JPH05331211A - Agent for preventing adhesion of polymer scale, polymerizer prevented from adhesion of polymer scale and production of polymer using the same - Google Patents

Abstract

PURPOSE:To provide an agent comprising the condensation product of an aliphatic diamine compound with a naphthoquinone compound in an aqueous medium and preventing the adhesion of scales to the surface of a gas-liquid interface in the polymerization of an ethylenic double bond-containing monomer to give products free from fish eyes. CONSTITUTION:The agent contains the condensation product of (A) an aliphatic diamine compound with (B) a naphthoquinone compound in an aqueous medium. The agent is coated on the inner wall of a polymerizer and subsequently dried to produce a coating film. The component A is preferably 1,3-diamino-2- hydroxypropane, etc., and the component B is preferably 6-methyl-1,4- naphthoquinone, plumbagin, etc. The condensation product is obtained by reacting both the components at room temperature to 50 deg.C or 0.5-100hr. The component B is used in an amount of 0.1-3 pts.wt. per pt.wt. of the component A.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a scale adhesion preventive agent for polymerizing a monomer having an ethylenic double bond, a polymerization vessel and a method for producing a polymer using the same.

[0002]

2. Description of the Related Art Conventionally, as a method for polymerizing a vinyl monomer, a suspension polymerization method, an emulsion polymerization method, a solution polymerization method, a gas phase polymerization method,
Alternatively, a bulk polymerization method or the like is known. In any of these polymerization methods, adhesion of the polymer scale is likely to occur on the inner wall of the polymerization vessel, the stirrer section or the like where the monomer comes into contact.

When the polymer scale adheres, the yield of the polymer, the cooling capacity of the polymerization vessel and the like decrease, and the scale is peeled off and mixed in the product, which brings about a disadvantage that the quality of the product is deteriorated. In addition, not only excessive labor and time are required to remove the adhered polymer scale,
Since unreacted monomer is contained in this scale,
There is a risk of human injury due to monomers (vinyl chloride, etc.), which has become a very serious problem in recent years.

As for the prevention of adhesion of polymer scale to the inner wall of a polymerization vessel, polarities of amine compounds, quinone compounds, aldehyde compounds, etc. have been heretofore used, for example, in some cases in suspension polymerization of vinyl chloride. A method of applying an organic compound or a method of adding such a compound to an aqueous medium is known (Japanese Patent Publication No. 30343/1985). However, these methods show a scale-preventing effect when repeating polymerization up to about 5 to 6 batches, but have a disadvantage that the preventive effect disappears when the number of polymerization batches is larger than that (inferior in sustainability). .. In this respect, the use of a water-soluble catalyst has a particularly remarkable effect and is not industrially satisfactory.

In order to overcome this disadvantage, JP-A-53-13689
In the publication, a condensation product of an aromatic amine compound is proposed. When a coating film of the condensation product of this aromatic amine compound is formed on the inner wall of the polymerization vessel where the monomer contacts, even if the polymerization is repeated for 100 to 200 batches, the scale to the liquid phase portion in the polymerization vessel No adhesion occurs. Further, even when a water-soluble catalyst is used, the scale adhesion in the liquid phase part is similarly prevented.

[0006]

However, there is a drawback that scale adheres to the vicinity of the interface between the gas phase portion and the liquid phase portion located in the upper layer portion in the polymerization vessel. Once the scale adheres to the vicinity of the interface between the gas phase part and the liquid phase part, the scale that adheres gradually grows as the polymerization is repeated, and eventually it may peel off and enter the product polymer. .. Then, when the scale is mixed in the product polymer in this way, when the product polymer is processed into a molded article such as a sheet, many fish eyes are generated in the molded article, and the quality of the molded article is significantly deteriorated. Will end up.

The coloring that occurs when the polymer is processed into a molded article is called initial coloring, and the smaller the value, the better. However, the coating film composed of the condensation product of the aromatic amine compound may be peeled off or dissolved and mixed into the product polymer, so that the initial colorability is deteriorated. Further, when forming a coating film of the condensation product of the aromatic amine compound, the condensation product is used as a coating solution dissolved in an organic solvent or a mixture of water containing an organic solvent as a main component, There is a risk of ignition and explosion of the organic solvent, and there is a problem in handling safety such as toxicity.

Therefore, an object of the present invention is to effectively prevent the polymer scale from adhering not only in the liquid phase part in the polymerization vessel but also in the vicinity of the interface between the gas phase part and the liquid phase part, and to prevent the fish after molding from occurring. It is possible to produce a product polymer with very few eyes and good initial colorability. Furthermore, there is little risk of ignition and explosion of the organic solvent when forming a coating film, and it is safe to handle. It is an object of the present invention to provide a scale adhesion preventing agent, a polymerization vessel using the prevention agent, and a method for producing a polymer.

[0009]

[Means for Solving the Problems] That is, the present invention, in order to achieve the above object, is a condensation product obtained by condensing (A) an aliphatic diamine compound and (B) a naphthoquinone compound in an aqueous medium. There is provided a polymer scale anti-adhesion agent for polymerizing a monomer having an ethylenic double bond, which comprises a substance.

The present invention also provides a polymerization vessel having a coating film containing a condensation product obtained by condensing the above (A) and (B) in an aqueous medium. Furthermore, it is a method for producing a polymer by polymerization of a monomer having an ethylenic double bond in a polymerization vessel, which has a step of performing the polymerization in a polymerization vessel having the above coating film on the inner wall surface. A method for producing a polymer is provided.

The condensation product, which is an essential component of the polymer scale inhibitor of the present invention, is a substance obtained by condensing (A) an aliphatic diamine compound and (B) a naphthoquinone compound in an aqueous medium. is there. The raw materials and the synthesis will be described below.

(A) Aliphatic Diamine Compound The aliphatic diamine compound (A) is, for example, diaminoalkanes, diaminocycloalkanes, diaminodialkylamines, diaminodialkylsulfides, piperazine and the like.

Diaminoalkanes have 2 to 12 carbon atoms.
Are preferred, for example 1,2-diaminoethane,
1,2-diaminopropane, 1,3-diaminopropane, 1,
4-diaminobutane, 1,7-diaminoheptane, 1,6-
Examples thereof include diaminohexane, 1,8-diaminooctane, 9,10-diaminononane, 1,10-diaminodecane, 1,12-diaminododecane, and 1,2-diamino-2-methylpropane. Further, compounds obtained by substituting the hydrogen atom of these diaminoalkanes with a substituent such as a hydroxyl group, for example, 1,3-diamino-2-hydroxypropane and the like can be mentioned.

The diaminocycloalkanes preferably have 3 to 8 carbon atoms, and examples thereof include 1,4-diaminocyclohexane and bis (4-aminocyclohexyl) methane. Further, compounds obtained by substituting the hydrogen atom of these diaminocycloalkanes with a substituent such as a hydroxyl group, for example, 1,4-diamino-2-hydroxycyclohexane and the like can be mentioned.

Diaminodialkylamines are, for example,
Bis (3-aminopropyl) amine, bis (3-aminopropyl) methylamine, bis (5-aminoheptyl)
Examples include methylamine and the like.

Examples of the diaminodialkyl sulfides include bis (3-aminopropyl) sulfide and bis (5-aminoheptyl) sulfide.

Among the above aliphatic diamine compounds, preferred are 1,2-diaminoethane, 1,3-diaminopropane, 1,3-diamino-2-hydroxypropane, 1,4
-Diaminocyclohexane, bis (3-aminopropyl) amine, bis (3-aminopropyl) sulfide and piperazine. In the present invention, the above-mentioned aliphatic diamine compounds can be used alone or as a mixture of two or more kinds.

(B) Naphthoquinone Compound The naphthoquinone compound (B) has the following general formula:
It is a compound represented by (1) to (2).

[Chemical 1]

[Chemical 2]

[Here, R ¹ is --H, --NH ₂ , --Cl,-
_{OH, -NO 2, -COCH 3,} - OCH 3, represents a -N (CH _{3) 2} or an alkyl group having 1 to 3 carbon atoms, R ² is, -H, -
NH ₂ , -OH, -CH ₃ , -COOH, -SO ₃ H, R
_{^3, -H, -OH, -CH 3,} -Cl, -COCH 3, - OC
H _3, -COOH, represents a -SO ₃ H. Specific examples thereof include 6-methyl-1,4-naphthoquinone, 2-methyl-1,4-naphthoquinone, lawson, juglone, plumbagin, α-naphthoquinone and β-naphthoquinone. In the present invention, the above naphthoquinone compounds may be used alone or as a mixture of two or more kinds.

Condensation Product The condensation of the aliphatic diamine compound (A) and the naphthoquinone compound (B) described above is usually carried out in an aqueous medium at room temperature to 100 ° C.
0.1 to 300 hours, preferably 0.5 to 100 at room temperature to 50 ° C
It is carried out by reacting for a time.

An aqueous medium is used as a medium for the condensation reaction. Here, the aqueous medium means a mixed solvent of water and an organic solvent containing 30% by weight or less of water and an organic solvent miscible with water. When a mixed solvent of water and an organic solvent miscible with water is used, the content ratio of the organic solvent is 30% by weight or less, preferably 20% by weight or less. Examples of the organic solvent miscible with water include alcohols such as methanol, ethanol and propanol; ketones such as acetone and methyl ethyl ketone; esters such as methyl acetate and ethyl acetate.

The pH of the aqueous medium is preferably 7.5 to 13.5, more preferably 9.0 to 13.0. Since the aliphatic diamine compound (A) often exhibits alkalinity, it may not be necessary to adjust the pH. Examples of the alkaline compound used when adjusting the pH include LiOH, NaOH, KOH, Na ₂ CO ₃ , and Na ₂ S.
Examples thereof include alkali metal compounds such as iO ₃ , Na ₂ HPO ₄ , and NH ₄ OH, or ammonium compounds.

The condensation product is affected by the types of aliphatic diamine compound and naphthoquinone compound, composition ratio and reaction temperature, and reaction time. In the present invention, the naphthoquinone compound is used per 1 part by weight of the aliphatic diamine compound (A). (B) 0.01
The amount is preferably -10 parts by weight, more preferably 0.1-3 parts by weight. If the amount of the naphthoquinone compound (B) is too much or too little, the effect of preventing scale adhesion of the obtained condensation product will be reduced.

Preparation of coating liquid For the coating liquid containing the condensation product produced by the above condensation reaction, for example, the condensation product containing solution obtained by performing the above condensation reaction may be used as it is or in an aqueous medium such as water. The diluted one may be used.

Examples of the aqueous solvent used for preparing the coating liquid include water or a mixed solvent of water and an organic solvent miscible with water. Examples of the organic solvent miscible with water include alcohols such as methanol, ethanol and propanol; ketones such as acetone and methyl ethyl ketone; esters such as methyl acetate and ethyl acetate. When a mixed solvent of water and an organic solvent miscible with water is used, the content ratio of the organic solvent should be such that there is no danger of ignition, explosion, etc., and there is no safety problem in handling such as toxicity. Well, specifically, it is preferably 50% by weight or less, and further preferably 30% by weight or less.
If the amount of the organic solvent is too large, there is a risk of ignition and explosion when forming the coating film as described above, and there is also a problem in handling safety such as toxicity.

The concentration of the condensation product of the components (A) and (B) in the coating solution is not particularly limited as long as the total coating amount described below can be obtained, but it is usually about 0.005 to 10% by weight, preferably
It is 0.01 to 5% by weight.

Further, for example, cationic, nonionic and anionic surfactants can be added to the coating solution as long as the scale preventing effect is not impaired. Water-soluble polymer compounds such as polymer compounds, anionic polymer compounds and amphoteric polymer compounds can be added.

Examples of the cationic polymer compound include polyvinylamine, polyethyleneamine, polyethyleneimine, polyacrylamide, N-vinyl-2-pyrrolidone-acrylamide copolymer, cyclized polymer of dimethyldiamylammonium chloride, and dimethyl. Cyclic polymer of diethylammonium bromide, cyclized polymer of diallylamine hydrochloride, cyclized copolymer of dimethyldiallylammonium chloride and sulfur dioxide, polyvinylpyridine, polyvinylpyrrolidone, polyvinylcarbazole, polyvinylimidazoline, polydimethylaminoethyl acrylate , Polydimethylaminoethylmethacrylate, polydiethylaminoethylacrylate, polydiethylaminoethylmethacrylate, etc. have a nitrogen atom in the side chain and Atoms cationic polyelectrolyte bearing a charged positively, and the like.

Examples of the amphoteric polymer compound include amphoteric polymer compounds such as glue, gelatin, casein and albumin. As the anionic polymer compound,
For example, sulfomethylated polyacrylamide; polyacrylic acid; alginic acid, acrylamide-vinyl sulfonic acid copolymer, polymethacrylic acid, polystyrene sulfonic acid, or the like, or alkali metal salts or ammonium salts thereof; for side chains such as carboxymethyl cellulose. Examples thereof include anionic polymer compounds having a carboxyl group or a sulfonic acid group.

Further, an inorganic compound may be appropriately added to the coating solution, if necessary, as long as the function of preventing scale is not impaired. Examples of inorganic compounds that can be added include orthosilicic acid, metasilicic acid, mesodisilicate, mesotrisilicic acid, mesotetrasilicic acid, sodium metasilicate, sodium orthosilicate, sodium disilicate, sodium tetrasilicate, and water glass. Silicic acids or silicates; oxyacid salts of metals selected from alkaline earth metals such as magnesium, calcium and barium, zinc group metals such as zinc, aluminum group metals such as aluminum, and platinum group metals such as platinum, acetic acid Examples thereof include metal salts such as salts, nitrates, hydroxides and halides; inorganic colloids such as ferric hydroxide colloid, silicic acid colloid, barium sulfate colloid and aluminum hydroxide colloid. The above-mentioned inorganic colloid may be prepared by, for example, mechanical grinding, irradiation with ultrasonic waves, electrical dispersion and chemical method.

Formation of coating film To form a coating film on the inner wall surface of the polymerization vessel using the coating solution prepared as described above, first, the coating solution is applied to the inner wall surface of the polymerization vessel, and then, for example, at room temperature. After thoroughly drying in the temperature range from 1 to 100 ° C, further wash with water if necessary.

Further, it is preferable that the coating solution is applied not only to the inner wall surface of the polymerization vessel, but also to other portions with which the monomer contacts during the polymerization. For example, stirring blade, stirring shaft, baffle,
Examples include capacitors, headers, search coils, bolts and nuts. More preferably, the coating liquid is a site other than the site where the monomer comes into contact during the polymerization, but a site where the polymer scale may be attached, for example, the inner surface of the device and piping of the recovery system of the unreacted monomer. For example, it is better to form the coating film. Specifically, a monomer distillation column, a condenser,
The inner surface of the monomer storage tank, valve, etc. may be mentioned.

In this way, when a coating film is formed on the site where the monomer contacts during the polymerization and the site where the other polymer scale may adhere, the adhesion of the polymer scale to those sites. Is prevented. The method of applying the coating liquid to the inner wall surface of the polymerization vessel is not particularly limited, and examples thereof include brush coating, spray coating, a method of withdrawing after filling the polymerization vessel with the coating solution, and others.
No. 55-36288, Special Publication No. 56-501116, No. 56-50
The automatic coating method described in 1117, JP-A-59-11303, etc. can also be used.

There is no limitation on the method of drying the wet surface due to the application of the coating liquid, and the following method can be used, for example. That is, after applying the coating solution, a method of applying an appropriately heated warm air to the coating surface, or the inner wall surface of the polymerization vessel and the other surface to be coated with the coating solution are heated to, for example, 30 to 80 ° C. in advance. The method of directly applying the coating solution to the heated surface can be used. After drying the coated surface, the coated surface is washed with water as needed.

The coating film thus obtained has a total coating amount after drying of usually 0.001 g / m ² or more, particularly 0.05 to ²
It is preferably g / m ² . The coating operation described above does not necessarily need to be performed for each batch of polymerization, because the formed coating film has high durability and the polymer scale adhesion preventing action continues. Therefore, the productivity of the product polymer is improved.

Polymerization As described above, a coating film is formed by applying a coating treatment to the inner wall of the polymerization vessel, and preferably to the other portions where the monomers come into contact during the polymerization. Polymerize. That is, in addition to a monomer having an ethylenic double bond and a polymerization initiator (catalyst), if necessary, a polymerization medium such as water, and a suspending agent, a solid dispersant, a nonionic or anionic emulsifier, etc. A dispersant and the like are charged, and then polymerization is performed by a conventional method.

Examples of the monomer having an ethylenic double bond to be polymerized by applying the method of the present invention include vinyl halide such as vinyl chloride; vinyl ester such as vinyl acetate and vinyl propionate; acrylic acid. , Methacrylic acid, and their esters or salts; maleic acid, fumaric acid, and their esters or anhydrides; diene-based monomers such as butadiene, chloroprene, isoprene; styrene, acrylonitrile, vinylidene halide, vinyl ether, etc. Be done.

The type of polymerization to which the method of the present invention is applied is not particularly limited, and suspension polymerization, emulsion polymerization, solution polymerization,
It is effective in both bulk polymerization and vapor phase polymerization, and is particularly suitable for polymerization in an aqueous medium such as suspension polymerization and emulsion polymerization.

The general polymerization method will be specifically described below by taking suspension polymerization and emulsion polymerization as examples. First,
Water and a dispersant are charged into a polymerization vessel, and then a polymerization initiator is charged. Next, after exhausting the inside of the polymerization vessel to reduce the pressure to 0.1 to 760 mmHg, the monomer was charged (at this time, the internal pressure of the polymerization vessel was
Usually 0.5 to 30 kgf / cm ² · G), then 30 to 150
Polymerize at reaction temperature of ° C. During the polymerization, if necessary,
One or more of water, a dispersant and a polymerization initiator are added. Further, the reaction temperature at the time of polymerization varies depending on the kind of the monomer to be polymerized. For example, in the case of vinyl chloride polymerization,
Polymerization is carried out at 30-80 ° C, and in the case of styrene polymerization, 50-
Polymerize at 150 ° C. For polymerization, the internal pressure of the polymerization vessel is 0 to 7 kgf /
When the temperature falls to cm ² · G, or when there is almost no difference between the inlet temperature and the outlet temperature of the cooling water that flows in and out of the jacket mounted on the outer periphery of the polymerization vessel (that is, when the heat generated by the polymerization reaction disappears). ), It is judged that it is completed. Water, a dispersant, and a polymerization initiator charged during polymerization are usually 20 to 500 parts by weight of water, 0.01 to 30 parts by weight of a dispersant, and 0.01 to 5 parts by weight of a polymerization initiator with respect to 100 parts by weight of a monomer. It is a department.

In the case of solution polymerization, an organic solvent such as toluene, xylene or pyridine is used as a polymerization medium instead of water. A dispersant is used as needed. Other polymerization conditions are generally the same as those for suspension polymerization and emulsion polymerization. Further, in the case of bulk polymerization, after evacuating the inside of the polymerization vessel to a pressure of about 0.01 to 760 mmHg, charging a monomer and a polymerization initiator into the polymerization vessel,
Polymerize at a reaction temperature of -10 to 250 ° C. For example, it is carried out at 30 to 80 ° C. in the case of vinyl chloride polymerization and at 50 to 150 ° C. in the case of styrene polymerization.

When polymerization is carried out by applying the polymer scale adhesion preventing method of the present invention, adhesion of the polymer scale can be prevented regardless of the material of the inner wall surface of the polymerization vessel. The adhesion of polymer scale can be prevented even when the polymerization is carried out in a steel or other steel-made polymerization vessel, a glass-lined polymerization vessel, or the like.

What is added to the polymerization system can be used without any restrictions. That is, for example, t-butyl peroxy neodecanoate, bis (2-ethylhexyl) peroxydicarbonate, 3,5,5-trimethylhexanoyl peroxide, α-cumylperoxy neodecanoate, cumene hydroper Oxite, cyclohexanone peroxide, t-butyl peroxypivalate, bis (2-ethoxyethyl) peroxydicarbonate, benzoyl peroxide, lauroyl peroxide, 2,4-dichlorobenzoyl peroxide, diisopropyl peroxydicarbonate , Α,
Polymerization initiators such as α'-azobisisobutyronitrile, α, α'-azobis-2,4-dimethylvaleronitrile, potassium peroxodisulfate, ammonium peroxodisulfate and p-menthane hydroperoxide; partially saponified polyvinyl Suspending agents for alcohols, polyacrylic acid, copolymers of vinyl acetate and maleic anhydride, cellulose derivatives such as hydroxypropylmethyl cellulose, natural or synthetic polymer compounds such as gelatin; solid dispersants such as calcium phosphate and hydroxyapatite; Nonionic emulsifiers such as sorbitan monolaurate, sorbitan trioleate, and polyoxyethylene alkyl ether; sodium alkylbenzene sulfonates such as sodium lauryl sulfate and sodium dodecylbenzenesulfonate; sodium dioctylsulfosuccinate Anionic emulsifiers such as lithium; fillers such as calcium carbonate and titanium oxide; stabilizers such as tribasic lead sulfate, calcium stearate, dibutyltin dilaurate, dioctyltin mercaptide; lubricants such as rice wax, stearic acid and cetyl alcohol; D
OP: plasticizer such as DBP; mercaptans such as t-dodecyl mercaptan; chain transfer agent such as trichlorethylene; pH
Even in a polymerization system in which a regulator and the like are present, the method of the present invention can effectively prevent the adhesion of polymer scale.

The polymer scale adhesion preventive agent of the present invention may be used for forming a coating film on the inner wall surface of the polymerization vessel or the like, and may be further added directly to the polymerization system, whereby the scale prevention effect is improved. You can also let it. In that case, the addition amount of the polymer scale anti-adhesion agent is appropriately about 10 to 1000 ppm with respect to the total weight of the charged monomers. When adding, care should be taken not to affect the quality of the product polymer such as fish eye, bulk specific gravity and particle size distribution.

[0044]

EXAMPLES Production Example 1 Production of condensation product No. 1 In a pressure resistant reactor, 980 g of water and α as a naphthoquinone compound were used.
10 g of naphthoquinone was charged and stirred at room temperature to disperse α-naphthoquinone in water. Next, 10 g of 1,2-diaminoethane was added as an aliphatic diamine compound and the temperature was raised to 25 ° C. After reacting at 25 ° C. for 10 hours, it was cooled to obtain an aqueous solution of a condensation product. This solution was designated as condensation product No. 1.

Production of Condensation Products Nos. 2 to 11 Using the aliphatic diamine compound, naphthoquinone compound and solvent shown in Table 1 and the condensation products No. 1 at the reaction temperature and reaction time shown in the same table, The condensation reaction was performed in the same manner to obtain condensation products Nos. 2 to 11. However, Nos. 2 and 3 marked with * in Table 1 are condensation products that do not satisfy the conditions of the present invention, and No. 11 was obtained by condensation in an organic solvent instead of an aqueous medium. It is a condensation product.

[0046]

[Table 1]

Example 1 (Experiment Nos. 101 to 111) Polymerization was carried out as follows using a stainless steel polymerization vessel equipped with a stirrer and having an internal volume of 1000 liters. The condensation products and solvents used in each experiment are shown in Table 2. A solvent was added to the condensation product to prepare a coating solution so that the solvent ratio and concentration shown in Table 2 were obtained. These coating solutions were applied to the inner wall of the polymerization vessel, the stirring shaft, the stirring blades, and other parts where the monomers come into contact with each other during the polymerization, and were heated and dried at 40 ° C for 15 minutes to form a coating film, and then washed with water.

However, Nos. 102 and 103 marked with * in Table 2
Experiments 111 and 111 are comparative examples in which a coating solution that does not satisfy the conditions of the present invention is applied. After that, 400 kg of water and vinyl chloride were placed in the polymerization vessel where the coating film was formed by coating in this way.
200 kg, partially saponified polyvinyl alcohol 250 g, hydroxypropylmethyl cellulose 25 g and 3,5,5-trimethylhexanoyl peroxide 70 g were charged and polymerized at 66 ° C. for 6 hours while stirring. After the polymerization was completed, the produced polymer and unreacted monomer were recovered, and the inside of the polymerization vessel was washed with water to remove the residual resin.

Thereafter, the coating operation was not performed, and the above-mentioned polymerization and washing of the inner wall of the polymerization vessel were made into one batch, and the same operation was repeated for the number of batches shown in Table 2. After the final batch, the liquid phase part in the polymerization vessel was repeated. Then, the scale adhesion amount near the interface between the gas phase portion and the liquid phase portion was determined by the following method. The results are shown in Table 2. Moreover, the fish eye when the polymer obtained in each experiment was formed into a sheet was measured by the following method. The results are shown in Table 2. -Measurement of the amount of polymer scale attached The scale attached to a 10 cm square area at a predetermined location on the inner wall of the polymerization vessel was scraped off with a spatula and weighed with a balance. The measured value was multiplied by 100 to obtain the scale adhesion amount per 1 m ² .

Measurement of Fish Eye A mixture prepared by mixing 100 parts by weight of polymer, 50 parts by weight of DOP, 1 part by weight of dibutyltin dilaurate, 1 part by weight of cetyl alcohol, 0.25 part by weight of titanium oxide and 0.05 part by weight of carbon black. Using a 6-inch roll at 150 ° C for 7
After kneading for a minute, it was formed into a sheet having a thickness of 0.2 mm, and the number of fish eyes contained in 100 cm ^{2 of the} obtained sheet was examined by a light transmission method. Further, the brightness index (L value) when the polymer obtained in each experiment was molded into a sheet was measured by the following method. The results are shown in Table 2.

Measurement of lightness index (L value) 100 parts by weight of the obtained polymer, a stabilizer (TS manufactured by Akishima Chemical Co., Ltd., TS
-101) 1 part by weight, stabilizer (C-100 J, manufactured by Katsuta Kako Co., Ltd.)
0.5 parts by weight and 50 parts by weight of dioctyl phthalate as a plasticizer are kneaded in a two-roll mill at 160 ° C. for 5 minutes, and then formed into a sheet having a thickness of 1 mm. Next, put the formed sheet into a 4 x 4 x 1.5 cm mold, and keep it at 160 ℃ and 65 to 70 kgf / cm.
Heat the sample at ² for 0.2 hours and press-mold it to make a sample for measurement. For this sample, the lightness index L in the Hunter color difference formula described in JIS Z 8730 (1980) was obtained, and the larger the L value, the higher the whiteness, that is, the better the initial colorability.

The L value is obtained as follows. JIS Z 8722
The standard value C, photoelectric colorimeter (manufactured by Nippon Denshoku Industries Co., Ltd., Z-1001DP colorimetric color difference meter) is used to obtain the stimulus value Y of the XYZ color system by the stimulus value direct reading method. As the geometric condition of illumination and light reception, condition d described in JIS Z 8722, section 4.3.1 was adopted. From the obtained stimulation value Y,
The L value is calculated by the formula: L = 10 Y ^1/2 described in JIS Z 8730 (1980).

[0053]

[Table 2]

Example 2 (Experiment Nos. 201 to 208) Polymerization was carried out as follows using a stainless steel polymerization vessel equipped with a stirrer and having an internal volume of 20 liters. In each experiment, the condensation product and the solvent shown in Table 3 were used to prepare a coating solution so that the solvent ratio and the concentration shown in the same table were obtained. As in Example 1, these coating solutions were applied to the inner wall of the polymerization vessel, the stirring shaft, the stirring blades, and other portions where the monomers come into contact with each other during the polymerization, to form a coating film and wash with water. However, No. 2 marked with * in Table 3
The experiments of 02 and 203 are comparative examples in which a coating solution which does not satisfy the conditions of the present invention is applied.

Next, 9 kg of water and sodium dodecylbenzenesulfonate 2 were placed in the coating vessel thus coated.
After charging 25 g, t-dodecyl mercaptan 12 g and potassium peroxodisulfate 13 g and substituting with nitrogen gas, 1.3 kg of styrene and 3.8 kg of butadiene were charged and polymerization was carried out at 50 ° C. for 20 hours. After the polymerization was completed, the produced polymer and unreacted monomer were recovered, and the inside of the polymerization vessel was washed with water to remove the residual resin.

Thereafter, the above operation of polymerization and washing of the inner wall of the polymerization vessel was set as one batch without performing the coating operation, and the same operation was repeated for the number of batches shown in Table 3, and after the end of the final batch, the liquid phase part in the polymerization vessel was repeated. The amount of scale adherence and the amount of scale adherence near the interface between the gas phase part and the liquid phase part were determined by the same method as in Example 1. The results are shown in Table 3. The lightness index (L
The value was measured by the following method. The results are shown in Table 3.

Measurement of lightness index (L value) 1 kg of a 2% magnesium sulfate solution was added to 1 kg of the obtained polymer.
Is added to carry out coagulation precipitation, and then the precipitate is separated by filtration. The precipitate separated by filtration was washed with hot water at 80 to 90 ° C. for 2 to 3 times,
A resin was obtained by drying at 40 ° C. for 25 hours using a vacuum dryer.
Put the resin obtained in a 9 × 9 cm, 0.1 cm thick mold,
95 ° C., and heated at 50 to 60 kgf / cm ² 0.2 hours, the final pressure 80kg
A sample for measurement is prepared by pressure molding at f / cm ² . The lightness index L value of this sample was determined in the same manner as described above.

[0058]

[Table 3]

[0059]

According to the present invention, the adhesion of polymer scale can be effectively prevented not only in the liquid phase part in the polymerization vessel but also in the vicinity of the interface between the gas phase part and the liquid phase part. The resulting product polymer has less fish eyes after molding. Furthermore, the coating film formed on the inner wall surface of the polymerization vessel according to the present invention does not peel off during the polymerization or dissolve in the polymerization system. Good property.

Further, according to the present invention, since the coating liquid used for forming the coating film contains water as a main component, there is little risk of ignition and explosion of the organic solvent, and toxicity is not a problem. Can be used in a range. Further, when the present invention is applied to carry out the polymerization, it is not necessary to carry out the work of removing the polymer scale for each polymerization, thereby improving the productivity.

Claims (3)

[Claims] 1. A monomer having an ethylenic double bond, comprising a condensation product obtained by condensing (A) an aliphatic diamine compound and (B) a naphthoquinone compound in an aqueous medium. Polymer scale anti-adhesion agent for polymerization of. 2. An ethylenic double bond on which a coating film containing a condensation product obtained by condensing (A) an aliphatic diamine compound and (B) a naphthoquinone compound in an aqueous medium is formed. A polymerization vessel for polymerizing a monomer having: 3. A method for producing a polymer by polymerizing a monomer having an ethylenic double bond in a polymerization vessel,
The polymerization is carried out in a polymerization vessel having a coating film containing a condensation product obtained by condensing (A) an aliphatic diamine compound and (B) a naphthoquinone compound on the inner wall of the polymerization vessel in an aqueous medium. A method of manufacturing, which has a step, whereby adhesion of polymer scale in a polymerization vessel is prevented.