JP3516808B2 - Process for producing vinyl acetate polymer, process for producing saponified vinyl acetate polymer, and resin composition - Google Patents

Description

Detailed Description of the Invention

[0001]

TECHNICAL FIELD The present invention relates to a process for producing a vinyl acetate-based polymer, particularly an ethylene-vinyl acetate copolymer, which is obtained by saponifying the same, has less coloring, and less gel-like spots are formed during molding. The present invention relates to a method for producing a high-quality saponified vinyl acetate polymer, particularly a saponified ethylene-vinyl acetate copolymer, and a resin composition using the same.

[0002]

2. Description of the Related Art Saponified vinyl acetate polymers are used for various purposes by taking advantage of their hydrophilicity. Among them, the saponified product of ethylene-vinyl acetate copolymer is excellent in melt moldability, and particularly, oxygen shielding property, oil resistance,
Since it is excellent in antistatic property and mechanical strength, it is useful as various packaging materials such as films, sheets and containers. When the saponified product of ethylene-vinyl acetate copolymer is used as various packaging materials, not only the performance for the intended purpose but also a slight color appearance, fish eyes, gel-like spots, rough skin and transparency are problematic.

However, the saponified product of the ethylene-vinyl acetate copolymer has a problem that it tends to cause problems such as coloring and the formation of gel-like spots during melt molding. Therefore, conventionally, the following various methods have been proposed as a method for suppressing the coloring and the generation of gel-like spots.

For example, as to the method of adding an acid such as acetic acid and phosphoric acid and / or a salt thereof to an ethylene-vinyl acetate copolymer, JP-A-48-25048 and JP-A-5-25048 are known.
1-26993, JP-A-51-28891, JP-A-51
-49294, JP-A-51-91988, JP-A-52-
954, JP-A-52-955, JP-A-52-956, JP-A-56-20044, JP-A-56-41204, JP-A-61-95053, JP-A-61-95054, and JP-A-62-143954. Etc., many applications have been filed. That is, the saponified ethylene-vinyl acetate copolymer is a solution polymerization of ethylene and vinyl acetate in an organic solvent such as methanol using a radical initiator to drive out unreacted vinyl acetate, and then an alkali catalyst is added to the saponified product. It is said that by neutralizing and neutralizing, washing, adding an acid such as acetic acid and phosphoric acid and salts thereof, and further drying, a product with less generation of coloring and gelled spots can be obtained.

A method of adding a specific aromatic compound after the copolymerization of ethylene and vinyl acetate is disclosed in JP-A-61-1.
97603. That is, at the end of the polymerization of the ethylene-vinyl acetate copolymer, a specific aromatic compound (for example, 2,4-diphenyl-4-methyl-1-pentene) is added and then saponified to obtain the saponification of the polymer. It is said that the compound does not generate an offensive odor during melt molding, the obtained film has excellent hue, and has less fish eyes.

[0006]

As described above, there are various means for solving the problems such as coloring and gelled spots in the saponified vinyl acetate polymer, particularly in the saponified ethylene-vinyl acetate copolymer. It is taken. But,
Regarding the method of adding an acid such as acetic acid and phosphoric acid and / or a salt thereof to a saponified ethylene-vinyl acetate copolymer, neutralization and washing after saponification are not sufficient, and acetic acid and phosphoric acid If the addition amount of the acid and / or the salt thereof is not appropriate, coloring and generation of gel-like spots are likely to increase. In order to improve this drawback, sufficient washing after saponification and optimization of the addition amount of acids such as acetic acid and phosphoric acid and salts thereof have been carried out, but nevertheless, to a satisfactory level. The current situation is that we have not reached it.

Further, after the copolymerization of ethylene and vinyl acetate, a specific aromatic compound (for example, 2,4-diphenyl-4-) is used.
Regarding the method of adding methyl-1-pentene), as a result of additional examination by the present inventors, it could not be said that coloring and gel-like spots were sufficiently generated. The object of the present invention is to obtain a high-quality vinyl acetate-based polymer, which is obtained by saponifying a vinyl acetate-based polymer, particularly an ethylene-vinyl acetate copolymer, has less coloring, less gel-like spots are generated during molding. To get the compound.

[0008]

The above object is to provide a conjugated polyene having a boiling point of 20 ° C. or higher, preferably a boiling point higher than that of vinyl acetate, after polymerizing one or more monomers containing vinyl acetate. Vinyl acetate polymer to which a compound is added,
It is preferably achieved by providing a method for producing an ethylene-vinyl acetate copolymer and a method for saponifying the saponified vinyl acetate polymer. Further, it is effectively achieved by adding a conjugated polyene compound after polymerizing with a polymerization catalyst having a half-life of 5 hours or less in methanol at 60 ° C.

[0009]

BEST MODE FOR CARRYING OUT THE INVENTION The polyene compound according to the present invention has a structure in which carbon-carbon double bonds and carbon-carbon single bonds are alternately connected, and the number of carbon-carbon double bonds is 2.
It is a compound having more than one, a so-called conjugated double bond. It may be a conjugated diene having a structure in which two carbon-carbon double bonds and one carbon-carbon single bond are alternately connected, or three carbon-carbon double bonds and two carbons. −
It may be a conjugated triene having a structure in which carbon single bonds are alternately connected, or a conjugated polyene compound having a structure in which a number of carbon-carbon double bonds and carbon-carbon single bonds are alternately connected. It doesn't matter. Therefore,
Conjugated triene compounds such as 2,4,6-octatriene are also included in the polyene compound of the present invention. However, when the number of conjugated carbon-carbon double bonds is 8 or more, the polymer itself is colored. Therefore, a polyene having 7 or less conjugated carbon-carbon double bonds is preferable. Also,
The conjugated double bond composed of two or more carbon-carbon double bonds may be plural sets in one molecule without being conjugated with each other.
For example, a compound having three conjugated trienes in the same molecule, such as tung oil, is also included in the polyene compound of the present invention.

Further, in addition to the above-mentioned conjugated double bond consisting of two or more carbon-carbon double bonds, other functional groups such as carboxyl group and its salt, hydroxyl group, ester group,
Carbonyl group, ether group, amino group, imino group, amide group, cyano group, diazo group, nitro group, sulfone group, sulfoxide group, sulfide group, thiol group, sulfonic acid group and salts thereof, phosphoric acid group and salts thereof, Phenyl group,
It may have various functional groups such as a halogen atom, a double bond and a triple bond. Such a functional group may be directly bonded to a carbon atom in the conjugated double bond or may be bonded to a position apart from the conjugated double bond. Therefore,
The multiple bond in the functional group may be in a position capable of conjugating with the conjugated double bond. For example, 1-having a phenyl group
Phenyl butadiene and sorbic acid having a carboxyl group are also included in the polyene compound of the present invention.

Regarding the residual polyene compound in the final saponified product, from the viewpoint of being widely used in packaging containers and the like, it is not always desirable that the residual amount is too large due to problems such as odor generation and bleeding. From such a viewpoint, in order to obtain a molded article suitable for a packaging container having a small amount of residual polyene compound, the polyene compound is easily washed and removed from the resin in a washing step such as saponification and subsequent washing with water,
It is preferable to use a polyene compound having a functional group containing an oxygen atom. This is because such a functional group has a high polarity and an excellent affinity for water. Among them, those having a carboxyl group and a salt thereof, a hydroxyl group and an ester group are particularly preferable. This is because the carboxyl group and its salt and hydroxyl group are particularly excellent in affinity to water, and the ester group is hydrolyzed in the saponification step to be converted into carboxylic acid and its salt or hydroxyl group. Further, polyenecarboxylic acid, a salt thereof, and an esterified product thereof, whose solubility in water is further improved by forming an alkali salt in the saponification step, are most preferable.

Further, in industrial production, the raw materials are often recovered and reused, but from the viewpoint of easy separation of the recovered unreacted vinyl acetate or methanol and the polyene compound, the above-mentioned materials are generally used. Compared with a polyene compound having no functional group, a polyene compound having a functional group is less likely to be azeotroped with vinyl acetate or methanol, and is easily separated by distillation, which is also a preferable aspect.

By adding the conjugated polyene compound as shown above, a molded product of a saponified vinyl acetate polymer with less coloring and less gel-like spots can be obtained as compared with the case where it is not added. Is possible.

On the other hand, even if one carbon-carbon double bond and the aromatic ring have a structure in which they can be conjugated through one carbon-carbon single bond, they are not included in the polyene compound of the present invention. . For example, a conjugated compound with an aromatic ring such as styrene is insufficient in both the effect of suppressing coloration and the effect of suppressing the formation of gel-like spots. Further, even if one carbon-carbon double bond and carbon-heteroatom double bond have a structure in which they can be conjugated via one carbon-carbon single bond, they are included in the polyene compound of the present invention. I can't. For example, with a conjugated compound such as tiglic acid with a carbon-oxygen double bond of a carboxyl group, almost no effect of suppressing the formation of gel-like spots was observed. Here, the hetero atom refers to a nitrogen atom, a sulfur atom, a phosphorus atom, and the like in addition to the oxygen atom.

Further, even if the polyene compound has two or more carbon-carbon double bonds but is not a structure in which the double bonds are alternately connected to the carbon-carbon single bond and can be conjugated, the polyene compound of the present invention Not included in. Therefore, compounds having a plurality of non-conjugated carbon-carbon double bonds such as geraniol and squalene are not included in the polyene compound of the present invention.

It is important that the boiling point of the polyene compound used in the present invention is 20 ° C. or higher when measured at 1 atm. That is, if the boiling point is less than 20 ° C,
It is a gas at room temperature and pressure, and easily evaporates even when added to the reaction solution after polymerization, resulting in less coloring and less saponification of vinyl acetate-based polymer with less gelled spots. It is not possible to obtain a molded product.

For example, in the production of a saponified product of an ethylene-vinyl acetate copolymer, the above polyene compound is added after the polymerization. Usually, after that, ethylene remaining in the solution is evaporated off under normal pressure. Have steps. At this time, if the boiling point of the polyene compound is 20 ° C. or less, many polyene compounds are evaporated at this stage, and the effects of the present invention as described above cannot be obtained. In fact, when 1,3-butadiene having a boiling point of −4.4 ° C. was used as the polyene compound, most of it was evaporated together with ethylene when the ethylene was removed by evaporation. At that time, it was not possible to obtain a molded product of a saponified vinyl acetate-based polymer which was less colored and less gelled. From such a situation, it is considered highly possible that the presence of the polyene compound in the polymer in the subsequent steps is important in order to bring out the effect of the polyene compound in the present invention. The boiling point is more preferably 40 ° C. or higher from the viewpoint of less evaporation.

In addition, by using a polyene compound having a boiling point higher than that of vinyl acetate,
The effects described above can be obtained more remarkably. That is, after the ethylene is evaporated and removed as described above, it usually has a step of heating and evaporating the vinyl acetate to drive it out, but at this time, when the boiling point of the polyene compound is higher than the boiling point of the vinyl acetate, more, It is possible to obtain a saponified product of an ethylene-vinyl acetate copolymer that is less colored and less gelled. The evaporation of the polyene compound before the evaporation of vinyl acetate seems to reduce the effect obtained in the present invention. That is, it is important that the polymer contains a polyene compound in the step of expelling vinyl acetate. From this viewpoint, the boiling point of the polyene compound is preferably 100.
℃ or more, more preferably 130 ℃ or more.

Specific examples of the polyene compound in the present invention include isoprene, 2,3-dimethyl-1,3-butadiene, 2,3-diethyl-1,3-butadiene and 2-t-.
Butyl-1,3-butadiene, 1,3-pentadiene,
2,3-dimethyl-1,3-pentadiene, 2,4-dimethyl-1,3-pentadiene, 3,4-dimethyl-
1,3-pentadiene, 3-ethyl-1,3-pentadiene, 2-methyl-1,3-pentadiene, 3-methyl-1,3-pentadiene, 4-methyl-1,3-pentadiene, 1,3- Hexadiene, 2,4-hexadiene, 2,5-dimethyl-2,4-hexadiene, 1,3
-Octadiene, 1,3-cyclopentadiene, 1,3
-Cyclohexadiene, 1-phenyl-1,3-butadiene, 1,4-diphenyl-1,3-butadiene, 1-
Methoxy-1,3-butadiene, 2-methoxy-1,3
-Butadiene, 1-ethoxy-1,3-butadiene, 2
-Ethoxy-1,3-butadiene, 2-nitro-1,3
-Butadiene, chloroprene, 1-chloro-1,3-butadiene, 1-bromo-1,3-butadiene, 2-bromo-1,3-butadiene, fulvene, tropone, ocimene, ferrandrene, myrcene, farnesene, sembrene, Conjugated dienes having a conjugated structure of two carbon-carbon double bonds such as sorbic acid, sorbic acid ester, sorbate, and abietic acid; 1,3,5-hexatriene;
Carbon of 2,4,6-octatriene-1-carboxylic acid, eleostearic acid, tung oil, cholecalciferol, etc.
Conjugated trienes having a conjugated structure of three carbon double bonds; cyclooctatetraene, 2,4,6,8-decatetraene-1-carboxylic acid, retinol, retinoic acid, etc. Examples thereof include conjugated polyenes having a conjugated structure. In addition, 1,3-pentadiene,
Any of those having a plurality of stereoisomers such as myrcene and farnesene may be used. Two or more kinds of such polyene compounds may be used in combination. Further, a compound other than the polyene compound can be added simultaneously or separately.

By adding such a conjugated polyene compound, it is possible to obtain a molded product of a saponified vinyl acetate-based polymer with less coloring and less gelled spots as compared with the case where it is not added. That is, a polyene compound having a so-called conjugated double bond, which is a structure in which carbon-carbon double bonds and carbon-carbon single bonds are alternately connected and has two or more carbon-carbon double bonds, Therefore, the purpose is achieved by adding a substance having a boiling point of 20 ° C. or higher.

The catalyst used for the polymerization is not particularly limited, but 2,2'-azobisisobutyronitrile, 2,2'-azobis- (2,4-dimethylvaleronitrile), 2,2'-azobis-isobutyronitrile, 2'-azobis- (4-methyl-2,4
-Dimethylvaleronitrile), 2,2'-azobis-
Azonitrile initiators such as (2-cyclopropylpropionitrile) or isobutyryl peroxide, cumylperoxyneodecanoate, diisopropylperoxycarbonate, di-n-propylperoxydicarbonate, t-butylperoxyneo. Decanoate,
An organic peroxide type initiator such as lauroyl peroxide, benzoyl peroxide, t-butyl hydroperoxide, etc. can be used.

Further, in order to obtain a molded product of a saponified vinyl acetate polymer with less coloring and less generation of gelled spots, it is effective to use a polymerization catalyst having a short half-life. Specifically, its half-life in methanol at 60 ° C is 5
It is preferable to carry out the polymerization using a polymerization catalyst for a time not more than that. The half-life is more preferably 2 hours or less,
It is more preferably 1 hour or less. It is not clear why a molded product with less coloring and less gelled spots can be obtained when such a catalyst with a short half-life is used, but by using a catalyst with a short half-life, that is, a highly active catalyst, the polymerization reaction It is considered that the side reaction after the completion of the polymerization can be suppressed to the minimum while the reaction proceeds rapidly. Examples of such a catalyst having a short half-life include 2,2'-azobis- (4-methyl-2,4-dimethylvaleronitrile) (half-life 0.22 hours), diisopropyl peroxycarbonate (half-life 0.60). Hours), di-n-propylperoxydicarbonate (half-life 0.58 hours), isobutyryl peroxide (half-life 0.07 hours), and the like.

From the viewpoint of efficient use of the catalyst, it is preferable to use an organic peroxide type catalyst. This is because, in general, the efficiency of the initiator at the time of polymerization using an organic peroxide-based polymerization catalyst takes a larger value than that at the time of azonitrile-based polymerization. Here, the initiator efficiency refers to the ratio of the catalyst molecule that actually contributes to the polymerization reaction when decomposing and the catalyst molecule that decomposes without contributing to the polymerization reaction. (40% of the added amount is deactivated without contributing to the polymerization reaction)
In the case of organic peroxides, it is about 0.8 to 1.0, and it is known that almost all the amount contributes to the reaction. When the initiator efficiency is high as described above, there are few catalyst molecules that are deactivated without contributing to the reaction, and as a result, the same polymerization rate can be maintained with a smaller amount of catalyst, which is effective in reducing catalyst cost. . Examples of the organic peroxide-based polymerization catalyst include cumyl peroxy neodecanoate, diisopropyl peroxy carbonate, di-n-propyl peroxy dicarbonate, t-butyl peroxy neodecanoate, lauroyl peroxide, and benzoyl. Examples thereof include peroxides and t-butyl hydroperoxide.

The vinyl acetate polymer in the present invention includes a vinyl acetate homopolymer and a copolymer of vinyl acetate and another monomer. Among these copolymers, the ethylene-vinyl acetate copolymer is Especially, it is given as a typical one. Further, the saponified vinyl acetate-based polymer in the present invention includes those obtained by saponifying the vinyl acetate-based polymer, and typically saponified ethylene-vinyl acetate copolymer. .

Hereinafter, a method for producing an ethylene-vinyl acetate copolymer, which is a typical example of the vinyl acetate-based polymer of the present invention, and a saponified ethylene-vinyl acetate copolymer, which is a typical example of the saponified vinyl acetate-based polymer, will be described. The manufacturing method will be described in detail. Polymerization of ethylene and vinyl acetate may be any of solution polymerization, suspension polymerization, emulsion polymerization, bulk polymerization, and may be continuous type or batch type, for example,
The polymerization conditions in the case of batch type solution polymerization are as follows.

Solvent: Alcohols are preferable, but other organic solvents (such as dimethyl sulfoxide) which can dissolve ethylene, vinyl acetate and ethylene-vinyl acetate copolymer can be used. As alcohols, methyl alcohol, ethyl alcohol, propyl alcohol, n-butyl alcohol, t-butyl alcohol and the like can be used, and methyl alcohol is particularly preferable. Catalyst: An initiator such as an azonitrile-based initiator and an organic peroxide-based initiator as described above can be used. However, when a catalyst having a short half-life is used, it is not possible to batch-load the catalyst in a batch system, and it is necessary to continuously charge the catalyst. Temperature: 20 to 90 ° C, preferably 40 to 70 ° C. Time: 2 to 15 hours, preferably 3 to 11 hours. In the case of continuous polymerization, it is preferable that the average residence time in the polymerization tank is about the same. Polymerization rate: 10 to 90%, preferably 30 to 80% with respect to charged vinyl acetate. Resin content in solution after polymerization: 5-85%, preferably 20
˜70% Ethylene content in copolymer; 5 to 60 mol%, preferably 10 to 50 mol%.

In addition to ethylene and vinyl acetate, monomers copolymerizable with them, for example, α-olefins such as propylene, isobutylene, α-octene and α-dodecene; acrylic acid, methacrylic acid, crotonic acid, maleic acid. Acids, unsaturated acids such as itaconic acid or anhydrides thereof, salts, or mono- or dialkyl esters; nitriles such as acrylonitrile and methacrylonitrile; amides such as acrylamide and methacrylamide; ethylene sulfonic acid, allyl sulfonic acid, It is also possible to coexist an olefin sulfonic acid such as methallyl sulfonic acid or a salt thereof; an alkyl vinyl ether, a vinyl ketone, N-vinylpyrrolidone, vinyl chloride, vinylidene chloride and the like.

After the polymerization for a predetermined period of time and after reaching a predetermined polymerization rate, at least one polyene compound is added to evaporate and remove unreacted ethylene gas, and then unreacted vinyl acetate is expelled. From the viewpoint of uniform diffusion, it is preferable to add the polyene compound after dissolving it in the solvent used for the polymerization. Similarly, from the viewpoint of uniform diffusion, solution polymerization is more preferable than bulk polymerization.

The addition amount of the polyene compound is not particularly limited, but if it is shown as the amount of polyene charged to the vinyl acetate charged, it is about 0.0001 to 3% by weight,
The amount is preferably 0.0005 to 1% by weight, more preferably 0.001 to 0.5% by weight.

As a method for expelling unreacted vinyl acetate from the ethylene-vinyl acetate copolymer obtained by adding a polyene compound and removing ethylene by evaporation, for example, the copolymer solution is fixed from the upper part of a column filled with Raschig rings. Continuously supplying at a rate, blowing an organic solvent vapor such as methanol from the lower part of the column to let out a mixed vapor of an organic solvent such as methanol and unreacted vinyl acetate from the top of the column, and removing unreacted vinyl acetate from the bottom of the column. A method of taking out the copolymer solution is adopted.

An alkali catalyst is added to the copolymer solution from which unreacted vinyl acetate has been removed to saponify the acetic acid ester component in the copolymer. The saponification method may be either continuous or batch. As the alkali catalyst, sodium hydroxide, potassium hydroxide, alkali metal alcoholate or the like is used. For example, the saponification conditions for the batch system are as follows. Concentration of the copolymer solution: 10 to 50% Reaction temperature: 30 to 60 ° C. Amount of catalyst used: 0.02 to 0.6 equivalent (per acetic ester group) Time: 1 to 6 hours Saponification degree after saponification reaction Varies depending on the purpose, but is usually 95% or more of the vinyl acetate component, and can be arbitrarily adjusted depending on the saponification conditions.

The saponified product of the copolymer after the reaction contains an alkali catalyst, by-product salts and other impurities, and therefore these are removed by washing, for example, washing with water. The polyene compound can also be removed by washing such as washing with water, but the ease of removal varies depending on the polarity of the polyene compound, and a certain amount remains in the saponified product. The saponified product of the copolymer obtained in this manner contains phosphoric acid, pyrophosphoric acid, phosphorous acid, oxalic acid, succinic acid, adipic acid, tartaric acid, citric acid, sodium dihydrogen phosphate, potassium dihydrogen phosphate, acetic acid, etc. It is also possible to add partial salts of acids or polybasic acids. Finally, it is dried to obtain the desired saponified ethylene-vinyl acetate copolymer.

The washed and dried saponified product preferably contains 0.000001 to 1% by weight of a polyene compound. By containing such an amount of polyene compound,
It is possible to obtain a molded product which is less colored and has less gel-like particles during molding. Preferably 0.00001-
The content is 0.5% by weight, and 0.0001 to 0.2% by weight is more preferable.

The preferred melt index (M) of the saponified ethylene-vinyl acetate copolymer used in the present invention is
I) (190 ° C, measured under a load of 2160 g; provided that the melting point is near 190 ° C or higher than 190 ° C is 21)
Measured at a plurality of temperatures above the melting point under a load of 60 g, and plotted on a semilogarithmic graph with the reciprocal of absolute temperature as the horizontal axis and the melt index as the vertical axis (logarithm), and the value extrapolated to 190 ° C.) ~ 200 g / 10 min. , Optimally 0.
2 to 100 g / 10 min. Is.

A saponified product of the ethylene-vinyl acetate copolymer thus obtained, for example, a polyene compound of 0.0000 is added.
The saponified ethylene-vinyl acetate copolymer composition containing 0 to 1% by weight is molded into various molded products such as films, sheets, containers, pipes and fibers by melt molding. These molded products can be crushed and molded again for the purpose of reuse. It is also possible to uniaxially or biaxially stretch a film, sheet, fiber or the like. As the melt molding method, extrusion molding, inflation extrusion, blow molding, melt spinning, injection molding and the like are possible. The melting temperature varies depending on the melting point of the copolymer and the like, but is preferably about 150 to 270 ° C. It is also possible to blend two or more kinds of saponified copolymers having different polymerization degrees, ethylene contents and saponification degrees, and melt-mold them. Further, other various plasticizers, stabilizers, surfactants, cross-linking agents, metal salts to the saponified copolymer,
It is also possible to add an appropriate amount of a filler, a reinforcing agent for various fibers and the like. By such a method, a molded product with less coloring and less gelled spots can be obtained.

It is also possible to add an appropriate amount of a thermoplastic resin other than the saponified product of the copolymer. As the thermoplastic resin, various polyolefins (polyethylene, polypropylene, poly 1-butene, poly 4-methyl-1-pentene, ethylene-propylene copolymer, copolymers of ethylene and α-olefin having 4 or more carbon atoms, polyolefin And maleic anhydride copolymers, ethylene-vinyl acetate copolymers, ethylene-acrylic acid ester copolymers, modified polyolefins obtained by graft-modifying these with unsaturated carboxylic acids or their derivatives, and various nylons (nylon). 6, nylon 66, nylon 6/66 copolymer, etc.), polyvinyl chloride, polyvinylidene chloride, polyester, polystyrene, polyacrylonitrile, polyurethane, polyacetal, and modified polyvinyl alcohol resin. Further, the saponified product of the ethylene-vinyl acetate copolymer obtained according to the present invention may be laminated with the above-mentioned thermoplastic resin, particularly coextruded to be used as a multilayer structure. It is also possible to coextrusion coat or solution coat the saponified ethylene-vinyl acetate copolymer composition on a base film such as paper, plastic film and metal foil.

[0037]

EXAMPLES The present invention will be specifically described below with reference to examples. In addition, (part) and (%) are expressed on a weight basis unless otherwise specified. Further, in the following examples, the amount of the polyene compound remaining in the saponified copolymer, the coloration of the film, and the method for measuring gel-like spots in the film were measured by the following procedures.

The amount of polyene compound remaining in the saponified product of the copolymer was determined by the following procedure. The saponified product of the ethylene-vinyl acetate copolymer was pulverized, and coarse particles were removed by a 100-mesh sieve to obtain 10 g of the product, which was subjected to Soxhlet extraction with 100 mL of chloroform for 48 hours. The amount of polyene compound in this extract was quantified by high performance liquid chromatography by preparing a calibration curve using each polyene compound preparation.

In Examples 1 to 7 and Comparative Examples 1 to 5, the coloration of the film was measured by dissolving the sample film in dimethyl sulfoxide at a concentration of 50 g / L and measuring the absorbance at a wavelength of 360 nm. Based on this absorbance value, the coloration of the film was judged in the following three stages. Coloring degree 1;
Almost not recognized (absorbance less than 0.10), coloring degree 2; slightly colored (absorbance 0.10 or more, less than 0.25),
Coloring degree 3: Remarkably colored (absorbance of 0.25 or more). Also,
In Examples 8 to 13 and Comparative Examples 6 to 11, the absorbance values similarly measured were evaluated.

In Examples 1 to 7 and Comparative Examples 1 to 5, the gel-like particles in the film were observed with a polarizing stereomicroscope at a magnification of 10 times in a range of 10 cm × 10 cm to obtain 100 μm.
It was measured by counting gel-like particles having a size of m or more. In addition, in Examples 8 to 13 and Comparative Examples 6 to 11, the measurement was performed by counting gel-like particles having a size of 20 μm or more by the same measurement method.

Example 1 Vinyl acetate 1960 was placed in a polymerization tank having a pressure resistance of 100 kg / cm ^2.
0 part, 2180 parts of methanol, and 7.5 parts of AIBN (azobisisobutyronitrile) were charged, and after nitrogen replacement with stirring, the temperature was raised and the internal pressure was raised to 60 ° C. and the ethylene pressure was 35.
It was adjusted to 5 kg / cm ² . After maintaining the temperature and pressure for 3.5 hours to polymerize, β-myrcene 6.2 parts {0.0
316 wt% / VAc (vinyl acetate)} was dissolved in methanol to prepare a 1% solution, which was added. The polymerization rate at this time was 47% based on the charged vinyl acetate, and the ethylene content rate was 33 mol%.

After the addition of the polyene compound, the polymerization tank was returned to normal pressure, and ethylene was removed by evaporation. Subsequently, this methanol solution was continuously flown down from the upper part of the expulsion column filled with Raschig rings, while methanol vapor was blown from the bottom part of the column to discharge unreacted vinyl acetate monomer from the column top part with methanol vapor and pass through the condenser. By removing, a 45% methanol solution of an unreacted vinyl acetate 0.01% or less ethylene-vinyl acetate copolymer was obtained.

Next, a methanol solution of ethylene-vinyl acetate copolymer was charged into a saponification reactor, and caustic soda / methanol solution (80 g / L) was added to the vinyl acetate component in the copolymer at 0.4 equivalent. Then, methanol was added to adjust the copolymer concentration to 20%. The temperature was raised to 60 ° C. and the reaction was carried out for about 4 hours while blowing nitrogen gas into the reactor. After 4 hours, it was neutralized with acetic acid to stop the reaction, and the contents were taken out of the reactor and allowed to stand at room temperature for about 20 hours to be precipitated in a particulate form. The precipitated particles were deliquored with a centrifuge, and then a large amount of water was added to deliquorate.

Finally, the saponification product of the ethylene-vinyl acetate copolymer obtained by deliquoring and drying has a saponification degree of 99.5 mol% and a melt index (190 ° C., under a load of 2160 g) of 2 g / 10 min. Met. The amount of β-myrcene remaining in the saponified product of the copolymer was 0.05% by weight. The saponified product of this copolymer was prepared by setting the temperature of the cylinder, the adapter and the die at 230 ° C. 60
mm thickness extruder / T die single layer film forming machine
A film of μm was obtained.

The degree of coloring of the obtained film was 1, and a film having a good color tone could be obtained. The number of gel-like particles of 100 μm or more in the film is 100 cm ²
It was 5 per. The measurement results of the properties of the above resins and films are summarized in Table 1 together with the boiling point of β-myrcene.

Examples 2 to 6 Instead of the β-myrcene of Example 1, an equimolar amount of α-
Farnesene 9.3 parts (0.0474 wt% / VAc,
Example 2), 5.1 parts of sorbic acid (0.0260% by weight)
/ VAc, Example 3), 12.7 parts of eleostearic acid (0.0645% by weight / VAc, Example 4), 16.6 parts of tung oil in a 1/3 molar amount (0.0845% by weight / VAc,
Example 5) and 3.1 parts of equimolar isoprene (0.
Example 1 using 0158 wt% / VAc, Example 6)
A saponified product of ethylene-vinyl acetate copolymer was produced by the same method. Here, the amount of tung oil added in Example 5 was 1/3 the molar amount of the other polyene compounds, considering that three molecules of triene were contained in one molecule of tung oil.

Using the saponified product of the copolymer thus obtained, a film was prepared and evaluated in the same manner as in Example 1. The evaluation results are shown in Table 1. The amount of tung oil remaining in Example 5 is the amount of eleostearic acid produced by hydrolysis in the saponification step. The residual amount of isoprene of Example 6 was not detected, probably because it was evaporated during Soxhlet extraction with a chloroform solvent.
It was impossible to measure.

Example 7 The particles of saponified ethylene-vinyl acetate copolymer obtained by deliquoring and drying in Example 1 were treated with an aqueous solution of acetic acid and sodium dihydrogen phosphate, and deliquored and dried. Saponification degree 99.5 mol%, melt index 2.1 g / 1
0 min. To obtain a saponified ethylene-vinyl acetate copolymer. When the components in the saponified ethylene-vinyl acetate copolymer were analyzed, the following results were obtained. Acetic acid 0.05% Sodium acetate 0.0075% Sodium dihydrogen phosphate 0.01% β-Myrcene 0.05% Using the saponified copolymer thus obtained, a film was prepared in the same manner as in Example 1 and evaluated. did. The evaluation results are shown in Table 1.
Shown in.

Comparative Examples 1 to 4 4.7 parts of styrene (0.0241% by weight / VAc, Comparative Example 1) in an equimolar amount in place of β-myrcene of Example 1 and 2,4-diphenyl-4. -Methyl-1-pentene (hereinafter sometimes abbreviated as DPMP) 10.7 parts (0.
0548 wt% / VAc, Comparative Example 2), tiglic acid 4.
6 parts (0.0232 wt% / VAc, Comparative Example 3) and 1,3-butadiene 2.5 parts (0.0125 wt% / V).
A saponified ethylene-vinyl acetate copolymer was produced in the same manner as in Example 1 using Ac and Comparative Example 4).

A film was prepared and evaluated in the same manner as in Example 1 using the saponified product of the copolymer thus obtained.
The evaluation results are shown in Table 1. In addition, 1,3-of Comparative Example 4
As with Example 6, the residual amount of butadiene could not be measured.

Comparative Example 5 A saponified ethylene-vinyl acetate copolymer was produced in the same manner as in Example 1 without adding any additive in place of β-myrcene. Using the saponified product of the copolymer thus obtained, a film was prepared and evaluated in the same manner as in Example 1. The evaluation results are shown in Table 1.

[0052]

[Table 1]

Example 8 Using a polymerization tank having a cooling coil inside and equipped with a 4-blade paddle type stirrer and a capacity of 100 L, continuous polymerization was carried out to produce an ethylene-vinyl acetate copolymer. The polymerization conditions are as follows. Vinyl acetate supply amount: 5.0 kg / hr 2,2′-azobis- (2,4-dimethylvaleronitrile) supply amount: 2.8 g / L as a methanol solution of 0.
3 L / hr Polymerization temperature; 60 ° C. Polymerization tank ethylene pressure; 45 kg / cm ² Average residence time; 7 hours

As a result, the polymerization rate of vinyl acetate was about 55%.
The polymerization liquid of was discharged from the polymerization tank at 7 kg / hr and had the following composition. Ethylene-vinyl acetate copolymer (ethylene content 34 mol%); 46 wt% vinyl acetate; 32 wt% ethylene; 8.7 wt% methanol; 10 wt%

Immediately after the polymerization reaction liquid was discharged from the polymerization tank, 0.20 of a 1.0 g / L methyl acetate solution of β-myrcene was used.
L / hr was added and introduced into the post-mixing tower, and methanol vapor was blown from the bottom of the tower at 3.5 kg / hr to separate unreacted vinyl acetate and ethylene from the top, and ethylene-vinyl acetate mixed from the bottom. A 45 wt% polymer solution in methanol was obtained at 7.2 kg / hr.

With respect to 100 parts by weight of the above copolymer solution,
Add a methanol solution containing 1 part by weight of caustic soda to 110
° C., 3.5 kg / cm ² below, while blowing a methanol vapor was 30 minutes saponification reaction, methyl acetate formed during the reaction was removed out of the system by distilling with some methanol. Water-methanol vapor was further blown into the obtained saponification solution to distill the methanol-water mixed vapor, and the saponification solution (methanol / water of a methanol-water mixed system having a saponified copolymer concentration of 35% by weight). = 65/35 weight ratio). This solution was discharged into a water / methanol mixture (10% by weight of methanol) at 5 ° C. from a die having a hole with a diameter of 2 mm to coagulate it in a strand form. 2.5-3.5mm by cutting this strand-like material with a cutter
After making a pellet having a length of, the pellet was washed with 15 parts by weight of process water per 1 part by weight of the pellet, and then deliquored and dried.

The particles of saponified ethylene-vinyl acetate copolymer obtained by deliquoring and drying were treated with an aqueous solution of acetic acid and sodium dihydrogen phosphate in the same manner as in Example 7, and deliquoring and drying to saponify. 99.4 mol%, melt index 2.0 g / 10 min. To obtain a saponified ethylene-vinyl acetate copolymer. When the components in the saponified ethylene-vinyl acetate copolymer were analyzed, the following results were obtained.
In addition, the contents of acetic acid, sodium acetate, and sodium dihydrogen phosphate are described in Examples 9 to 13 and Comparative Examples 6 to
The value of 11 was also the same. Acetic acid 0.05% Sodium acetate 0.0075% Sodium dihydrogen phosphate 0.01% β-Myrcene 0.05%

Using the saponified product of the copolymer thus obtained, the same film as in Example 1 was prepared and evaluated. The absorbance of the obtained film was 0.09, and a film having a good color tone could be obtained. In addition, 20μ in the film
The number of gel-like particles of m or more was 5 per 100 cm ² .

Examples 9 to 13 and Comparative Examples 6 to 11 Ethylene-vinyl acetate was the same as Example 8 except that the type and amount of the polymerization catalyst and polyene compound were changed as follows. The saponified copolymer was produced in a continuous polymerization process. Here, the addition amount of each catalyst was adjusted so that a polymer solution having the same degree of polymerization, degree of polymerization, and ethylene content as in the case of polymerization with the AMV catalyst of Example 8 was obtained. Specifically, AMV {2
2'-azobis- (2,4-dimethylvaleronitrile)
Is 1.3 g / L, AIBN (2,2′-azobisisobutyronitrile) is 1.9 g / L, and NPP (di-n-propylperoxydicarbonate) is 0.5 g / L in a methanol solution. In both cases, the amount added was 0.7 L / hr. In addition, β-myrcene was used as a 2.0 g / L methyl acetate solution, and sorbic acid was used as a 1.7 g / L methanol solution as 2,4-diphenyl-4-methyl-1-.
Pentene was added as a 3.5 g / L methanol solution at a feed rate of 0.1 L / hr, and β- in Example 8 was added.
The number of moles added was the same as that of myrcene. Also,
When the additive after polymerization was not added, only methanol was added at a supply amount of 0.1 L / hr.

The catalyst used in each example and the polyene compound added were as follows. Example 9 AMV, sorbic acid Comparative Example 6 AMV, DPMP Comparative Example 7 AMV, no additive Example 10 AIBN, β-myrcene Example 11 AIBN, sorbic acid Comparative Example 8 AIBN, DPMP Comparative Example 9 AIBN, no additive Example 12 NPP, β-myrcene Example 13 NPP, sorbic acid Comparative Example 10 NPP, DPMP Comparative Example 11 NPP, no additive A film of the obtained saponified ethylene-vinyl acetate copolymer was prepared in the same manner as in Example 1. It was created and the evaluation results are shown in Table 2.

[0061]

[Table 2]

[0062]

EFFECTS OF THE INVENTION After polymerizing a vinyl acetate polymer, particularly an ethylene-vinyl acetate copolymer, a conjugated polyene compound having a boiling point of 20 ° C. or higher is added, and the polymer is saponified to form a resin obtained. Thus, it is possible to obtain a molded product made of a saponified product of a high-quality vinyl acetate polymer, particularly a saponified product of an ethylene-vinyl acetate copolymer, which is less colored and causes less gel-like spots during molding.

Continuation of front page (51) Int.Cl. ⁷ Identification code FI C08L 29/04 C08L 29/04 31/04 31/04 (72) Inventor Yukihiro Ohara 1-2-1 Kaigandori, Okayama-shi, Okayama Stock Company Kuraray (72) Inventor Nao Nakagawa 1-1239 Umeda, Kita-ku, Osaka-shi, Osaka Kuraray Co., Ltd. (72) Inventor Toshinori Tsugaru 1-23-139 Umeda, Kita-ku, Osaka-shi, Osaka Kuraray Co., Ltd. (56) References JP-A-55-38864 (JP, A) JP-A-59-226003 (JP, A) JP-A-61-197603 (JP, A) JP-B-45-12147 (JP, B1) (58) Fields surveyed (Int.Cl. ⁷ , DB name) C08F 6/00 C08F 8/12 C08F 263/04 C08K 5/01 C08L 23/08 C08L 29/04 C08L 31/04

Claims (6)

(57) [Claims] 1. A method for producing a vinyl acetate polymer, which comprises adding a conjugated polyene compound having a boiling point of 20 ° C. or higher after polymerizing one or more kinds of monomers containing vinyl acetate. 2. The method for producing a vinyl acetate polymer according to claim 1, wherein the vinyl acetate polymer is an ethylene-vinyl acetate copolymer. 3. The method for producing a vinyl acetate polymer according to claim 1, wherein the conjugated polyene compound has a boiling point higher than that of vinyl acetate. 4. The method for producing a vinyl acetate polymer according to claim 1, wherein the conjugated polyene compound is added after polymerizing using a polymerization catalyst having a half-life of 5 hours or less in methanol at 60 ° C. . 5. A method for producing a saponified product of a vinyl acetate-based polymer, which comprises saponifying the vinyl acetate-based polymer produced by the method according to any one of claims 1 to 4. 6. A saponified vinyl acetate polymer having a boiling point of 2
The conjugated polyene compound having a temperature of 0 ° C. or higher is 0.000001-1
A resin composition containing wt%.