JPH1036407A - Production of vinyl chloride polymer - Google Patents

Abstract

PROBLEM TO BE SOLVED: To obtain at a high productivity a vinyl chloride polymer excellent in polymn. stability and qualities such as freeness from fisheyes by using a specified amt. of a specified water-soluble polymer dispersant and also by employing a specified feeding method. SOLUTION: A vinyl chloride monomer is suspension-polymerized in an aq. medium by (A) feeding deaerated warm water and soon after a vinyl chloride monomer or feeding them simultaneously into a deaerated polymerizer, (B) feeding an oil-soluble initiator and an aq. soln. of a water-soluble polymer dispersant simultaneously with the start of the feeding of the vinyl chloride monomer, (C) selecting the water-soluble polymer dispersant so that it comprises 0.01 to 0.04 pt.wt. (for 100 pts.wt. monomer) partially saponified polyvinyl acetate and 0.0001 to 0.005 pt.wt. water-soluble emulsifier and/or oil-soluble emulsifier, and (D) controlling the time of the step B so that the step B is completed within 40% of the operation time of the step A. A vinyl chloride polymer excellent in the polymn. stability and qualities such as freeness from fisheyes is obtained at a high productivity.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

The present invention relates to a method for producing a vinyl chloride polymer, and more particularly, to a method for producing a vinyl chloride polymer having excellent polymerization stability and excellent fisheye quality. The present invention relates to a method of manufacturing while maintaining productivity.

[0002]

2. Description of the Related Art Vinyl chloride polymers are inexpensive and have excellent quality balance, and are therefore used in various fields such as light and hard fields. For example, in the hard field,
It is used for pipes, window frames, films, etc., and in the light field, it is used for electric wire coating, sheets, etc., and high quality is required for a wide variety of quality.

[0003] On the other hand, it is the mission of vinyl chloride resins to be an inexpensive material, and various technical studies have been made to produce it inexpensively. For example,
A method of increasing productivity by increasing the capacity of the polymerization vessel, a method of increasing the productivity by first charging a vinyl chloride-based monomer, followed by charging degassed warm water to shorten the heating time, and A method has been proposed in which a vinyl chloride-based monomer and degassed hot water are simultaneously charged to shorten the heating time and thereby increase productivity.

For example, Japanese Patent Publication No. 62-39601 discloses that an aqueous medium (a mixture in which a dispersant is dissolved in water) preheated and a homogeneous mixture of a vinyl chloride monomer and an initiator are simultaneously charged. Japanese Patent Publication No. 60-26488 discloses a method of shortening the heating time and increasing the productivity by adding water in which the entire amount of the dispersant is dissolved and vinyl chloride-based monomer in which the entire amount of the initiator is dissolved. Japanese Patent Application Laid-Open No. 60-158207 discloses a method of increasing the productivity by setting a predetermined temperature at the end of the preparation of both, and comprising a vinyl chloride monomer containing an initiator and a dispersant. 5 with water
A method in which the mixture is preliminarily mixed at 0 ° C. or lower, and the mixture is charged into a polymerization vessel while heating to a reaction temperature in a heat exchanger;
No. 172407 discloses that at least 20% of the dispersant is charged during the charging of the vinyl chloride monomer, and the total amount of the initiator is adjusted while the weight ratio of the vinyl chloride monomer to water in the polymerization vessel is 1.5 or less. A method of charging is disclosed.

However, the method of Japanese Patent Publication No. 62-39601 requires a tank and a special mixer for uniform mixing of the initiator, which not only complicates the charging operation but also starts the polymerization at the same time as the charging. Since the reaction starts rapidly and there is no time to disperse the dispersant uniformly on the surface of the suspended oil droplets and form a stable protective layer, polymerization stability is poor, coarse particles are large, and fish eye Is disadvantageously increased.

In the method of JP-B-60-26488, although there is a slight time difference in the charging time of the vinyl chloride monomer in which water and the whole amount of the initiator are dissolved, the method of JP-B-62-26488 is used.
As in the method of JP-A-39601, there are disadvantages such as poor polymerization stability, a large amount of coarse particles, and an increase in fish eyes.

The method disclosed in Japanese Patent Application Laid-Open No. 60-158207 has a problem that since the mixture is preliminarily mixed and heated to a reaction temperature in a heat exchanger, heat exchange takes time and the effect of improving productivity is small. The method disclosed in Japanese Patent Application Laid-Open No. 1-172407 is an improvement of the above, but similarly, the problems of poor polymerization stability, a large amount of coarse particles, and an increase in fish eyes cannot be sufficiently solved. , The problem remained. As described above, the method of charging the heated dispersant-containing hot water and the initiator-containing vinyl chloride monomer simultaneously or with a slight time difference has an effect of improving productivity, but has poor polymerization stability. In addition, there are problems such as a large amount of coarse particles, an increase in fish eyes, and a problem that a large amount of a dispersing agent is required to maintain polymerization stability, resulting in an increase in cost.

Further, Japanese Patent Application Laid-Open No. 58-21408 discloses that
A method in which water degassed by heating and degassing at 50 to 80 ° C. in advance, Japanese Patent Publication No. 50603/1983, is used. A dispersant and cold water are charged in a polymerization vessel, and then a vinyl chloride monomer is charged.
A method for charging heated water is disclosed. However, in the former (Japanese Patent Application Laid-Open No. 58-21408), a vinyl chloride monomer containing an initiator comes into direct contact with the inner surface of a polymerization vessel during charging, so that a film scale is easily generated, and the polymerization heat is increased. However, since the heat removal ability of the polymer significantly decreases, it is impossible to shorten the polymerization time and the like, and there is a problem that the productivity cannot be increased due to an increase in the operation rate. The latter (Japanese Patent Publication No. 58-50603)
No.) has the effect of improving fisheye, but has a problem that the charging time is long because the vinyl chloride monomer and hot water are sequentially charged, and the productivity cannot be increased by increasing the operation rate.

[0009]

SUMMARY OF THE INVENTION An object of the present invention is to provide a method for simultaneously charging a vinyl chloride monomer and hot water and a problem for a method for previously charging the vinyl chloride monomer, that is, a scale on the inner surface of the polymerization vessel. Without causing quality problems such as adhesion, deterioration of polymerization stability, generation of coarse particles, generation of fish eyes,
The purpose of the present invention is to shorten the preparation time, improve the polymerization operation rate, and provide a method for producing a highly productive vinyl chloride polymer.In other words, the relation between quality problems and productivity conflicts. It aims to improve balance.

[0010]

Means for Solving the Problems The present inventors have conducted various studies to improve the balance between the problems of quality and the conflicting relationship of productivity. By using a specific amount of the conductive polymer dispersant, the effect of stirring and mixing, the dispersing power in the initial stage of polymerization is increased
The present inventors have found that productivity can be improved without causing quality problems, and have completed the present invention.

That is, the present invention provides a method for suspension polymerization of a vinyl chloride monomer in an aqueous medium using an oil-soluble initiator and a water-soluble polymer dispersant. Degassed warm water and vinyl chloride monomer are charged simultaneously or slightly earlier with warm water. (B) Oil-soluble initiator, water-soluble polymer dispersant at the same time as the start of vinyl chloride monomer charging Are introduced into the vinyl chloride-based monomer line and the warm water line, respectively, through dedicated measuring lines, and are charged. (C) The aqueous solution of the water-soluble polymer dispersant used in the step (b) is (1) ) Partially saponified polyvinyl acetate,
(2) a dispersant system in which at least one emulsifier selected from the group consisting of a water-soluble emulsifier and an oil-soluble emulsifier is combined, and the amount of the partially saponified polyvinyl acetate (1) used is 0.01 with respect to 100 parts by weight of the monomer
0.04 parts by weight, and the amount of the emulsifier used in (2) is
0.0001 to 100 parts by weight of the vinyl chloride monomer
(D) completing the operation of the step (b) within 40% of the operation time of the step (a). I do.

In particular, in the above step (a), polymerization stability is remarkable when the degassed warm water is first charged and then a vinyl chloride monomer is charged with a time difference of 1 to 2 minutes or less. To be improved.

In carrying out the present invention, first, in step (a), degassed hot water and a vinyl chloride monomer are charged into a degassed polymerization vessel. At this time, the warm water and the vinyl chloride monomer may be charged at the same time for the first time, but it is preferable to charge the warm water slightly earlier. If the time difference is long, the charging end time is long, which is not preferable. Therefore, preferably,
About 1-2 minutes is good. The polymerization is stabilized by charging degassed warm water first, and a polymer having a small amount of coarse particles and fine powder and a sharp particle size distribution can be obtained. The time required for the preparation of warm water and the preparation of the vinyl chloride-based monomer depends on the pumping capacity, but is preferably completed within 25 minutes.

Next, as a step (b), an oil-soluble initiator,
An aqueous solution of a water-soluble polymer dispersant is introduced into a vinyl chloride-based monomer line and a warm water line through dedicated measuring lines, respectively, and charging is started. In the present invention, the oil-soluble initiator and the aqueous solution of the water-soluble polymer dispersant are started at substantially the same time as the charging of the vinyl chloride-based monomer, and 40% of the total charging time.
The processing is completed within 10 minutes when the total preparation time is 25 minutes. If it exceeds 40% of the total charge time, the charge of the initiator becomes too slow, the polymerization time becomes long, and the productivity becomes poor. In addition, the charge of the dispersant becomes too slow, so that the oil droplets initially dispersed are protected. Insufficient protective power causes abnormal polymerization or coarse particles. Conventionally, it has been proposed that an oil-soluble initiator and an aqueous solution of a water-soluble polymer dispersant be homogeneously charged in a vinyl chloride monomer or warm water, but in order to homogenize a separate tank is required. Or
It requires special metering equipment to control the uniformity and is not practical. For the measurement of the oil-soluble initiator and the aqueous solution of the water-soluble polymer dispersant, dedicated lines are respectively used. The respective measurement lines are connected to a vinyl chloride monomer line and a hot water line, and are introduced into a polymerization vessel. The polymerization reaction starts simultaneously with the introduction of the oil-soluble initiator, but at the same time, a relatively concentrated aqueous solution of the water-soluble polymer dispersant exists. A polymer having less fine powder and a sharp particle size distribution can be easily obtained. Further, since the polymerization reaction proceeds simultaneously with the introduction of the initiator, the polymerization time including the time for raising the temperature is shortened, which is important in maintaining high productivity.

The dispersant system used in step (b) is
It is a dispersant system combining (1) partially saponified polyvinyl acetate and (2) a water-soluble or oil-soluble emulsifier. Among the conventionally known dispersants, for example, water-soluble cellulose-based dispersants such as methylcellulose, hydroxyethylcellulose, hydroxymethylcellulose, and hydroxypropylcellulose have a strong oil-drop protecting power at the time of initial dispersion and tend to be insufficiently homogenized. It is not preferable. However, it may be added in combination if it is used in such an amount that the initial dispersion is not impaired, specifically, a very small amount of about 0.02 parts by weight or less based on 100 parts by weight of the charged monomer. Further, a water-soluble polymer dispersant such as a polyacrylic acid-based dispersant, starch, gelatin, polyoxyethylene, or polyvinylpyrrolidone is not preferable because the initial dispersing power is insufficient. As the partially saponified polyvinyl acetate used in the present invention, conventionally known ones can be used alone or in combination of two or more.
The amount used is based on 100 parts by weight of the charged monomer.
The range of 0.01 to 0.04 parts by weight, which is smaller than the conventional amount, is good. If the amount is less than 0.01 part by weight, the oil droplet protecting power at the time of the initial dispersion is insufficient, resulting in abnormal polymerization. If the amount exceeds 0.04 part by weight, the oil droplet protecting power at the time of the initial dispersion becomes too strong, and the homogenization is insufficient. This causes inconveniences such as an increase in fine powder and an increase in fish eyes.

In the present invention, it is necessary to use a conventionally known oil-soluble emulsifier or water-soluble emulsifier. This emulsifier is used for maintaining the initial dispersion of a heterogeneous system in which the charged state gradually changes and the polymerization is progressing. The type is not particularly limited. One or more polyoxyethylene-based water-soluble emulsifiers such as monolaurate and polyoxyethylene glycerin oleate, and fatty acid metal salt-based water-soluble emulsifiers such as sodium laurate can be used. In particular, when an oil-soluble emulsifier is used, a vinyl chloride polymer having a good balance of physical properties can be obtained. The amount of the emulsifier used is
0.0001 to 100 parts by weight of the charged monomer
The amount used may be less than the conventional amount of about 0.005 parts by weight. If the amount is less than 0.0001 part by weight, the oil droplet forming force and the surface tension at the time of the initial dispersion are insufficiently reduced, causing disadvantages such as an increase in coarse particles and an increase in fish eyes.
If the amount is more than 5 parts by weight, heat stability, initial coloration, and polymer quality such as broadening of particle size distribution are reduced, or abnormal polymerization due to excessive dispersion is caused.

Particularly preferred dispersant systems are those having a degree of saponification of from 60 to
85 mol%, one or more of partially saponified polyvinyl acetates having a degree of polymerization of 1000 to 2500 are used in an amount of 0.02 to 0.04.
Parts by weight, and in addition, one or more emulsifiers selected from glycerin-based oil-soluble emulsifiers, sorbitan-based oil-soluble emulsifiers, polyoxyethylene-based water-soluble emulsifiers, and fatty acid metal salt-based water-soluble emulsifiers 0.0001-0.0
It is a dispersant system that uses a very small amount of 05 parts by weight and improves the dispersion efficiency.

In the present invention, the stirring operation is preferably performed at the same time as the start of the step (b), and it is important to homogenize the components charged in the polymerization vessel as soon as possible. The stirring speed varies depending on the shape of the stirring blade,
When the stirring speed is 5.0 m / sec or more, the effect of the present invention can be easily achieved. If the stirring blade peripheral speed is less than 5.0 m / sec, homogenization becomes incomplete and disadvantages such as an increase in fish eyes, a broad particle size distribution, an increase in coarse particles and fine powder, and an abnormal polymerization are not preferred. 5.0m / sec
A stirring blade suitable for maintaining the above-mentioned peripheral speed of the stirring blade is an inclined paddle or a blue margin blade. The inclination angle of the inclined paddle is preferably an inclined paddle blade having a small stirring torque of 10 ° or less.

In the present invention, degassed hot water is used. The temperature of the degassed hot water is preferably 50 to 80 ° C., and is preferably as high as possible to control the polymerization. (B) Although the polymerization temperature has reached the predetermined polymerization temperature in the middle of the process and polymerization has been started, conventional heat removal methods, for example, jacket heat removal, reflux condenser heat removal, and internal jacket heat removal are used. Then, the polymerization reaction may be controlled.

In the present invention, the conversion at the end of the charging is controlled, and the H (water) / M (monomer) in the step (b) is controlled.
It is not necessary to control the ratio, and the heat may be removed in accordance with the polymerization exothermic state. By selecting a special dispersant system, sufficient homogenization can be achieved, and reduction of polymerization stability, generation of coarse particles and fine powder, broadening of particle size distribution, generation of fish eyes, etc. can be easily suppressed. it is conceivable that.

As the polymerization initiator used in the present invention, conventionally known initiators can be used. Of the conventionally known initiators, 10
It is preferable to use one or more of those having a time half-life of 30 to 65 ° C. The amount of the initiator used varies depending on the type and polymerization temperature, but is preferably 0.005 to 0.5 part by weight based on 100 parts by weight of the charged monomer. By using this amount of initiator, the polymerization time can be less than 6 hours. As such a polymerization initiator, acetylcyclohexylsulfonyl peroxide,
2,4,4-trimethylpentyl-2-peroxyneodecanoate, di-2-ethylhexylperoxydicarbonate, di (2-ethoxyethyl) peroxydicarbonate, t-butylperoxypivalate, 3,
Organic peroxide initiators such as 5,5-trimethylhexanoyl peroxide and azo compounds such as azobisisobutyronitrile and azobis-2,4-dimethylvaleronitrile can be used, and these can be used alone or in combination of two or more. Used.

These initiators are used in step (b)
It is weighed in a dedicated line, cut into a vinyl chloride monomer charging line, and introduced into a polymerization vessel. In order to start the polymerization reaction as soon as possible and to shorten the temperature rise time and the total polymerization time, it is better to perform the charging of the initiator as early as possible. % (10% if the total preparation time is 25 minutes)
It is preferable to carry out within the time of (minute).

The monomer used in the present invention is a monomer containing vinyl chloride as a main component, and specifically, a vinyl chloride monomer alone or containing 70% or more of vinyl chloride and It is a mixture with a copolymerizable monomer.

As the monomer copolymerizable with vinyl chloride, conventionally known monomers can be used. For example, vinyl esters such as vinyl acetate and vinyl propionate, (meth) acrylates such as methyl (meth) acrylate and propyl (meth) acrylate, olefins such as ethylene and propylene, 1-chloropropylene, 2-
Examples thereof include chlorinated olefins such as chlorobutylene, maleic esters such as butyl maleate or monomers, acid anhydrides, monomers such as acrylonitrile, styrene, and vinylidene chloride. Other than the above, polymerization regulators, chain transfer agents, p-type compounds conventionally used for the polymerization or copolymerization of vinyl chloride monomers.
Additives such as an H adjuster, a gelling improver, an antistatic agent and a cross-linking agent can be used arbitrarily according to the purpose, and the amounts used are the same as in the conventional art.

[0025]

The contents of the present invention will be described in detail with reference to examples, but the present invention is not limited to these examples. In the Examples and Comparative Examples,% indicates weight% unless otherwise specified, and the number of parts indicates weight part. The characteristic values of the obtained vinyl chloride polymer were measured by the following methods.

(1) Fish eye Dioctyl phthalate 5 was added to 100 parts of a vinyl chloride polymer.
After 0 parts, 2 parts of calcium stearate, 1 part of barium stearate and 0.02 part of carbon black were added and thoroughly mixed and dried up, the mixture was poured and kneaded into an 8-inch roll whose surface temperature was adjusted to 150 ° C. Minutes, 5 minutes, 6
A 0.3 mm sheet was sampled on the way in minutes. The number of transparent particles observed in 100 mm ² of the surface of each sampled sheet was counted and shown.

(2) Average particle size, particle size distribution, coarse fraction, P
ASS component According to JIS K-6721, 42, 60, 80, 1
Using a sieve of 00, 120, 145, 200 mesh,
The mixture was sieved with a sieve shaker, and the average particle diameter was defined as the 50% passage diameter. The particle size distribution was measured by measuring the weight of the vinyl chloride polymer remaining on each mesh and expressed as a percentage. Further, the coarse fraction is the residual amount on a 42 mesh sieve (100 fraction, not counted in the fraction of particle size distribution), P
ASS is the amount that passed through 200 mesh (100 fraction)
Displayed with.

(3) Porosity Using a mercury intrusion porosimeter manufactured by Aminco, USA,
When pressurized from normal pressure to 1000 psi, about 0.2 g of P
The volume of mercury injected into the VC was measured, and the value converted per 100 g of the vinyl chloride polymer (PVC) was defined as porosity.

(4) Absorbency of plasticizer Using a laboratory plastomill manufactured by Toyo Seiki Seisaku-sho, at 125 ° C.
Is charged into a container held in the above, and preheated while stirring for 2 minutes, and 300 g of di-2-undecyl phthalate heated to 80 ° C. is charged at a constant rate using a charging device. The stirring at 100 rpm was continued as it was, and the time required for the mixing torque to decrease and stabilize was determined.

(5) Charge time, polymerization time The time from the start of charging cold water, hot water or vinyl chloride monomer to the time when a predetermined polymerization temperature is reached is defined as the charge time. The time from when the pressure dropped by 1 kg / cm ² from the steady pressure to when the polymerization was stopped and the unreacted monomer was started to be collected was defined as the polymerization time.

Example 1 Internal volume 2 provided with a stirrer and a reflux condenser
The inside of the 2,000 L stainless steel polymerization vessel was degassed by a vacuum pump, and the degassed hot water adjusted to a temperature of 65 ° C. was added thereto for about 4 hours.
The charging was started at a rate of 5 L / min, and one minute later, the vinyl chloride monomer was started to be charged at a rate of about 45 L / min. 850L of warm water
Was completed in about 19 minutes, and 790 L of vinyl chloride monomer was charged in about 18 minutes. At the same time as starting to charge the vinyl chloride monomer, about 2 L of 5% aqueous solution of partially saponified polyvinyl acetate
At the speed of / min, the mixture was introduced into the warm water line through the measuring line, and charging was started, and the charging was completed in about 5 minutes. The amount of partially saponified polyvinyl acetate charged was 100 parts of vinyl chloride monomer.
Parts was 0.036 parts. The partially saponified polyvinyl acetate has a saponification degree of 78% and a polymerization degree of 2000.
Was used. 5 of this partially saponified polyvinyl acetate
% Aqueous solution was prepared by mixing and dissolving 0.001 part of a water-soluble emulsifier, polyoxyethylene glycerin oleate, in 100 parts of a vinyl chloride monomer. At the same time as starting to charge the vinyl chloride monomer, a 50% toluene solution of di-2-ethylhexyl peroxydicarbonate was dissolved at a rate of about 0.2 L / min through a measuring line.
Introduced into the vinyl chloride monomer line and started charging, and the charging was completed in about 3 minutes. The charged amount of di-2-ethylhexyl peroxydicarbonate was 10 vinyl chloride monomers.
0.045 parts with respect to 0 parts. Further, a stirrer equipped with a blue margin blade was operated at the same time as the vinyl chloride monomer was charged, and the rotation speed was adjusted so that the peripheral speed of the stirring blade became 8.6 m / sec. Although the internal temperature gradually started to rise at the same time as the start of the charging, the jacket temperature and the temperature were controlled by a reflux condenser, and the internal temperature was adjusted to 57 ° C. 5 minutes before the completion of the charging. Five minutes before the completion of the charging was defined as a time when a predetermined temperature was reached (polymerization start time). The internal temperature was maintained at 57 ° C., and the polymerization was stopped when the internal pressure of the polymerization reactor dropped from the steady pressure by 1 kg / cm ² , and the unreacted monomer was recovered to terminate the polymerization. The obtained slurry was dehydrated and dried to obtain a vinyl chloride polymer, which was used for measuring various properties.

Example 2 The type of the water-soluble emulsifier dissolved in a 5% aqueous solution of partially saponified polyvinyl acetate was polyoxyethylene sorbitan monolaurate, and 0.002 part was dissolved in 100 parts of vinyl chloride monomer. A vinyl chloride polymer was obtained under the same polymerization conditions and under the same polymerization conditions as in Example 1 except that the aqueous solution was used, and subjected to measurement of various properties.

Example 3 An aqueous solution in which 0.002 part of glycerin monooleate as an oil-soluble emulsifier was suspended in 100% of vinyl chloride monomer in a 5% aqueous solution of partially saponified polyvinyl acetate was used. A vinyl chloride polymer was obtained under exactly the same charging operation as in Example 1 under the same polymerization conditions, and used for measurement of various properties.

Example 4 0.030 parts of partially saponified polyvinyl acetate having a degree of saponification of 78% and a degree of polymerization of 2,000, a degree of saponification of 83%, and a degree of polymerization of 230
Except that 0.006 parts of partially saponified polyvinyl acetate was used in combination with 0, and a 5% aqueous solution of partially saponified polyvinyl acetate obtained by mixing and dissolving them was used. Under the same polymerization conditions, a vinyl chloride polymer was obtained and used for measuring various properties.

Comparative Example 1 Except that 0.001 part of a water-soluble emulsifier, polyoxyethylene glycerin oleate, was not mixed and dissolved, a 5% aqueous solution of only partially saponified polyvinyl acetate was used. By operation, under the same polymerization conditions, a vinyl chloride polymer was obtained and used for measurement of various properties.

Comparative Example 2 The charging rate of a 5% aqueous solution of partially saponified polyvinyl acetate in which a water-soluble emulsifier was mixed and dissolved was reduced to a rate of about 0.6 L / min, and introduced into a warm water line through a measuring line. A vinyl chloride polymer was obtained under the same polymerization conditions and under the same polymerization conditions as in Example 1, except that charging was completed in about 15 minutes after the start of charging, and subjected to measurement of various properties.

COMPARATIVE EXAMPLE 3 A 50% toluene solution of di-2-ethylhexylperoxydicarbonate was introduced into a vinyl chloride monomer line at a rate of about 0.04 L / min through a metering line, and charging was started. Except that the preparation was completed in about 15 minutes,
A vinyl chloride polymer was obtained under exactly the same charging operation as in Example 1 under the same polymerization conditions, and used for measurement of various properties.

Comparative Example 4 15 minutes after the start of the preparation of the vinyl chloride monomer, di-2
A 50% toluene solution in which ethylhexyl peroxydicarbonate was dissolved was introduced at a rate of about 0.2 L / min through a measuring line into a vinyl chloride monomer line, and charging was started, and charging was completed in about 3 minutes. In the same manner as in Example 1, a vinyl chloride polymer was obtained under the same polymerization conditions and under the same polymerization conditions, and used for measurement of various properties.

Comparative Example 5 After degassing the inside of the polymerization vessel, the vinyl chloride monomer was started to be charged, and at the same time, a 50% toluene solution in which di-2-ethylhexylperoxydicarbonate was dissolved was dissolved at a rate of about 0.2 L / min. The charging was completed in about 3 minutes, and at the same time, the 5% aqueous solution of partially saponified polyvinyl acetate containing the water-soluble emulsifier used in Example 1 was started to be charged at a rate of about 2 L / min, and the charging was started in about 5 minutes. Completed. About 790 L of vinyl chloride monomer
After the charging was completed in 8 minutes, charging of warm water adjusted to 65 ° C. was started, and charging of 850 L of warm water was completed in about 19 minutes. The type and amount of the initiator and the dispersant are the same as in Example 1, and the polymerization is started about 5 minutes before the completion of the warm water charging. A vinyl chloride polymer was obtained by the same polymerization operation as in Example 1 and used for measurement of various properties.

COMPARATIVE EXAMPLE 6 850 L of ion-exchanged water at about 20 ° C. was charged into a polymerization vessel in about 19 minutes, and then the inside of the polymerization vessel was degassed. Then, a vinyl chloride monomer was started and, simultaneously, di-2-ethylhexyl parylene was added. The charging was completed in about 3 minutes at a rate of about 0.2 L / min with a 50% toluene solution in which oxydicarbonate was dissolved, and at the same time, the partially saponified polyvinyl acetate containing the water-soluble emulsifier used in Example 1. Was started at a rate of about 2 L / min, and the preparation was completed in about 5 minutes. The types and amounts of the initiator and the dispersant were the same as in Example 1, and after completing the vinyl chloride monomer charging, the jacket was heated over about 25 minutes to initiate polymerization. A vinyl chloride polymer was obtained by the same polymerization operation as in Example 1 and used for measurement of various properties.

[0041]

[Table 1]

[0042]

As can be seen from the comparison between Example 1 and Comparative Example 1, when the water-soluble emulsifier polyoxyethylene glycerin oleate was not added, the amount of coarse particles and fish eyes was large, and the plasticizer absorption time was long. PV with broad particle size distribution
C. As can be seen from the comparison between Example 1 and Comparative Example 2,
If the dispersant is charged over a long period of time and the same time as the warm water preparation is used, the dispersant becomes insufficient at the time of initial dispersion, resulting in abnormal polymerization.

As can be seen from the comparison between Example 1 and Comparative Example 3, when the initiator is charged over a long period of time and the same time as that for warm water charging is applied, the initial polymerization rate becomes slow and the polymerization time becomes long. Not only that, P has many coarse particles and fish eyes, long plasticizer absorption time, and broad particle size distribution.
VC. Also, as can be seen from the comparison between Example 1 and Comparative Example 4, when the initiator was added all at once at the end of the monomer preparation, the initial polymerization rate was slowed down, and the polymerization time was prolonged. PVC with many fish eyes, long plasticizer absorption time, and broad particle size distribution.

As can be seen from the comparison between Example 1 and Comparative Example 5, when the monomer is charged before the warm water, the charging time becomes longer, the amount of coarse particles and fish eyes are increased, and the plasticizer absorption time is increased. Long PVC with a broad particle size distribution. Furthermore, as can be seen from the comparison between Example 1 and Comparative Example 6, in the ordinary cold water pre-charging method, the charging time was significantly long, the coarse particles and fish eyes were large, the plasticizer absorption time was long, and the particle size was low. The distribution is also broad PVC.

As described above, according to the present invention, the balance between productivity and quality, particularly fish eye, particle size distribution, plasticizer absorption, etc., is significantly improved as compared with the conventional method, and Excellent PVC can be produced with high productivity, and its industrial value is extremely large. Further, among the present invention, as can be seen from the comparison of Examples 1 to 4, Example 3 using glycerin monooleate as an oil-soluble emulsifier has a particularly excellent quality balance and remarkable effects.

Claims (2)

[Claims] 1. An aqueous medium comprising a vinyl chloride monomer or a mixture of a vinyl chloride monomer and a monomer copolymerizable with vinyl chloride (hereinafter referred to as both vinyl chloride monomers). When performing suspension polymerization using an oil-soluble initiator and a water-soluble polymer dispersant, (a) simultaneously deaerate warm water deaerated in a deaerated polymerization vessel with a vinyl chloride monomer or slightly (B) Simultaneously with the start of the charging of the vinyl chloride monomer, the oil-soluble initiator and the aqueous solution of the water-soluble polymer dispersant are respectively supplied through dedicated measuring lines, respectively, to the vinyl chloride monomer line and the hot water line. (C) the aqueous solution of the water-soluble polymer dispersant used in the step (b) is (1) partially saponified polyvinyl acetate;
(2) a dispersant system in which at least one emulsifier selected from the group consisting of a water-soluble emulsifier and an oil-soluble emulsifier is combined, and the amount of the partially saponified polyvinyl acetate (1) used is 0.01 with respect to 100 parts by weight of the monomer
0.04 parts by weight, and the amount of the emulsifier used in (2) is
0.0001 to 100 parts by weight of the vinyl chloride monomer
(D) the operation of the step (b) is completed within 40% of the operation time of the step (a), a method for producing a vinyl chloride polymer. 2. After starting to add degassed hot water, it is 1 to 2
2. The method according to claim 1, wherein the vinyl chloride monomer is charged within minutes.