived from monomer (a). Monomers that give the above other structural units include α-olefins such as ethylene, propylene, 1-butene, isobutene, and 1-hexene; acrylamide derivatives such as N-methylacrylamide, N-ethylacrylamide, and 2-acrylamide-2-methylpropanesulfonic acid; methacrylamide derivatives such as N-methylmethacrylamide and N-ethylmethacrylamide; vinyl ethers such as methyl vinyl ether, ethyl vinyl ether, n-propyl vinyl ether, isopropyl vinyl ether, and n-butyl vinyl ether; hydroxyl group-containing vinyl ethers such as ethylene glycol vinyl ether, 1,3-propanediol vinyl ether, and 1,4-butanediol vinyl ether; allyl acetate; and 3,4-diacetate. Examples include cy-1-butene; allyl ethers such as propyl allyl ether, butyl allyl ether, and hexyl allyl ether; monomers having an oxyalkylene group; hydroxyl group-containing α-olefins such as 3-buten-1-ol, 4-penten-1-ol, 5-hexen-1-ol, 7-octen-1-ol, 9-decen-1-ol, and 3-methyl-3-buten-1-ol; and monomers having a silyl group such as vinyltrimethoxysilane, vinylmethyldimethoxysilane, vinyldimethylmethoxysilane, vinyltriethoxysilane, vinylmethyldiethoxysilane, vinyldimethylethoxysilane, 3-(meth)acrylamidepropyltrimethoxysilane, and 3-(meth)acrylamidepropyltriethoxysilane.

[0033] The content of the above-mentioned other structural units relative to the total structural units of the PVA of the present invention is preferably 20 mol% or less, more preferably 10 mol% or less, and even more preferably 3 mol% or less, 1 mol% or less, or 0.1 mol% or less. On the other hand, the content of the above-mentioned other structural units may be, for example, 0.1 mol% or more, or 1 mol% or more.

[0034] The PVA of the present invention may not have a C12 aliphatic hydrocarbon group at its terminus, nor may it not have a C6 to C18 aliphatic hydrocarbon group at its terminus. Such terminal aliphatic hydrocarbon groups can be introduced, for example, by a chain transfer agent having a C6 to C18 aliphatic hydrocarbon group. Examples of such chain transfer agents include alkylthiols having C6 to C18, such as n-dodecanethiol.

[0035] <Powder> The powder of the present invention is a powder containing the PVA of the present invention. Because the powder contains the PVA of the present invention, even when the PVA is dissolved in water to a high concentration, the increase in the viscosity of the aqueous solution can be suppressed.

[0036] In the powder of the present invention, the PVA of the present invention is usually the main component. The main component refers to the component with the highest mass content. The lower limit of the content of the PVA of the present invention relative to the nonvolatile content of the powder of the present invention is preferably 50% by mass, more preferably 70% by mass, even more preferably 90% by mass, and in some cases, even more preferably 99% by mass. The upper limit of the content of the PVA of the present invention relative to the nonvolatile content of the powder of the present invention may be 100% by mass. Nonvolatile components other than the PVA of the present invention that may be contained in the powder of the present invention include PVA other than the PVA of the present invention, resins other than PVA, additives such as surfactants and plasticizers, and various compounds used during manufacturing. Furthermore, the volatile content in the powder of the present invention is usually 20% by mass or less, preferably 15% by mass or less, and more preferably 10% by mass or less. Volatile components that may be contained in the powder of the present invention include alcohol and water. The powder of the present invention may be a powder of the PVA of the present invention.

[0037] In the powder of the present invention, the upper limit of the content of powder (fine powder) that passes through a sieve with a mesh size of 180 μm is preferably 12% by mass, and may be more preferably 10% by mass, 8% by mass, or 5% by mass. As described above, fine powder is easily overheated by heat treatment, and crosslinking progresses too much, making it prone to becoming insoluble. Therefore, by keeping the content of powder that passes through a sieve with a mesh size of 180 μm below the above upper limit, the amount of insoluble material is reduced, improving the coating properties when used as an aqueous solution. The lower limit of the content of powder that passes through a sieve with a mesh size of 180 μm may be 0.1% by mass or 1% by mass. The mesh size of the sieve conforms to the nominal mesh size W of JIS Z 8801-1-2006 (the same applies hereinafter).

[0038] In the powder of the present invention, it is preferable that the content of powder that passes through a sieve with a mesh size of 1.00 mm is 97% by mass or more, and the content of powder that passes through a sieve with a mesh size of 500 μm is 40% by mass or more. The lower limit of the content of powder that passes through a sieve with a mesh size of 1.00 mm is more preferably 98% by mass, and even more preferably 99% by mass. On the other hand, the upper limit of the content of powder that passes through a sieve with a mesh size of 1.00 mm may be 100% by mass or 99.9% by mass. The upper limit of the content of powder that passes through a sieve with a mesh size of 500 μm may be 70% by mass or 60% by mass. When the powder of the present invention has such a size, the amount of coarse powder is small and the uniformity of the particle size is high, which improves water solubility and coating properties when used in an aqueous solution.

[0039] The particle size distribution in the powder of the present invention can be adjusted by sieving during the manufacturing process or after manufacturing.

[0040] It is preferable that the insoluble matter when 4 parts by mass of the powder of the present invention is added to 96 parts by mass of water and stirred at 60°C for 1 hour is 0.1 ppm or more and less than 2000 ppm. The insoluble matter may be more preferably less than 1500 ppm, and may be even more preferably less than 1000 ppm. By having such a small amount of insoluble matter, the coating property and the like of the aqueous solution obtained from the powder of the present invention can be enhanced. On the other hand, the insoluble matter may be 1 ppm or more, or may be 10 ppm or more or 100 ppm or more. The measurement of the insoluble matter of the powder can be carried out in the same manner as the measurement of the insoluble matter of PVA.

[0041] <Uses of PVA and powder> The PVA and powder of the present invention can be used in various uses similar to those of conventional PVA and its powder. Examples thereof are given below, but the present invention is not limited thereto. (1) Vinyl chloride dispersant use: Dispersing stabilizer and dispersing aid for suspension polymerization of vinyl chloride and vinylidene chloride (2) Coating agent use: Sizing agent, fiber treating agent, leather finishing agent, paint, antifogging agent, metal corrosion inhibitor, brightening agent for zinc plating, antistatic agent (3) Adhesive and binder use: Adhesive, tackifier, rewet adhesive, various binders, additives for cement and mortar (4) Agricultural use: Binder for agricultural chemicals, spreading agent for agricultural chemicals, coating agent for agriculture, soil conditioner, erosion inhibitor, dispersing agent for agricultural chemicals (5) Medical and cosmetic use: Granulation binder, coating agent, emulsifier, adhesive patch, binder, film preparation base material, film forming agent (6) Viscosity regulator use: Thickening agent (7) Coagulant use: Coagulant for suspended matter and dissolved matter in water, metal coagulant (8) Film use: Water-soluble film, polarizing film, barrier film, film for packaging fiber products, seed dressing sheet, vegetation sheet, seed tape, hygroscopic film (9) Molded product use: Fiber, pipe, tube, leak-proof film, water-soluble fiber for chemical lace, sponge (10) Resin raw material use: Raw material for polyvinyl butyral, photosensitive resin raw material, graft polymer raw material, various gel raw materials (11) Post-reaction applications: Post-reaction applications with low molecular weight organic compounds, high molecular weight organic compounds, and inorganic compounds. (12) Dispersants for emulsion polymerization: Dispersants for emulsion polymerization of vinyl acetate emulsion, dispersants for emulsion polymerization of ethylene-vinyl acetate (13) Paper processing agents: Surface sizing agents for general paper, sealants for release paper, overcoats for thermal paper, silica binders for inkjet paper

[0042] The PVA and powder of the present invention exhibit suppressed viscosity increases when dissolved in high-concentration aqueous solutions. Therefore, they are particularly suitable for applications in aqueous solution form. Such applications include adhesives, films (film-forming solutions), paper processing agents, and emulsion polymerization dispersants. Specifically, aqueous solutions containing the PVA of the present invention, adhesives containing the PVA of the present invention, films containing the PVA of the present invention, paper processing agents containing the PVA of the present invention, and emulsion polymerization dispersants containing the PVA of the present invention are also preferred embodiments of the present invention. The content of the PVA of the present invention in the above aqueous solutions, adhesives, film-forming solutions, etc., is, for example, 1% by mass or more and 30% by mass or less, and may be 5% by mass or more and 20% by mass or less, or 10% by mass or more. The above aqueous solutions, adhesives, film-forming solutions, etc., may further contain other components besides the PVA of the present invention and water. Such other components include those contained in conventionally known adhesives, film-forming solutions, etc.

[0043] <Paper processing agent> The paper processing agent of the present invention contains the PVA of the present invention. The paper processing agent of the present invention may be in the form of a powder or in the form of a liquid such as an aqueous solution. The paper coating agent of the present invention may be a coating agent for paper. The paper processing agent can be the same as conventionally known paper processing agents except for the use of the PVA of the present invention. The paper processing agent may further contain other components other than the PVA of the present invention. Examples of other components include pigments, dispersants, plasticizers, pH adjusters, defoamers, surfactants, resins other than the PVA of the present invention, etc.

[0044] <Dispersant for emulsion polymerization> The dispersant for emulsion polymerization of the present invention contains the PVA of the present invention. The dispersant for emulsion polymerization of the present invention may be in the form of powder or in a liquid form such as an aqueous solution. The dispersant for emulsion polymerization can be the same as the conventionally known dispersants for emulsion polymerization except for using the PVA of the present invention. The dispersant for emulsion polymerization may further contain other components besides the PVA of the present invention. Examples of other components include surfactants, buffers, polymerization degree regulators, PVAs other than the PVA of the present invention, and the like. The dispersant for emulsion polymerization is particularly preferably used as a dispersant for emulsion polymerization of ethylenically unsaturated monomers.

[0045] <Manufacturing Method of PVA and Powder> The manufacturing method of the PVA or powder of the present invention is not particularly limited, but the following method is preferred. That is, the manufacturing method of the PVA or powder of the present invention Step (1) of obtaining a copolymer of monomer (a) and vinyl ester, Step (2) of obtaining a saponified product of the above copolymer, and Step (3) of heat-treating the above saponified product is provided.

[0046] (Step (1)) In step (1), a copolymer of monomer (a) and vinyl ester is obtained. Specific examples and preferred examples of monomer (a) are as described above. Examples of vinyl esters include vinyl formate, vinyl acetate, vinyl propionate, vinyl valerate, vinyl caprate, vinyl laurate, vinyl stearate, vinyl benzoate, vinyl pivalate, vinyl versatic acid, and the like. Among them, vinyl acetate is preferred.

[0047] Examples of polymerization methods include known methods such as bulk polymerization, solution polymerization, suspension polymerization, and emulsion polymerization. Of these methods, bulk polymerization carried out without a solvent and solution polymerization carried out using a solvent such as an alcohol are preferred, and solution polymerization carried out in the presence of a lower alcohol is more preferred. As the lower alcohol, alcohols with 3 or fewer carbon atoms are preferred, methanol, ethanol, n-propanol, and isopropanol are more preferred, and methanol is even more preferred. When carrying out polymerization reactions using bulk polymerization or solution polymerization, either batch or continuous reaction methods can be employed.

[0048] Examples of initiators used in polymerization reactions include azo-based initiators such as 2,2'-azobisisobutyronitrile, 2,2'-azobis(2,4-dimethylvaleronitrile), and 2,2'-azobis(4-methoxy-2,4-dimethylvaleronitrile); and known initiators such as organic peroxide initiators such as benzoyl peroxide and n-propyl peroxycarbonate. There are no particular restrictions on the polymerization temperature during the polymerization reaction, but a range of 5°C to 200°C is appropriate.

[0049] When copolymerizing monomer (a) with a vinyl ester, copolymerizable monomers can be further copolymerized without impairing the spirit of the present invention. Specific examples of such other monomers are those described above as monomers that provide other structural units.

[0050] During copolymerization, a chain transfer agent may be added to adjust the degree of polymerization of the resulting PVA. Examples of chain transfer agents include aldehydes such as acetaldehyde, propionaldehyde, butyraldehyde, and benzaldehyde; ketones such as acetone, methyl ethyl ketone, hexanone, and cyclohexanone; mercaptans such as 2-hydroxyethanethiol and 3-mercaptopropionic acid; thiocarboxylic acids such as thioacetic acid; and halogenated hydrocarbons such as trichloroethylene and perchloroethylene. Among these, aldehydes and ketones are preferred. The amount of chain transfer agent added is determined according to the chain transfer constant of the added chain transfer agent and the desired degree of polymerization of the PVA, but generally, 0.1 to 10% by mass relative to the vinyl ester used is preferred.

[0051] (Process (2)) In step (2), the copolymer (vinyl ester polymer) obtained in step (1) is saponified in solution using an alkaline catalyst or an acid catalyst to obtain a saponified product. For the saponification reaction, conventionally known basic catalysts such as sodium hydroxide, potassium hydroxide, or sodium methoxide, or acidic catalysts such as p-toluenesulfonic acid, can be used for alcohol decomposition or hydrolysis reactions. Solvents used in the saponification reaction include alcohols such as methanol and ethanol; esters such as methyl acetate and ethyl acetate; ketones such as acetone and methyl ethyl ketone; and aromatic hydrocarbons such as benzene and toluene. These can be used individually or in combination of two or more. Among these, it is convenient and preferable to use methanol or a mixed solution of methanol and methyl acetate as the solvent and carry out the saponification reaction in the presence of sodium hydroxide, which is a basic catalyst.

[0052] The saponification reaction can be carried out using a belt reactor, kneader reactor, column reactor, etc. While there are no particular limitations on the saponification temperature, 20°C to 60°C is preferred. If a gel-like product precipitates as saponification progresses, the product should be crushed and the saponification process should be continued. Afterward, the resulting solution can be neutralized to terminate the saponification, and the saponified product can be obtained by washing. The saponification method is not limited to the method described above; other known methods can be used.

[0053] (Step (3)) In step (3), the saponified product obtained in step (2) is heat-treated. The heat treatment is preferably carried out in an air atmosphere or a nitrogen atmosphere. The heat treatment is preferably carried out on a solid, more preferably powdered (particulate) saponified product. The saponified product may be pre-dried to remove some of the volatile components before heat treatment. The heat treatment may be carried out while stirring the saponified product. The heat treatment can be carried out using, for example, a cylindrical stirring dryer.

[0054] In one embodiment of the method for producing PVA or powder according to the present invention, heat treatment is performed at a heat treatment temperature of 110°C or higher and for a heat treatment time of 1 hour or more. By performing heat treatment under these conditions, a sufficient crosslinking reaction occurs, and PVA with a minimum branching degree of 0.93 or less can be efficiently obtained. The lower limit of the heat treatment temperature may be 115°C or 120°C. The upper limit of the heat treatment temperature may be 150°C, 140°C, 130°C, or 125°C. The lower limit of the heat treatment time is preferably 2 hours, more preferably 3 hours, even more preferably 4 hours, and even more preferably 5 hours. The upper limit of the heat treatment time may be 24 hours, 12 hours, or 8 hours. By setting the heat treatment temperature and heat treatment time below the above upper limits, the formation of excessive crosslinks can be suppressed, and the insoluble content of the obtained PVA or powder can be reduced.

[0055] In one embodiment of the powder production method of the present invention, the content of powder that passes through a sieve with a mesh size of 180 μm in the saponified product at the end of step (3) is set to 12% by mass or less. The upper limit of the content of powder that passes through this sieve with a mesh size of 180 μm may preferably be 10% by mass, 8% by mass, or 5% by mass. By reducing the amount of fine powder that is easily overheated in this way, it is possible to efficiently obtain PVA powder with low insoluble content and suppressed excessive crosslinking formation.

[0056] Methods to ensure that the content of powder passing through a sieve with a mesh size of 180 μm in the saponified product at the end of step (3) is 12% by mass or less include sieving the saponified product before heat treatment, and removing the generated fine powder while performing heat treatment. For example, the heat treatment may be performed in multiple stages, and sieving may be performed between each heat treatment to remove the fine powder. Alternatively, the fine powder may be removed after the heat treatment.

[0057] Between step (2) and step (3), steps such as crushing the saponified material into particles and sieving the saponified material into particles may be provided. [Examples]

[0058] The present invention will be specifically described by the following examples, but the present invention is not limited in any way by these examples. In the following examples and comparative examples, "parts" and "%" refer to mass unless otherwise specified. The measurement methods used in the following examples and comparative examples are shown below.

[0059] [Viscosity average degree of polymerization] The viscosity-average degree of polymerization of PVA was measured in accordance with JIS K6726:1994. Specifically, PVA was saponified to a degree of saponification of 99.5 mol% or higher, purified, and then the intrinsic viscosity [η] (unit: liters / g) was measured in a 30°C sodium chloride aqueous solution (0.5 mol / L) for PVA containing structural units derived from monomer (a). For PVA not containing structural units derived from monomer (a), the intrinsic viscosity [η] (unit: liters / g) was measured in a 30°C aqueous solution. The viscosity-average degree of polymerization (P) of PVA was calculated from this intrinsic viscosity [η] using the following formula. P = ([η] × 10 4 (8.29) (1 / 0.62)

[0060] [Degree of saponification] The degree of saponification of PVA was determined by the method described in JIS K6726:1994.

[0061] [Degeneration rate] The denaturation rate of PVA (the content of structural units derived from monomer (a) in PVA) is determined using vinyl ester polymers, which are precursors of PVA. 1 This was determined using a method employing H-NMR. For example, when monomethyl maleate is used as monomer (a), the above denaturation rate can be determined by the following procedure. That is, the vinyl ester polymer, which is a precursor of PVA, is thoroughly reprecipitated and purified at least three times using n-hexane / acetone as the solvent, and the resulting purified product is dried at 70°C for one day to prepare a sample for analysis. This sample is dissolved in CDCl3, 1 The measurement is performed at room temperature using 1H-NMR. From the peak α (4.7-5.2 ppm) originating from the methine structure of the vinyl ester unit in the vinyl ester polymer and the peak β (3.6-3.8 ppm) originating from the methyl group of the methyl ester portion of the structural unit derived from monomer (a), the denaturation rate (content S of the structural unit derived from monomer (a)) can be calculated using the following formula. S (mol%) = {(number of protons in β / 3) / (number of protons in α + (number of protons in β / 3))} × 100

[0062] [Branching degree] First, using hexafluoroisopropanol as the mobile phase, gel permeation chromatography (GPC) measurements were performed using a differential refractive index detector, a light scattering detector, and a viscometer to determine the intrinsic viscosity for each absolute molecular weight between 200,000 and 800,000 for the target PVA (branched PVA) and the corresponding reference linear PVA. For the linear PVA, unmodified PVA was used, where the viscosity of a 4% by mass aqueous solution was within ±20% of the target PVA, and the degree of saponification was within ±3 mol%. The specific measurement conditions for GPC are shown below. Solvent: Hexafluoroisopropanol (containing sodium trifluoroacetate at a concentration of 20 mmol / L) Columns: Two Shodex HFIP-806M and one HFIP-LG Column temperature: 40℃ Flow rate: 1.0mL / min Sample concentration: 0.1 mass / vol% Injection volume: 100μL Standard: Polymethyl methacrylate for relative molecular weight Absolute molecular weight polymethyl methacrylate Intrinsic viscosity [η] of the PVA being measured for each measured absolute molecular weight. branch and the intrinsic viscosity [η] of linear PVA linear Using the above formulas (1) and (2), the degree of branching g for each absolute molecular weight is obtained. m We determined the smallest degree of branching g within the range of absolute molecular weight between 200,000 and 800,000. m This was defined as the minimum degree of branching. Furthermore, the degree of branching g at an absolute molecular weight of 200,000 was also defined. A And the degree of branching g at an absolute molecular weight of 800,000 B The ratio of g A / g B They sought it. As an example of the measurement results, the results for PVA-1 are shown in Figures 1 and 2. Figure 1 shows the absolute molecular weight and intrinsic viscosity ([η]) of PVA-1 and its corresponding linear PVA, PVA-1'. branch or [η] linear Figure 2 is a graph (Mark-Houwink plot) showing the branching degree g for each absolute molecular weight of PVA-1, calculated using equations (1) and (2) above, based on the results shown in Figure 1. m This is a graph plotting the values.

[0063] [Particle size distribution] The particle size distribution of PVA powder was measured using the dry sieving method described in JIS Z8815:1994. Using sieves with mesh sizes of 1.00 mm, 500 μm, and 180 μm, the percentage of the mass of powder passing through the 1.00 mm sieve (content: mass%), the percentage of the mass of powder passing through the 500 μm sieve (content: mass%), and the percentage of the mass of powder passing through the 180 μm sieve (content: mass%) relative to the mass of PVA powder before sieving was determined. The above mesh sizes conformed to the nominal mesh size W of JIS Z8801-1-2006.

[0064] [Insoluble matter] A 500 mL flask equipped with a stirrer was prepared in a water bath set to 60°C. 288 g of distilled water was added to the flask, and stirring was started at 300 rpm. 12 g of PVA powder was weighed and gradually added to the flask. After adding the entire amount of PVA powder (12 g), stirring was continued for 60 minutes to obtain a PVA solution. The obtained PVA solution was then filtered to remove undissolved particles (insoluble particles) through a metal filter with a mesh size of 63 μm. Next, the filter was thoroughly washed with 30°C warm water to remove any remaining solution, leaving only the insoluble particles on the filter. The filter was then dried in a 120°C heating dryer for 1 hour. The mass of the dried filter was compared to the mass of the filter before filtration to calculate the mass of the insoluble particles. The mass of the insoluble particles relative to the PVA powder used (12 g) was defined as the content percentage (ppm) of the insoluble matter.

[0065] [Aqueous solution viscosity] Aqueous PVA solutions were prepared, and their viscosity (mPa·s) was measured using a B-type viscometer (rotor speed 12 rpm, temperature 20°C). The PVA solutions were prepared as follows: 90 parts by mass of water were added to 10 parts by mass of PVA, and the mixture was heated to 90°C while stirring, then cooled after 1 hour. The same unmodified PVA used in the GPC measurement to determine the degree of branching was selected as the reference unmodified PVA. The viscosity of the unmodified PVA was also measured in the same manner. The viscosity ratio (viscosity of the reference unmodified PVA / PVA of the example or comparative example) was calculated. If the viscosity ratio was greater than 1.0, it was judged that the increase in viscosity was suppressed, and if the viscosity ratio was greater than 1.2, it was judged that the increase in viscosity was particularly sufficiently suppressed.

[0066] [Example 1] (Production of PVA-1) In a reactor equipped with a stirrer, reflux condenser, nitrogen inlet, comonomer dropper port, and polymerization initiator port, 700 parts by mass of vinyl acetate and 1050 parts by mass of methanol were charged, and the system was purged with nitrogen for 30 minutes while bubbling nitrogen. Monomethyl maleate was used as monomer (a), and a methanol solution of monomethyl maleate (10% concentration) was added and nitrogen was purged by bubbling nitrogen gas. The reactor was heated, and when the internal temperature reached 60°C, 0.84 parts by mass of 2,2'-azobisisobutyronitrile (AIBN) was added to start polymerization. The methanol solution of monomethyl maleate was added dropwise to the reactor to maintain a constant monomer composition ratio in the polymerization solution, and polymerization was carried out at 60°C for 5 hours, after which it was cooled to stop the polymerization. The total amount of monomer (a) added until polymerization was stopped was 12.1 parts by mass, the solid content concentration at the time of polymerization stoppage was 23.6%, and the polymerization rate was 60%. Next, unreacted monomers were removed by adding methanol occasionally under reduced pressure at 30°C to obtain a methanol solution of the vinyl ester polymer (concentration 36.7%). Then, 569.2 parts by mass of the methanol solution of the vinyl ester polymer (150.0 parts by mass of the polymer in the solution) was prepared by adding more methanol to this methanol solution. To this, 26.0 parts by mass of a 10% methanol solution of sodium hydroxide and water were added to bring the water content of the system to 1%, and saponification was carried out at 40°C (polymer concentration in the saponified solution: 25%, molar ratio of sodium hydroxide to vinyl acetate units in the polymer: 0.009, water content: 1%). A gel-like substance was formed about 10 minutes after the addition of the methanol solution of sodium hydroxide, so this was pulverized with a pulverizer, and after letting it stand at 40°C for 1 hour to allow saponification to proceed, 600 parts by mass of methyl acetate was added to neutralize the remaining alkali. After confirming that neutralization was complete using a phenolphthalein indicator, the solution was filtered to obtain a white solid. 600 parts by mass of methanol were added to this white solid and it was washed by standing at 40°C for 30 minutes. After repeating this washing operation twice, the white solid obtained by centrifugation was pre-dried overnight. Then, while removing fine powder, it was heat-treated in a dryer at 120°C for 6 hours to obtain PVA (PVA-1) powder. The physical properties and evaluation results of PVA-1 are shown in Table 2.

[0067] [Examples 2-7 and Comparative Examples 1-5] (Production of PVA-2 to PVA-12) Except for the following changes, which were made to the polymerization conditions such as the amounts of vinyl acetate and methanol used, the type and amount of monomer (a) used, the saponification conditions such as the concentration of the vinyl ester polymer in saponification and the molar ratio of sodium hydroxide to vinyl acetate units, and the heat treatment conditions as shown in Table 1, powders of PVA (PVA-2 to PVA-12) for Examples 2 to 7 and Comparative Examples 1 to 5 were obtained by the same method as in Example 1. The physical properties and evaluation results of these PVAs are shown in Table 2.

[0068] [Comparative Example 6] (Manufacturing of PVA-13) In a reactor equipped with a stirrer, reflux condenser, nitrogen inlet, and initiator addition port, 700 parts by mass of vinyl acetate and 1050 parts by mass of methanol were charged, and the system was purged with nitrogen for 30 minutes while bubbling with nitrogen. The reactor was heated, and when the internal temperature reached 60°C, 0.84 parts by mass of 2,2'-azobisisobutyronitrile (AIBN) was added to start polymerization. Polymerization was carried out at 60°C for 3 hours, and then cooled to stop the polymerization. At the time of polymerization cessation, the solid content concentration was 24.0%, and the polymerization rate was 60%. Subsequently, unreacted monomers were removed by occasionally adding methanol at 30°C under reduced pressure to obtain a methanol solution (concentration 36.7%) of the vinyl ester polymer. Next, 569.2 parts by mass of a methanol solution of a vinyl ester polymer (150.0 parts by mass of the polymer in the solution) was prepared by adding more methanol to the methanol solution. To this, 26.0 parts by mass of a 10% methanol solution of sodium hydroxide and water were added to bring the water content of the system to 1%, and saponification was carried out at 40°C (polymer concentration in the saponified solution: 25%, molar ratio of sodium hydroxide to vinyl acetate units in the polymer: 0.009, water content: 1%). After about 10 minutes after adding the methanol solution of sodium hydroxide, a gel-like substance was formed. This was pulverized using a pulverizer, and after letting it stand at 40°C for 1 hour to allow saponification to proceed, 600 parts by mass of methyl acetate was added to neutralize the remaining alkali. After confirming that neutralization was complete using a phenolphthalein indicator, the solution was filtered to obtain a white solid. 600 parts by mass of methanol was added to this white solid and it was washed by letting it stand at 40°C for 30 minutes. After repeating this washing operation twice, the white solid obtained by centrifugation was pre-dried overnight. Subsequently, the powder was heat-treated in a dryer at 120°C for 6 hours while removing fine particles to obtain PVA (PVA-13) powder. The physical properties and evaluation results of PVA-13 are shown in Table 2.

[0069] Furthermore, unmodified PVA (linear PVA) corresponding to each manufactured PVA (PVA-1 to 13) was produced in accordance with the manufacturing method of Comparative Example 6, to serve as a standard for measuring the degree of branching and evaluating the viscosity of aqueous solutions. However, no heat treatment was performed on the unmodified PVA after pre-drying.

[0070] [Table 1]

[0071] [Table 2]

[0072] As shown in Table 2, it can be seen that the viscosity increase of each PVA in Examples 1 to 7 is suppressed when prepared as a high-concentration aqueous solution. In particular, the PVAs in Examples 1 and 7 are excellent not only in their sufficient viscosity suppression effect but also in their low insoluble content. This is because the minimum degree of branching is within an appropriate range and the ratio of the degree of branching g A / g B It is thought that factors such as the small size of the plant are influencing the results.

[0073] On the other hand, each of the PVAs in Comparative Examples 1 to 3 had a high degree of polymerization, and the introduction of a branched structure actually resulted in a further increase in viscosity. The PVA in Comparative Example 4 had a low degree of saponification, and crosslinking proceeded easily with heat, resulting in many thermally crosslinked sites, and a uniform aqueous solution could not be obtained. Since a high-concentration aqueous solution of 10% by mass could not be obtained with the PVA in Comparative Example 4, it was determined that the problem of suppressing the increase in viscosity when a high-concentration aqueous solution is used could not be solved. The PVA in Comparative Example 5 had few branches, so no viscosity-suppressing effect was observed. The PVA in Comparative Example 6 did not contain structural units derived from monomer (a), and no branches were formed even after heat treatment, so no viscosity-suppressing effect was observed. [Industrial applicability]

[0074] The PVA of the present invention can be used in various applications such as coating agents, adhesives, film raw materials, paper processing agents, and dispersants for emulsion polymerization.< / pva>

Claims

1. A vinyl alcohol polymer obtained by saponifying a vinyl ester polymer containing a structural unit selected from the group consisting of monomers having a carboxyl group and derivatives thereof, wherein the minimum branching degree in the absolute molecular weight range of 200,000 to 800,000 is 0.93 or less, the viscosity-average degree of polymerization is 750 or less, and the degree of saponification is 65 mol% or more.

2. The vinyl alcohol polymer according to claim 1, wherein at least one selected from the group consisting of monomers having a carboxyl group and derivatives thereof is at least one selected from the group consisting of ethylenically unsaturated dicarboxylic acids, and their monoesters, diesters, and anhydrides.

3. The vinyl alcohol-based polymer according to claim 1, wherein at least one selected from the group consisting of monomers having a carboxyl group and derivatives thereof is at least one selected from the group consisting of maleic acid, monoalkyl maleic acid, dialkyl maleic acid, maleic anhydride, fumaric acid, monoalkyl fumaric acid, and dialkyl fumaric acid.

4. A vinyl alcohol-based polymer according to claim 1, satisfying the following formula (I). S×P>250...(I) In formula (I), S is the content (mol%) of structural units derived from at least one selected from the group consisting of monomers having a carboxyl group and their derivatives, relative to the total structural units. P is the viscosity-average degree of polymerization.

5. A vinyl alcohol-based polymer according to claim 1, satisfying the following formula (II). ..|. Ａ / Ｂ <..・・・(#). In formula (II), g Ａ This represents the degree of branching at an absolute molecular weight of 200,000. Ｂ This represents the degree of branching at an absolute molecular weight of 800,000.

6. The vinyl alcohol-based polymer according to claim 1, wherein when 4 parts by mass of the vinyl alcohol-based polymer are added to 96 parts by mass of water and stirred at 60°C for 1 hour, the insoluble content is 0.1 ppm or more and less than 2000 ppm.

7. A powder containing the vinyl alcohol-based polymer described in any one of claims 1 to 6.

8. The powder according to claim 7, wherein the content of powder that passes through a sieve with a mesh size of 180 μm is 12% by mass or less.

9. The powder according to claim 7, wherein the content of powder that passes through a sieve with a mesh size of 1.00 mm is 97% by mass or more, and the content of powder that passes through a sieve with a mesh size of 500 μm is 40% by mass or more.

10. A method for producing a vinyl alcohol polymer according to any one of claims 1 to 6, comprising the steps of: (1) obtaining a copolymer of a vinyl ester with at least one selected from the group consisting of monomers having a carboxyl group and derivatives thereof; (2) obtaining a saponified product of the copolymer; and (3) heat-treating the saponified product, wherein the heat treatment temperature in step (3) is 110°C or higher and the heat treatment time is 1 hour or longer.

11. A method for producing powder according to claim 7, comprising the steps of: (1) obtaining a copolymer of a vinyl ester with at least one selected from the group consisting of monomers having a carboxyl group and derivatives thereof; (2) obtaining a saponified product of the copolymer; and (3) heat-treating the saponified product, wherein the content of powder that passes through a sieve with a mesh size of 180 μm in the saponified product at the end of step (3) is 12% by mass or less.

12. A paper processing agent containing the vinyl alcohol polymer described in any one of claims 1 to 6.

13. A dispersant for emulsion polymerization containing the vinyl alcohol-based polymer described in any one of claims 1 to 6.

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