Patent Application
20220380499
The present invention relates to a modified vinyl alcohol-based polymer. Further, the present invention relates to a dispersion stabilizer for suspension polymerization, particularly to a dispersion stabilizer suitable for suspension polymerization of vinyl-based compounds typified by vinyl chloride.
When conducting suspension polymerization of a vinyl chloride monomer or a mixture of a vinyl chloride monomer and a monomer copolymerizable therewith, it is essential to use various dispersion stabilizers. Dispersion stabilizers such as polyvinyl alcohol, methylol cellulose, and gelatin are used. Among them, polyvinyl alcohol (hereinafter, also referred to as “PVA”) has excellent properties and is generally used most frequently. For example, methods of using a modified PVA having a specific oxyalkylene group in the side chain as a dispersion stabilizer for suspension polymerization of a vinyl-based compound have been proposed (see Patent Literatures 1 to 3).
Patent Literature 1 discloses a dispersion stabilizer for suspension polymerization of a vinyl-based compound, comprising a polyoxyalkylene modified vinyl alcohol-based copolymer (A), which is a vinyl alcohol-based polymer having polyoxyalkylene groups represented by the following general formula in a side chain, wherein the vinyl alcohol-based polymer has a viscosity average degree of polymerization of 600 to 5000, a saponification degree of 60 mol % or more, and a modification amount of the polyoxyalkylene groups of 0.1 to 10 mol %.
(In the formula, R1 represents a hydrogen atom or a methyl group, R2 represents a hydrogen atom or an alkyl group having 1 to 8 carbon atoms. m and n represent the number of repeating units of oxyalkylene unit, respectively. 1≤m≤10, 3≤n≤20.)
Patent Literature 1 describes the effects of the dispersion stabilizer as follows. When the dispersion stabilizer is used for suspension polymerization of a vinyl-based compound, high polymerization stability can be imparted by adding a small amount. As a result, blocking and scale adhesion due to unstable polymerization are suppressed, and vinyl-based polymer particles having a high bulk specific density, which have few coarse particles and a sharp particle size distribution, can be obtained.
Patent Literature 2 discloses a dispersion stabilizer for suspension polymerization comprising a polyoxyalkylene modified vinyl alcohol-based polymer (A) having polyoxyalkylene groups with 2 to 4 carbon atoms and a repeating unit number of 2 to 100 in a side chain, wherein the polyoxyalkylene modified vinyl alcohol-based polymer (A) has a viscosity average degree of polymerization of less than 500, a saponification degree of more than 70 mol %, and a modification rate of the polyoxyalkylene groups of 0.1 mol % or more and 10 mol % or less.
Patent Literature 2 discloses a polyoxyalkylene group represented by the following general formula as said polyoxyalkylene group.
(In the formula, R1 and R2 are both hydrogen atoms, or one is a methyl group and the other is a hydrogen atom. One of R3 and R4 is a methyl or ethyl group and the other is a hydrogen atom. R5 represents a hydrogen atom or an alkyl group having 1 to 8 carbon atoms. m and n represent the number of repeating units of oxyalkylene unit, respectively. 1≤m≤50 and 1≤n≤50.)
Patent Literature 2 describes the effects of the dispersion stabilizer as follows. When the dispersion stabilizer is used for suspension polymerization of a vinyl-based compound, coarse particles are less likely to be formed due to high polymerization stability, and particles having a uniform particle size can be obtained. Further, blocking and scale adhesion due to unstable polymerization are suppressed, and polymer particles having excellent plasticizer absorbability and monomer removal property can be obtained.
Patent Literature 3 discloses a dispersion stabilizer comprising a partially saponified polyvinyl alcohol-based resin having a saponification degree of 65 to 85 mol %, and 0.1 to 10 mol % of oxyalkylene groups in a side chain, and an iodine coloration degree value of 0.3 or more. According to Patent Literature 3, the oxyalkylene group is represented by the following general formula.
(In the formula, R1 and R2 represent a hydrogen atom or an alkyl group, n represents 0 or a positive integer, and X represents any of a hydrogen atom, an alkyl group, an alkylamide group, or an alkyl ester group, respectively.)
Patent Literature 3 describes the effects of the dispersion stabilizer as follows. Compared with conventional products, even in suspension polymerization using a buffer solution (agent), the protective colloidal property is not deteriorated, the polymerization stability is good, and the obtained vinyl-based polymer has a good performance such as good plasticizer absorption and good fisheye attenuation rate, and coarse particles of the vinyl polymer are not generated.
Usually, suspension polymerization of vinyl chloride is carried out in batch. Specifically, it is a method in which a water medium, a dispersion stabilizer, a polymerization initiator and a vinyl chloride monomer are charged in a polymerization can, and after adding required additives, the temperature is gradually raised to a polymerization temperature to carry out the reaction. However, in such a method, it takes a very long time for charging and raising the temperature, and the charging and raising the temperature themselves may occupy 10% or more of the polymerization time of one cycle, which reduces the productivity of the polymer. Therefore, it has been a cause of decrease in polymer productivity and has been a long-standing concern for those skilled in the art. Accordingly, various methods have been studied to solve the problem, and a hot water charging polymerization method (hot water charging method) that uses hot water of 40° C. or higher has been proposed. It shows a great effect in terms of process and time reduction during polymerization. In addition, in recent years, even in regions with higher temperatures such as Southeast Asia, production of vinyl chloride resin has become active due to the growth of infrastructure demand, and the number of cases where hot water of 40° C. or higher is used is increasing.
However, the dispersion stabilizers described in Patent Literatures 1 to 3 do not exhibit their original excellent effect as a dispersion stabilizer because they precipitate a part of the polyvinyl alcohol when the hot water is supplied, making the aqueous solution cloudy. Moreover, they may adversely affect the polymerization stability of the vinyl chloride-based monomers and the physical characteristics of the resin. Specifically, there has been an adverse effect that satisfactory properties cannot be constantly obtained with respect to the following required properties: (1) there should be few coarse particles in the produced vinyl chloride resin particles; (2) resin particles having uniform particle sizes as much as possible should be obtained, and scale adhesion should be prevented; (3) a resin having a high bulk density should be obtained, and as a result, molding processability during vinyl chloride processing should be improved.
Therefore, one object of the present invention is to provide a modified vinyl alcohol-based polymer suitable as a dispersion stabilizer for suspension polymerization, which has excellent handleability (for example, being able to adopt a hot water charging polymerization method that uses hot water of 40° C. or higher for suspension polymerization of vinyl-based compounds such as vinyl chloride) and satisfies the above-described required properties (1) to (3).
As a result of intensive studies to solve the above problem, the present inventors have found that it is effective to use a modified vinyl alcohol-based polymer as a dispersion stabilizer for suspension polymerization of a vinyl-based compound, wherein the modified vinyl alcohol-based polymer has a certain polyoxyalkylene unit (hereinafter referred to as “alkylene modifying group”) at a modification rate of 0.01 mol % to 5 mol %, and a certain organic acid unit at a modification rate of 0.1 mol % to 10 mol %.
Therefore, in one aspect, the present invention is exemplified as below.
[1]
A modified vinyl alcohol-based polymer, comprising a polyoxyalkylene unit, and an organic acid unit bonded to a polyvinyl alcohol chain, the polyoxyalkylene unit comprising a moiety represented by a general formula (I), the moiety being bonded to the polyvinyl alcohol chain only via an ether bond and/or a carbon-carbon bond,
wherein a ratio of a number of moles of monomer units constituting the polyvinyl alcohol chain of the modified vinyl alcohol-based polymer and bonded to the polyoxyalkylene unit to a total number of moles of the monomer units constituting the polyvinyl alcohol chain of the modified vinyl alcohol-based polymer is 0.01 mol % to 5 mol %, and a ratio of a number of moles of the organic acid unit to the total number of moles of the monomer units constituting the polyvinyl alcohol chain of the modified vinyl alcohol-based polymer is 0.1 mol % to 10 mol %.
(In the formula, R1 and R2 are independently a methyl group or an ethyl group or a hydrogen atom, and R3 is an alkyl group or a hydrogen atom. n represents a number of repeating units and is an integer of 5≤n≤70.)
[2]
The modified vinyl alcohol-based polymer according to [1], wherein at least a part of the polyoxyalkylene unit has a moiety represented by the general formula (II).
(In the formula, R1, R2, and R3 are as described in [1]. One of R4 and R5 is a methyl group or an ethyl group, and the other is a hydrogen atom. m represents a number of repeating units, and 1≤m≤30, provided that the moiety with the number of repeating units of n and the moiety with the number of repeating units of m are different.)
[3]
The modified vinyl alcohol-based polymer according to [1] or [2], wherein the organic acid unit comprises a carboxylic acid ester.
[4]
The modified vinyl alcohol-based polymer according to any one of [1] to [3] wherein a viscosity average degree of polymerization is 500 to 4000 and a saponification degree is 70 mol % or more.
[5]
A dispersion stabilizer for suspension polymerization, comprising the modified vinyl alcohol-based polymer according to any one of [1] to [4].
[6]
A method for manufacturing a vinyl-based resin, comprising conducting suspension polymerization by dispersing a vinyl-based compound monomer or a mixture of a vinyl-based compound monomer and a monomer copolymerizable therewith in water using the dispersion stabilizer for suspension polymerization according to [5].
[7]
A method for manufacturing the modified vinyl alcohol-based polymer according to any one of [1] to [4], comprising a step of copolymerizing a vinyl ester-based monomer with an unsaturated monomer having the polyoxyalkylene unit in coexistence with an unsaturated organic acid to obtain a modified vinyl ester polymer.
When suspension polymerization of a vinyl-based compound is carried out using the dispersion stabilizer for suspension polymerization of the present invention, the formation of coarse particles is reduced, and resin particles with high uniformity of particle size can be obtained. Further, since the formation of coarse particles is reduced, blocking during polymerization is suppressed, and particles having high particle size uniformity can be obtained, so that scale adhesion can be reduced. In addition, a resin having a high bulk density can be obtained, and the productivity during resin processing can be improved. Further, this dispersant can be used in a hot water charging polymerization method (hot water charging method) using hot water of 40° C. or higher, or in a region where the average temperature is high, without impairing the original properties. As described above, the dispersion stabilizer for suspension polymerization according to the present invention can have the required performance which was difficult to achieve by the prior arts.
In one embodiment, the dispersion stabilizer for suspension polymerization of the present invention comprises a modified vinyl alcohol-based polymer (hereinafter, also referred to as “modified PVA”), comprising a polyoxyalkylene unit, and an organic acid unit bonded to a polyvinyl alcohol chain. The polyoxyalkylene unit comprises a moiety represented by the general formula (I), and the moiety is bonded to the polyvinyl alcohol chain only via an ether bond and/or a carbon-carbon bond.
(In the formula, R1 and R2 are independently a methyl group or an ethyl group or a hydrogen atom, and R3 is an alkyl group or a hydrogen atom. n represents a number of repeating units and is an integer of 5≤n≤70.)
n is preferably 10 or more, more preferably 15 or more, and more preferably 20 or more. Further, n is preferably 70 or less, more preferably 60 or less.
It is preferable that at least a part of the polyoxyalkylene unit have two or more different moieties represented by the general formula (II). It is more preferable that all of the polyoxyalkylene units have two or more different oxyalkylene moieties represented by the general formula (II). Specifically, as the two or more moieties represented by the general formula (II), mention can be made to those in which the moiety having the number of repeating units of m is butylene oxide (R4 or R5 is an ethyl group and the other is a hydrogen atom) and the moiety having the number of repeating units of n is an ethylene oxide (both R1 and R2 are hydrogen atoms), and those in which the moiety having the number of repeating units of m is propylene oxide (R4 or R5 is a methyl group and the other is a hydrogen atom), and the moiety having the number of repeating units of n is ethylene oxide (both R1 and R2 are hydrogen atoms). Here, the moiety where the number of repeating units is m and the moiety where the number of repeating units is n may be in either a random or a block arrangement, but from the viewpoint that the physical properties due to the alkylene modifying group can be more easily expressed, a block arrangement is preferable.
(In the formula, R1 and R2 are independently a methyl group or an ethyl group or a hydrogen atom, and R3 is an alkyl group or a hydrogen atom. n represents a number of repeating units and is an integer of 5≤n≤70. One of R4 and R5 is a methyl group or an ethyl group, and the other is a hydrogen atom. m represents a number of repeating units, and 1≤m≤30, provided that the moiety with the number of repeating units of n and the moiety with the number of repeating units of m are different.)
m is preferably 3 or more, and more preferably 5 or more. Further, m is preferably 25 or less, more preferably 20 or less.
The alkyl group represented by R3 can be, for example, an alkyl group having 1 to 10 carbon atoms, preferably an alkyl group having 1 to 5 carbon atoms, and more preferably an alkyl group having 1 to 3 carbon atoms. Specific examples of the alkyl group represented by R3 include a methyl group, an ethyl group, an n-propyl group and an isopropyl group.
It is preferable that the moieties represented by the general formula (I) and the general formula (II) are bonded to the polyvinyl alcohol chain only via an ether bond and/or a carbon-carbon bond, respectively, from the viewpoint of preventing detachment due to a change in pH and failure to exhibit performance.
Examples of the organic acid unit in the modified PVA include unsaturated carboxylic acids such as acrylic acid, methacrylic acid, crotonic acid and maleic acid and salts thereof, as well as unsaturated carboxylic acid alkyl esters such as dimethyl maleate and monomethyl maleate. Further, unsaturated sulfonic acids such as ethylene sulfonic acid, allyl sulfonic acid and methallyl sulfonic acid and salts thereof, as well as unsaturated sulfonic acid esters and the like can be mentioned. The modified PVA may comprise one type of organic acid unit, or may comprise two types or more.
In the modified PVA of the present invention, the organic acid unit is not particularly limited, but an unsaturated carboxylic acid ester that forms a double bond in the polymer that can exhibit reactivity during polymerization of a vinyl-based compound at the time of saponification and drying is preferable.
It is important that the modified PVA has an alkylene modification rate of 0.01 mol % or more and 5 mol % or less, although depending on the type of the alkylene modifying group. If the alkylene modification rate exceeds 5 mol %, the balance of hydrophilic groups and hydrophobic groups contained in one molecule of the modified PVA cannot be maintained, and the water solubility of the modified PVA is lowered or the affinity with vinyl-based compound monomers is impaired, so it becomes difficult to use it as a dispersion stabilizer for suspension polymerization. Therefore, it is important that the alkylene modification rate is 5 mol % or less, preferably 4 mol % or less, and more preferably 2 mol % or less. On the other hand, when the alkylene modification rate is less than 0.01 mol %, although the water solubility is excellent, the number of modifying groups contained in the modified PVA is small, and the required physical properties are not sufficiently exhibited. Therefore, it is important that the alkylene modification rate is 0.01 mol % or more, preferably 0.05 mol % or more, and more preferably 0.1 mol % or more.
The alkylene modification rate is a ratio (mol %) of the number of moles of monomer units constituting the polyvinyl alcohol chain of the modified PVA and bonded to the polyoxyalkylene unit having the moiety represented by the above general formula (I) to the total number of moles of the monomer units constituting the polyvinyl alcohol chain of the modified PVA. The alkylene modification rate can be determined by proton NMR. Specifically, after the modified PVA is saponified to a saponification degree of 99.95 mol % or more, it is sufficiently washed with methanol to prepare a modified PVA for analysis. The prepared modified PVA for analysis is dissolved in heavy water, and a few drops of a heavy aqueous NaOH solution are added to adjust the pH to 14, and then the measurement is carried out at 80° C. using proton NMR. When calculating from the oxyethylene moiety (for example, R1═H, R2═H), the content is calculated by a conventional method from the integral value of the peak of 1.2 to 1.8 ppm attributed to the methylene group of the polyvinyl alcohol chain of the modified PVA and the integral value of the peak of 3.6 to 3.7 ppm attributed to the oxyethylene moiety. Specifically, assuming that the integral value of the methylene group of the polyvinyl alcohol chain of the modified PVA is b, the integral value of the oxyethylene moiety is a, and the number of repeating units of the oxyethylene moiety is x, considering the number of protons (2H for methylene group and 4H for ethylene group), the modification rate is calculated as {a/(4×x)}/(b/2)×100 (mol %). For example, when a=1, x=1, and b=100, it is calculated as 0.5 mol %. In addition, when calculating from the oxybutylene or oxypropylene moiety, the content is calculated by a conventional method from the integral value of the peak of 1.2 to 1.8 ppm attributed to the methylene group of the polyvinyl alcohol chain of the modified PVA and the integral value of peak of 0.80 to 0.95 ppm attributed to the terminal methyl group of the oxybutylene moiety (R1═H, R2═CH2CH3 (or R1═CH2CH3, R2═H)) or the oxypropylene moiety (R1═H, R2═CH3 (or R1 ═CH3, R2═H)). Specifically, assuming that the integral value of the methylene group of the polyvinyl alcohol chain of the modified PVA is b, the integral value of the oxybutylene moiety or the oxypropylene moiety is c, and the number of repeating units is y, considering the number of protons (2H for the methylene group and 3H for the methyl group), the modification rate is calculated as {c/(3×y)}/(b/2)×100 (mol %). For example, when c=1, y=1, and b=100, it is calculated as 0.67 mol %. In addition, when the modified PVA has both an oxyethylene moiety and an oxypropylene moiety or an oxybutylene moiety, the alkylene modification rate calculated based on the integral value of the peak attributed to the terminal methyl group of the oxypropylene moiety or the oxybutylene moiety is higher in measurement accuracy than the alkylene modification rate calculated from the oxyethylene moiety. Accordingly, if there is a difference between the two values, the alkylene modification rate calculated based on the integral value of the peak attributed to the terminal methyl group of the oxypropylene moiety or the oxybutylene moiety is adopted.
Further, the organic acid modification rate of the modified PVA needs to be 0.1 mol % to 10 mol %. If it is less than 0.1 mol %, it becomes difficult to keep the cloud point at 40° C. or higher, and the unsaturated double bond origin due to the carbonyl group decreases. As a result, a vinyl-based resin having an appropriate particle size cannot be obtained, and it becomes a vinyl-based resin having a low bulk density. Therefore, the organic acid modification rate needs to be 0.1 mol % or more, preferably 0.3 mol % or more, and more preferably 0.5 mol % or more. In addition, when the organic acid modification rate exceeds 10 mol %, the physical properties change significantly due to the change in pH, so that the protective colloidal property at the time of PVC polymerization may decrease, or it may become chemically unstable and may become insolubilized or gelled. Therefore, the organic acid modification rate needs to be 10 mol % or less, preferably 8 mol % or less, and more preferably 4 mol % or less.
The organic acid modification rate is a ratio (mol %) of the number of moles of the organic acid unit to the total number of moles of the monomer units constituting the polyvinyl alcohol chain of the modified PVA. The method for determining the organic acid modification rate is not particularly limited and can be obtained by acid value or the like, but it is convenient to measure it by proton NMR. Specifically, after the modified PVA is completely saponified to a saponification degree of 99.95 mol % or more, the modified PVA is thoroughly washed with methanol to prepare a modified PVA for analysis. The prepared modified PVA for analysis is dissolved in heavy water, and a few drops of a heavy aqueous NaOH solution are added to adjust the pH to 14, and then the measurement is performed at 80° C. to obtain a 1H-NMR spectrum. Calculation is conducted based on the integrated value of the peak of the methylene group (1.2 to 1.8 ppm) of the polyvinyl alcohol chain of the modified PVA. For example, when the organic acid unit has a carboxyl group, it is calculated from the peak of 2.2 to 2.9 ppm, which is a hydrogen atom of a carbon adjacent to a carboxyl group. When the organic acid unit is a sulfonyl group, it is calculated from the peak of 2.8 to 3.2 ppm, which is attributed to a hydrogen atom of a carbon adjacent to the sulfonic acid. In the case where the organic acid unit has a carboxyl group as an example, assuming the integral value of the methylene group of the polyvinyl alcohol chain of the modified PVA is b, and the integral value of the hydrogen atom of the carbon adjacent to the carboxyl group is a, considering the number of protons (methylene group is 2H), the modification rate is calculated as a/(b/2)×100 (mol %). For example, when a=1 and b=100, it is calculated as 2.0 mol %.
The viscosity average degree of polymerization of the modified PVA is preferably 500 or more, and more preferably 600 or more, in order to enhance the dispersion stability during suspension polymerization of a vinyl-based compound. Further, the viscosity average degree of polymerization of the modified PVA is preferably 4000 or less, more preferably 2000 or less, even more preferably 1500 or less, and even more preferably 1000 or less, in order to prevent the aqueous solution from becoming too viscous and difficult to handle.
The viscosity average degree of polymerization is determined according to JIS K6726: 1994. That is, the modified PVA is completely saponified, purified, and then it is determined from the intrinsic viscosity [η] measured in water or dimethyl sulfoxide (DMSO) at 30° C.
The saponification degree of the modified PVA is preferably 70 mol % or more in order to increase the water solubility and the cloud point, and to facilitate handling. In addition, the saponification degree of the modified PVA is preferably 99.9 mol % or less, preferably 90 mol % or less, and even more preferably 80 mol % or less, in order to increase the porosity of the particles obtained by suspension polymerization of the vinyl-based compound and to enhance plasticizer absorbability.
The saponification degree of the modified PVA is determined according to JIS K6726: 1994. That is, it can be determined by quantifying the residual acetic acid group (mol %) in the sample with sodium hydroxide and subtracting it from 100.
The method for manufacturing the modified PVA according to the present invention is not particularly limited, but for example, a method of reacting a hydroxyl group of PVA with a polyoxyalkylene group and an organic acid for grafting can be used. In particular, a method, which comprises a step of copolymerizing a vinyl ester-based monomer typified by vinyl acetate with an unsaturated monomer having the polyoxyalkylene unit having a moiety represented by the general formula (I) in coexistence with an unsaturated organic acid to obtain a modified vinyl ester polymer, and a step of saponifying the obtained modified vinyl ester polymer, is easy and economical, and is preferably used.
As an unsaturated monomer that induces the modified structure represented by the general formula (I), mention can be made to polyoxyalkylene alkenyl ether, polyoxyalkylene mono (meth) allyl ether, polyoxyalkylene monovinyl ether, and the like, and specifically, mention can be made to polyoxybutylene polyoxyethylene alkenyl ether, polyoxypropylene polyoxyethylene alkenyl ether, polyoxybutylene alkenyl ether, polyoxybutylene polyoxypropylene alkenyl ether, polyoxypropylene alkenyl ether, polyoxypropylene oxyethylene alkenyl ether, polyoxybutylene polyoxyethylene monoallyl ether, polyoxypropylene polyoxyethylene monoallyl ether, polyoxybutylene monoallyl ether, polyoxybutylene polyoxypropylene monoallyl ether, polyoxypropylene monoallyl ether, polyoxypropylene oxyethylene monoallyl ether, polyoxybutylene polyoxyethylene monovinyl ether, polyoxypropylene polyoxyethylene monovinyl ether, polyoxybutylene monovinyl ether, polyoxybutylene polyoxypropylene monovinyl ether, polyoxypropylene monovinyl ether, polyoxypropylene oxyethylene monovinyl ether, and the like. Among them, ethers represented by the following general formula (III) are more preferably used from the viewpoint of reactivity and properties. Specific examples of the polyoxyalkylene alkenyl ether represented by the general formula (III) include polyoxybutylene polyoxyethylene alkenyl ether.
(In the general formula (III), R1, R2, R3, R4, R5, m, and n are the same as those in the general formula (II).)
As examples of vinyl ester-based monomers, mentioned can be made to vinyl acetate, as well as vinyl formate, vinyl propionate, vinyl valerate, vinyl caprate, vinyl laurate, vinyl stearate, vinyl benzoate, vinyl pivalate and vinyl ester of versatic acid, and the like.
The method for inducing the organic acid unit is not particularly limited, but a method of copolymerizing with an unsaturated carboxylic acid (such as acrylic acid, methacrylic acid, crotonic acid, and maleic acid) or a salt thereof, or an olefin sulfonic acid (such as ethylene sulfonic acid, allyl sulfonic acid, and methallyl sulfonic acid) or a salt thereof or the like, which is copolymerizable with a vinyl ester-based monomer, is preferably used. Further, a method of inducing an organic acid unit (here, a carboxylic acid) by copolymerizing with an unsaturated carboxylic acid alkyl ester such as dimethyl maleate or monomethyl maleate and then saponifying is preferably used.
The temperature at which the vinyl ester-based monomer is copolymerized is not particularly limited, but is preferably 0° C. or higher and 200° C. or lower, and more preferably 30° C. or higher and 150° C. or lower. If the temperature at which the copolymerization is carried out is lower than 0° C., a sufficient polymerization rate cannot be obtained, which is not preferable. Further, when the temperature at which the polymerization is carried out is higher than 200° C., it is difficult to obtain the desired PVA. An example of methods of controlling the temperature adopted at the time of copolymerization to 0° C. or higher and 200° C. or lower includes a method of controlling it with an outer jacket using an appropriate heat medium such as water.
The polymerization method adopted for performing the present copolymerization may be any of batch polymerization, semi-batch polymerization, continuous polymerization and semi-continuous polymerization. As the polymerization method, any method can be adopted from known methods such as a massive polymerization method, a solution polymerization method, a suspension polymerization method, and an emulsion polymerization method. Among them, rather than suspension polymerization and emulsion polymerization in which it is necessary to control the polymerized particle size because modifying species used often have water-soluble and surface-active ability that affect the polymerized particle size, it is preferable to adopt a solution polymerization method or massive polymerization method in which polymerization is carried out in the presence of an alcohol-based solvent or without using a solvent. As the alcohol-based solvent used in the massive polymerization method or the solution polymerization method, methanol, ethanol, isopropanol and the like can be used, but the alcohol solvent is not limited thereto. Further, these solvents may be used alone, or two or more kinds of these solvents may be used in combination.
Examples of the polymerization initiator for radical polymerization of the vinyl ester-based monomer include, but not limited to, azo compounds such as azobisisobutyronitrile, azobis-2,4-dimethylvaleronitrile, azobis (4-methoxy-2,4-dimethylvaleronitrile), azobisdimethylvaleronitrile, and azobismethoxyvaleronitrile; peroxides such as acetyl peroxide, benzoyl peroxide, lauroyl peroxide, acetylcyclohexylsulfonyl peroxide, and 2,4,4-trimethylpentyl-2-peroxyphenoxyacetate; percarbonate compounds such as diisopropylperoxydicarbonate, di-2-ethylhexyl peroxydicarbonate, and diethoxyethylperoxydicarbonate; and perester compounds such as t-butyl peroxyneodecanoate, α-cumylperoxyneodecanoate, and t-butylperoxyneodecanoate. They can be used alone, or two or more of them can be used in combination.
Further, when the copolymerization is carried out at a high temperature, coloring of PVA due to decomposition of the vinyl ester-based monomer may be observed. In that case, for the purpose of preventing coloration, it is permissible to add an antioxidant such as citric acid to the polymerization system at about 1 ppm or more and 100 ppm or less (relative to the mass of the vinyl ester-based monomer).
The saponification method when manufacturing the modified PVA according to the present invention is not particularly limited, and it is preferable to saponify the polymer obtained by the above-mentioned method in accordance with a conventional method using alcohols which is also used as a solvent. Examples of the alcohol include methanol, ethanol, butanol and the like. The concentration of the polymer in alcohol can be selected from the range of 20 to 50% by mass. As the alkali catalyst, hydroxides of alkali metals such as sodium hydroxide, potassium hydroxide, sodium methylate, sodium ethylate and potassium methylate, and alkali catalysts such as alcoholate can be used. As the acid catalyst, an aqueous inorganic acid solution such as hydrochloric acid or sulfuric acid, and an organic acid such as p-toluenesulfonic acid can be used. The amount of these catalysts used needs to be 1 to 100 mmol equivalent with respect to the vinyl ester-based monomer. In such a case, the saponification temperature is not particularly limited, but is usually in the range of 10 to 70° C., preferably selected from the range of 30 to 50° C. The reaction is usually carried out for 0.5 to 3 hours.
The dispersion stabilizer for suspension polymerization according to the present invention may contain PVA other than the above-mentioned modified PVA and various other additives as long as the essence of the present invention is not impaired. As the additives, mention can be made to, for example, polymerization modifiers such as aldehydes, halogenated hydrocarbons, and mercaptans; polymerization inhibitors such as phenol compounds, sulfur compounds, and N-oxide compounds; pH regulators; cross-linking agents; preservatives; antifungal agents, anti-blocking agents; anti-foaming agent, and the like. From the viewpoint of significantly exerting the effect of the present invention, the dispersion stabilizer for suspension polymerization according to the present invention preferably comprises 10% by mass or more, more preferably 30% by mass or more, and even more preferably 70% by mass or more of the modified PVA.
The dispersion stabilizer for suspension polymerization according to the present invention can be particularly preferably used for suspension polymerization of vinyl-based compounds. As the vinyl-based compounds, mention can be made to vinyl halides such as vinyl chloride; vinyl esters such as vinyl acetate and vinyl propionate; acrylic acid, methacrylic acid, and esters and salts thereof; maleic acid, fumaric acid, and esters and anhydrides thereof; styrene, acrylonitrile, vinylidene chloride, vinyl ether, and the like. Among these, the dispersion stabilizer for suspension polymerization according to the present invention is particularly preferably used for suspension polymerization of vinyl chloride alone or polymerization of vinyl chloride with a monomer that can be copolymerized with vinyl chloride. As a monomer that can be copolymerized with vinyl chloride, mention can be made to vinyl esters such as vinyl acetate and vinyl propionate; esters of (meth) acrylic acid such as methyl (meth) acrylate and ethyl (meth) acrylate; α-olefins such as ethylene and propylene; unsaturated dicarboxylic acids such as maleic anhydride and itaconic acid; acrylonitrile, styrene, vinylidene chloride, vinyl ether, and the like.
The dispersion stabilizer for suspension polymerization according to the present invention can be used alone or in combination with other stabilizers such as cellulosic derivatives and surfactants.
By using the dispersion stabilizer for suspension polymerization according to the present invention, a vinyl chloride resin having a high bulk density of resin particles, a uniform particle size distribution, and excellent physical characteristics can be constantly obtained. Hereinafter, the method for polymerizing a vinyl-based compound will be specifically described with reference to examples, but the method is not limited thereto.
In the case of manufacturing resin particles of a vinyl-based compound such as vinyl chloride resin particles, the above-mentioned dispersion stabilizer for suspension polymerization is added in an amount of 0.01% by mass to 0.3% by mass, preferably 0.04% by mass to 0.15% by mass, with respect to the vinyl-based compound monomer. Further, the ratio of the vinyl-based compound to water can be a mass ratio of vinyl-based compound:water=1:0.9 to 1:3, preferably vinyl-based compound:water=1:1 to 1:1.5.
The polymerization initiator may be one conventionally used for polymerizing vinyl-based compounds, and examples include percarbonate compounds such as diisopropylperoxydicarbonate, di-2-ethylhexyl peroxydicarbonate, and diethoxyethylperoxydicarbonate; perester compounds such as t-butylperoxyneodecanoate, α-cumylperoxyneodecanoate, t-butylperoxyneodecanoate; peroxides such as acetylcyclohexylsulfonyl peroxide and 2,4,4-trimethylpentyl-2-peroxyphenoxyacetate; azo compounds such as azobis-2,4-dimethylvaleronitrile and azobis (4-methoxy-2,4-dimethylvaleronitrile); and further potassium persulfate, ammonium persulfate, hydrogen peroxide, and the like. They can be used alone, or two or more of them can be used in combination.
Further, it is also optional to add a polymerization modifier, a chain transfer agent, a gelation improver, an antistatic agent, a pH regulator and the like, which are appropriately used for the polymerization of vinyl-based compounds.
In carrying out the polymerization of the vinyl-based compound, the charging ratio of each component, the polymerization temperature and the like may be determined according to the conditions conventionally adopted in the suspension polymerization of the vinyl-based compound, and there is no particular reason for limitation.
Hereinafter, the present invention will be described in more detail with reference to examples.
1220 g of vinyl acetate, 1150 g of methanol, 1.6 g of dimethyl maleate, and 151 g of polyoxyalkylene alkenyl ether represented by the general formula (III) with m=5 to 9, n=45 to 55 (monomer A: a commercially available product) as a modifying species were charged into a polymerization can, and the inside of the system was replaced with nitrogen for 30 minutes. It was confirmed by NMR that the monomer A had m=5 to 9 and n=45 to 55. 0.3 g of azobisisobutyronitrile was charged into a polymerization can, and polymerization was performed at 60° C. for 11 hours while additionally adding dropwise 900 mL of a solution prepared by mixing vinyl acetate, methanol, and dimethyl maleate at a mass ratio of 40:58:2. After that, the dropping was stopped, and the mixture was cooled to stop the polymerization. Then, the unreacted vinyl acetate was removed by a conventional method, and the obtained modified vinyl acetate polymer was saponified with sodium hydroxide by a conventional method. Then, acetic acid was added to prepare a dispersion stabilizer having —COOH and —COONa. The viscosity average degree of polymerization, saponification degree and the modification rate of the obtained dispersion stabilizer were determined by the above-described analytical methods, and the viscosity average degree of polymerization was 750, the saponification degree was 72 mol %, the alkylene modification rate was 0.19 mol %, and the organic acid modification rate was 0.92 mol %.
An aqueous solution having a concentration of 4% by mass of the dispersion stabilizer obtained above was prepared. Approximately 5 cc was put in a glass test tube, a thermometer was placed in the measuring solution, and the temperature was raised while stirring to make the measuring solution cloudy. After that, the temperature at which the measuring solution became completely transparent was read while slowly cooling with stirring, which was used as the cloud point. As a result, the cloud point was 45° C.
In a 30 L stainless steel autoclave equipped with a stirrer, 12 kg of water at 30° C., 4.0 g of the dispersion stabilizer obtained above, 4.6 g of t-butylperoxyneodecanoate as a polymerization initiator and 1 g of α-cumylperoxyneodecanoate were charged while stirring. After degassing the autoclave in vacuum, 5 kg of vinyl chloride monomer was added, and polymerization was performed at 57° C. for 4 hours.
The average particle size, the particle size distribution, and the bulk specific density of the obtained vinyl chloride resin were evaluated by the following methods.
The average particle size was measured according to JIS Z8815: 1994. Sieves with 60 mesh (opening 250 μm), 80 mesh (opening 180 μm), 100 mesh (opening 150 μm), 150 mesh (opening 106 μm), 200 mesh (opening 75 μm) were used, and the particle size with a cumulative frequency of 50% (mass basis) (D50) was defined as the average particle size, and the difference between the particle size having a cumulative frequency of 80% (mass basis) (D80) and the particle size having a cumulative frequency of 20% (mass basis) (D20) was defined as the particle size distribution.
The bulk specific density was measured according to JIS K6720-2: 1999.
A modified vinyl acetate polymer was obtained in the same manner as in Example 1 except that the monomer A was changed to 101 g, and then a dispersion stabilizer was prepared by saponifying with sodium hydroxide. The viscosity average degree of polymerization, the saponification degree, the modification rate and the cloud point of the obtained dispersion stabilizer were determined by the above-described analytical methods. Further, suspension polymerization of vinyl chloride was carried out under the same conditions as in Example 1 except that the obtained dispersion stabilizer here was used, and the evaluations were carried out.
The modified vinyl acetate polymer obtained in Example 2 was saponified by adjusting the amount of sodium hydroxide to obtain a modified vinyl alcohol-based polymer dispersion stabilizer having a saponification degree of 76%. The viscosity average degree of polymerization, the saponification degree, the modification rate and the cloud point of the obtained dispersion stabilizer were determined by the above-described analytical methods. Further, suspension polymerization of vinyl chloride was carried out under the same conditions as in Example 1 except that the obtained dispersion stabilizer here was used, and the evaluations were carried out.
1220 g of vinyl acetate, 1350 g of methanol, 2.4 g of dimethyl maleate, and 52 g of polyoxyalkylene alkenyl ether represented by the general formula (III) as a modifying species with m=5 to 9, n=15 to 25 (monomer B: a commercially available product) were charged into a polymerization can, and the inside of the system was replaced with nitrogen for 30 minutes. It was confirmed by NMR that the monomer B had m=5 to 9, n=15 to 25. 0.3 g of azobisisobutyronitrile was charged into a polymerization can, and polymerization was performed at 60° C. for 11 hours while additionally adding dropwise 900 mL of a solution prepared by mixing vinyl acetate, methanol, and dimethyl maleate at a mass ratio of 45:52:3. After that, the dropping was stopped, and the mixture was cooled to stop the polymerization. Then, the unreacted vinyl acetate was removed by a conventional method, and the obtained modified vinyl acetate polymer was saponified with sodium hydroxide by a conventional method to prepare a dispersion stabilizer. The viscosity average degree of polymerization, the saponification degree, the modification rate and the cloud point of the obtained dispersion stabilizer were determined by the above-described analytical methods. Further, suspension polymerization of vinyl chloride was carried out under the same conditions as in Example 1 except that the obtained dispersion stabilizer here was used, and the evaluations were carried out.
1850 g of vinyl acetate, 1000 g of methanol, 1.2 g of dimethyl maleate, and 133 g of monomer B as a modifying species were charged into a polymerization can, and the inside of the system was replaced with nitrogen for 30 minutes. 0.3 g of azobisisobutyronitrile was charged into a polymerization can, and polymerization was performed at 60° C. for 11 hours while additionally adding dropwise 800 mL of a solution prepared by mixing vinyl acetate, methanol, and dimethyl maleate at a mass ratio of 45:52:2. After that, the dropping was stopped, and the mixture was cooled to stop the polymerization. Then, the unreacted vinyl acetate was removed by a conventional method, and the obtained modified vinyl acetate polymer was saponified with sodium hydroxide by a conventional method to prepare a dispersion stabilizer. The viscosity average degree of polymerization, the saponification degree, the modification rate and the cloud point of the obtained dispersion stabilizer were determined by the above-described analytical methods. Further, suspension polymerization of vinyl chloride was carried out under the same conditions as in Example 1 except that the obtained dispersion stabilizer here was used, and the evaluations were carried out.
1680 g of vinyl acetate, 1100 g of methanol, 7.3 g of dimethyl maleate, and 130 g of monomer A as a modifying species were charged into a polymerization can, and the inside of the system was replaced with nitrogen for 30 minutes. 0.3 g of azobisisobutyronitrile was charged into a polymerization can, and polymerization was performed at 60° C. for 11 hours while additionally adding dropwise 820 mL of a solution prepared by mixing vinyl acetate, methanol, and dimethyl maleate at a mass ratio of 64:28:8. After that, the dropping was stopped, and the mixture was cooled to stop the polymerization. Then, the unreacted vinyl acetate was removed by a conventional method, and the obtained modified vinyl acetate polymer was saponified with sodium hydroxide by a conventional method to prepare a dispersion stabilizer. The viscosity average degree of polymerization, the saponification degree, the modification rate and the cloud point of the obtained dispersion stabilizer were determined by the above-described analytical methods. Further, suspension polymerization of vinyl chloride was carried out under the same conditions as in Example 1 except that the obtained dispersion stabilizer here was used, and the evaluations were carried out.
A dispersion stabilizer was prepared in the same manner as in Example 1 except that instead of the monomer A, 56 g of polyoxyethylene glycol allyl ether with n=15 to 25 (monomer C) (Uniox PKA-5005 provided by NOF CORPORATION) was charged into a polymerization can. It was confirmed by NMR that the monomer C had n=15 to 25. The viscosity average degree of polymerization, the saponification degree, the modification rate and the cloud point of the obtained dispersion stabilizer were determined by the above-described analytical methods. Further, suspension polymerization of vinyl chloride was carried out under the same conditions as in Example 1 except that the obtained dispersion stabilizer here was used, and the evaluations were carried out.
A dispersion stabilizer was prepared in the same manner as in Example 1 except that instead of the monomer A, 74 g of polyethylene glycol polypropylene glycol allyl ether represented by the general formula (III) with m=15 to 25 and n=15 to 25 (monomer D) (Unilube PKA-5013 provided by NOF CORPORATION) was charged into a polymerization can. The viscosity average degree of polymerization, the saponification degree, the modification rate and the cloud point of the obtained dispersion stabilizer were determined by the above-described analytical methods. Further, suspension polymerization of vinyl chloride was carried out under the same conditions as in Example 1 except that the obtained dispersion stabilizer here was used, and the evaluations were carried out.
1600 g of vinyl acetate, 860 g of methanol, and 151 g of monomer A were charged into a polymerization can, and the inside of the system was replaced with nitrogen for 30 minutes. 0.3 g of azobisisobutyronitrile was charged into a polymerization can, and polymerization was performed at 60° C. for 9 hours, and then cooled to terminate the polymerization. Then, the unreacted vinyl acetate was removed by a conventional method, and the obtained modified vinyl acetate polymer was saponified with sodium hydroxide by a conventional method to prepare a dispersion stabilizer. The viscosity average degree of polymerization, the saponification degree, the modification rate and the cloud point of the obtained dispersion stabilizer were determined by the above-described analytical methods. Further, suspension polymerization of vinyl chloride was carried out under the same conditions as in Example 1 except that the obtained dispersion stabilizer here was used, and the evaluations were carried out.
1220 g of vinyl acetate, 1150 g of methanol, and 1.6 g of dimethyl maleate were charged into a polymerization can, and the inside of the system was replaced with nitrogen for 30 minutes. 0.3 g of azobisisobutyronitrile was charged into a polymerization can, and polymerization was performed at 60° C. for 12 hours while additionally adding dropwise 900 mL of a solution prepared by mixing vinyl acetate, methanol, and dimethyl maleate at a mass ratio of 40:58:2. After that, the dropping was stopped, and the mixture was cooled to stop the polymerization. Then, the unreacted vinyl acetate was removed by a conventional method, and the obtained modified vinyl acetate polymer was saponified with sodium hydroxide by a conventional method to prepare a dispersion stabilizer. The viscosity average degree of polymerization, the saponification degree, the modification rate and the cloud point of the obtained dispersion stabilizer were determined by the above-described analytical methods. Further, suspension polymerization of vinyl chloride was carried out under the same conditions as in Example 1 except that the obtained dispersion stabilizer here was used, and the evaluations were carried out.
3000 g of vinyl acetate, and 15 g of acetaldehyde as a modifying species were charged into a polymerization can, and the inside of the system was replaced with nitrogen for 30 minutes. 0.2 g of azobisisobutyronitrile was charged into a polymerization can, and polymerization was performed at 65 to 75° C. for 6 hours, and then cooled to terminate the polymerization. Then, a dispersion stabilizer was prepared according to Example 1. The viscosity average degree of polymerization, the saponification degree, the modification rate and the cloud point of the obtained dispersion stabilizer were determined by the above-described analytical methods. Further, suspension polymerization of vinyl chloride was carried out under the same conditions as in Example 1 except that the obtained dispersion stabilizer here was used, and the evaluations were carried out.
1600 g of vinyl acetate, 700 g of methanol, and 0.35 g of polyethylene glycol monomethacrylate (Blemmer PP-350 provided by NOF CORPORATION, hereinafter referred to as “monomer E”) as a modifying species were charged into a polymerization can, and the inside of the system was replaced with nitrogen for 30 minutes. Further, a comonomer solution in which monomer E was dissolved in methanol at a concentration of 5.7% by mass was prepared, and substituted with nitrogen by bubbling nitrogen gas. 2.5 g of azobisisobutyronitrile was charged into a polymerization can, and polymerization was performed at 60° C. for 9 hours while additionally adding dropwise 300 mL of comonomer solution (solution of monomer E dissolved in methanol at a concentration of 5.7% by mass), and then cooled to terminate the polymerization. The total amount of methanol added until the polymerization was stopped was 1066 g, and the total amount of monomer E was 22.3 g. After that, a dispersion stabilizer was prepared in the same manner as in Example 1. The viscosity average degree of polymerization, the saponification degree, the modification rate and the cloud point of the obtained dispersion stabilizer were determined by the above-described analytical methods. Further, suspension polymerization of vinyl chloride was carried out under the same conditions as in Example 1 except that the obtained dispersion stabilizer here was used, and the evaluations were carried out. In addition, the proton NMR of the obtained dispersion stabilizer was performed, but the peak derived from the modifying species which was observed in polyvinyl acetate was not observed in polyvinyl alcohol. This was because the polyoxyalkylene unit was bonded to the polyvinyl alcohol chain via an ester bond, so that the polyoxyalkylene unit was detached by the saponification reaction.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2019-127862 | Jul 2019 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2020/024268 | 6/19/2020 | WO |
