JPH06184218A - Production of vinyl chloride-based polymer - Google Patents

Production of vinyl chloride-based polymer

Info

Publication number
JPH06184218A
JPH06184218A JP33711392A JP33711392A JPH06184218A JP H06184218 A JPH06184218 A JP H06184218A JP 33711392 A JP33711392 A JP 33711392A JP 33711392 A JP33711392 A JP 33711392A JP H06184218 A JPH06184218 A JP H06184218A
Authority
JP
Japan
Prior art keywords
vinyl chloride
polymer
based polymer
vinyl
boric acid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP33711392A
Other languages
Japanese (ja)
Inventor
Toshihiko Tanaka
利彦 田中
Hiroshi Minamide
博 南出
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tosoh Corp
Original Assignee
Tosoh Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tosoh Corp filed Critical Tosoh Corp
Priority to JP33711392A priority Critical patent/JPH06184218A/en
Publication of JPH06184218A publication Critical patent/JPH06184218A/en
Pending legal-status Critical Current

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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

PURPOSE:To obtain the subject polymer, hardly causing a reduction in bulk specific gravity due to the electrification and excellent in powder fluidity, etc., by dehydrating a slurry, containing a vinyl chloride-based polymer and prepared by the suspension (co)polymerization and then adding boric acid as an aqueous solution thereto. CONSTITUTION:Vinyl chloride monomer or a mixture of vinylic monomers consisting essentially of the vinyl chloride is initially and usually subjected to the suspension (co)polymerization in the presence of a suspending agent and a polymerization initiator in an aqueous medium to provide a vinyl chloride- based polymer. A slurry containing the resultant vinyl chloride-based polymer is then dehydrated and boric acid in an amount of 0.001-0.5 pt.wt. based on the vinyl chloride-based polymer as an aqueous solution is subsequently added to the prepared polymer cake or vinyl chloride-based polymer powder obtained by drying the cake. Furthermore, e.g. vinyl acetate and methyl acrylate can be used as the vinylic monomers copolymerizable with the vinyl chloride.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、懸濁重合法により塩化
ビニル系重合体を製造する方法に関し、特に、優れた粉
体流動性を有する塩化ビニル系重合体の製造方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a vinyl chloride polymer by a suspension polymerization method, and more particularly to a method for producing a vinyl chloride polymer having excellent powder fluidity.

【0002】[0002]

【従来の技術】塩化ビニル系重合体は、通常、懸濁重合
法によって製造され、スラリーからの分離、乾燥等の精
製の後、空気輸送により搬送後保管され、あるいは袋詰
めされる。
2. Description of the Related Art Vinyl chloride polymers are usually produced by a suspension polymerization method, purified by separation from a slurry, dried, etc., transported by air transportation and then stored or packed.

【0003】しかしながら、このようにして得られた塩
化ビニル系重合体は、搬送や袋詰の過程でそれ自体およ
び他の物との摩擦により静電気を帯び流動性が低下し、
製造直後の塩化ビニル系重合体に比べて嵩比重が減少す
るため、著しく取り扱いにくくなり、作業に重大な支障
をきたすという問題がある。
However, the vinyl chloride polymer thus obtained is charged with static electricity due to friction with itself and other substances during transport and bagging, and its fluidity is lowered,
Since the bulk specific gravity is reduced as compared with the vinyl chloride polymer immediately after production, there is a problem that it becomes extremely difficult to handle and seriously hinders work.

【0004】このような重合体の帯電による悪影響を低
減する方法として、従来、帯電防止剤である非イオン系
界面活性剤またはカチオン系界面活性剤等を塩化ビニル
系重合体に添加する方法やスチームを塩化ビニル重合体
に吹込んで湿度を調整する方法が用いられてきた。
As a method for reducing the adverse effects of such polymer charging, conventionally, a method of adding a nonionic surfactant or a cationic surfactant, which is an antistatic agent, to a vinyl chloride polymer or steam. The method of controlling the humidity by blowing the vinyl chloride polymer has been used.

【0005】[0005]

【発明が解決しようとする課題】しかし、上記の界面活
性剤を添加する方法は、重合体の嵩比重の減少を十分に
防止することができず、さらに製品の熱安定性および初
期着色性に悪影響を与えるという欠点を有している。ま
た、スチームを吹込む方法では必要な労働力の増加、設
備の複雑化等を招くという欠点を有している。
However, the above-mentioned method of adding a surfactant cannot sufficiently prevent the decrease of the bulk specific gravity of the polymer, and further the heat stability and the initial colorability of the product are not improved. It has the drawback of having an adverse effect. Further, the method of blowing steam has drawbacks such as an increase in required labor force and complication of equipment.

【0006】そこで、本発明の目的は、帯電による嵩比
重の減少が起こりにくく、しかも、良好な品質を有する
塩化ビニル系重合体を製造する方法を提供することにあ
る。
Therefore, an object of the present invention is to provide a method for producing a vinyl chloride polymer having good quality which is unlikely to decrease in bulk specific gravity due to electrification.

【0007】[0007]

【課題を解決するための手段】本発明らは、上記目的を
達成するために鋭意検討を行った結果、本発明を完成す
るに至った。すなわち本発明は、塩化ビニル単量体また
は塩化ビニルを主成分とするビニル系単量体の混合物を
水性媒体中で懸濁重合し、塩化ビニル系重合体を製造す
るに際し、塩化ビニル系重合体を含有するスラリーを脱
水した後に、ホウ酸を水溶液として前記塩化ビニル系重
合体に対して0.001〜0.5重量部添加することを
特徴とする塩化ビニル系重合体の製造方法である。
Means for Solving the Problems The present inventors have completed the present invention as a result of intensive studies to achieve the above object. That is, the present invention is to produce a vinyl chloride-based polymer by suspension-polymerizing a vinyl chloride-based monomer or a mixture of vinyl-based monomers containing vinyl chloride as a main component in an aqueous medium. The method for producing a vinyl chloride-based polymer is characterized in that 0.001 to 0.5 part by weight of boric acid is added as an aqueous solution to the vinyl chloride-based polymer after the slurry containing is dehydrated.

【0008】本発明の方法では、まず懸濁重合方法によ
り塩化ビニル系重合体が合成される。塩化ビニル系重合
体としては塩化ビニルの単独重合体、塩化ビニルと共重
合可能な他の重合性ビニル系単量体との共重合体が挙げ
られる。塩化ビニルと共重合可能なビニル系単量体とし
ては、例えば、酢酸ビニルのようなアルキルビニルエス
テル、セチルビニルエーテルのようなアルキルビニルエ
ーテル、エチレンまたはプロピレンなどのα−モノオレ
フィン系単量体、アクリル酸メチルのようなアクリル酸
アルキルエステル、メタクリル酸メチルのようなメタク
リル酸アルキルエステルが挙げられる。
In the method of the present invention, a vinyl chloride polymer is first synthesized by the suspension polymerization method. Examples of vinyl chloride-based polymers include homopolymers of vinyl chloride and copolymers with other polymerizable vinyl-based monomers copolymerizable with vinyl chloride. Examples of vinyl monomers copolymerizable with vinyl chloride include alkyl vinyl esters such as vinyl acetate, alkyl vinyl ethers such as cetyl vinyl ether, α-monoolefin monomers such as ethylene and propylene, and acrylic acid. Examples thereof include acrylic acid alkyl esters such as methyl, and methacrylic acid alkyl esters such as methyl methacrylate.

【0009】塩化ビニル系重合体の懸濁重合は良く知ら
れており、塩化ビニル単量体または塩化ビニル単量体と
他の重合性ビニル単合性ビニル単量体とを懸濁剤、重合
開始剤の存在下、水性媒体中で重合させることにより行
われ、この懸濁重合法により塩化ビニル系重合体を含有
するスラリーを得ることができる。
Suspension polymerization of vinyl chloride type polymers is well known, and a vinyl chloride monomer or a vinyl chloride monomer and another polymerizable vinyl unifying vinyl monomer are used as a suspending agent and polymerized. Polymerization is carried out in an aqueous medium in the presence of an initiator, and a suspension containing a vinyl chloride polymer can be obtained by this suspension polymerization method.

【0010】次に、本発明の方法によると、塩化ビニル
系重合体を含有するスラリーを脱水した後、得られた重
合体ケーキまたは該重合体ケーキを乾燥した塩化ビニル
系重合体の粉末にホウ酸を水溶液として添加する。ホウ
酸の添加量は、塩化ビニル系重合体100重量部に対し
て0.001〜0.5重量部添加することが望ましい。
その添加量が0.001重量部未満であると帯電による
かさ比重の極端な低下を防止できない。一方、添加量が
0.5重量部を超えても添加の効果はそれ以上高まらな
いので経済的でない。
Next, according to the method of the present invention, after dehydrating the slurry containing the vinyl chloride polymer, the obtained polymer cake or the polymer cake is dried into powder of the vinyl chloride polymer. The acid is added as an aqueous solution. The amount of boric acid added is preferably 0.001 to 0.5 parts by weight with respect to 100 parts by weight of the vinyl chloride polymer.
If the added amount is less than 0.001 part by weight, it is not possible to prevent an extreme decrease in bulk specific gravity due to electrification. On the other hand, even if the amount added exceeds 0.5 parts by weight, the effect of the addition does not increase any more, which is not economical.

【0011】[0011]

【実施例】以下、本発明を実施例によって具体的に説明
するが、本発明はこれらに限定されるものではない。
EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited thereto.

【0012】実施例1 ステンレス製重合器に、塩化ビニル単量体100重量
部、脱イオン水150重量部、部分鹸化ポリビニルアル
コール0.1重量部および2−エチルヘキシルパーオキ
シジカーボネート0.04重量部を仕込み、温度57℃
で重合を行い重合器内の圧力が6.0kg/cm2Gに
達したときに未反応の塩化ビニル単量体を回収し、脱水
して20重量%の水を含む塩化ビニル重合体ケーキを得
た。こうして得られた重合体ケーキにホウ酸を重合体に
対して0.01重量部添加した後、70℃で2時間流動
乾燥し塩化ビニル重合体を得た。なお、ホウ酸は50%
水溶液として重合体ケ−キに添加した。
Example 1 100 parts by weight of vinyl chloride monomer, 150 parts by weight of deionized water, 0.1 part by weight of partially saponified polyvinyl alcohol and 0.04 part by weight of 2-ethylhexyl peroxydicarbonate were placed in a stainless steel polymerization vessel. , Temperature of 57 ℃
When the pressure in the polymerization vessel reaches 6.0 kg / cm 2 G, unreacted vinyl chloride monomer is recovered and dehydrated to obtain a vinyl chloride polymer cake containing 20% by weight of water. Obtained. To the polymer cake thus obtained, 0.01 part by weight of boric acid was added to the polymer, and then fluidized and dried at 70 ° C. for 2 hours to obtain a vinyl chloride polymer. 50% boric acid
It was added to the polymer cake as an aqueous solution.

【0013】実施例2 ステンレス製重合器に、塩化ビニル単量体100重量
部、脱イオン水150重量部、部分鹸化ポリビニルアル
コール0.1重量部および2−エチルヘキシルパーオキ
シジカーボネート0.04重量部を仕込み、温度57℃
で重合を行い重合器内の圧力が6.0kg/cm2 Gに
達したときに未反応の塩化ビニル単量体を回収し、脱水
した後、70℃で2時間流動乾燥し塩化ビニル重合体を
得た。得られた塩化ビニル重合体に流動状態下で、ホウ
酸を重合体に対して0.03重量部添加した。なお、ホ
ウ酸は水溶液として重合体に添加した。
Example 2 100 parts by weight of vinyl chloride monomer, 150 parts by weight of deionized water, 0.1 part by weight of partially saponified polyvinyl alcohol and 0.04 part by weight of 2-ethylhexyl peroxydicarbonate were placed in a stainless steel polymerization vessel. , Temperature of 57 ℃
The unreacted vinyl chloride monomer was recovered when the pressure in the polymerization vessel reached 6.0 kg / cm 2 G, dehydrated, and then fluidized and dried at 70 ° C. for 2 hours to obtain a vinyl chloride polymer. Got To the obtained vinyl chloride polymer, 0.03 parts by weight of boric acid was added to the polymer in a fluidized state. Boric acid was added to the polymer as an aqueous solution.

【0014】実施例3 ホウ酸の添加量、水溶液濃度を表1に示す条件とした以
外は、実施例2と同様にして塩化ビニル重合体を得た。
Example 3 A vinyl chloride polymer was obtained in the same manner as in Example 2 except that the addition amount of boric acid and the concentration of the aqueous solution were changed to those shown in Table 1.

【0015】比較例1 ホウ酸を添加しないかった以外は、実施例2と同様にし
て塩化ビニル重合体を得た。
Comparative Example 1 A vinyl chloride polymer was obtained in the same manner as in Example 2 except that boric acid was not added.

【0016】比較例2 ホウ酸の代わりにポリオキシエチレンソルビタンモノラ
ウレートの50%水溶液を用いた以外は、実施例2と同
様にして塩化ビニル重合体を得た。
Comparative Example 2 A vinyl chloride polymer was obtained in the same manner as in Example 2 except that a 50% aqueous solution of polyoxyethylene sorbitan monolaurate was used instead of boric acid.

【0017】比較例3 ホウ酸の添加量、水溶液濃度を表1に示す条件とした以
外は実施例2と同様にして塩化ビニル重合体を得た。
Comparative Example 3 A vinyl chloride polymer was obtained in the same manner as in Example 2 except that the amount of boric acid added and the concentration of the aqueous solution were changed to those shown in Table 1.

【0018】上記の実施例1〜3および比較例1〜3で
得られた塩化ビニル重合体について、下記に示すかさ比
重測定試験および熱安定性試験を行った。その結果を表
1に示す。
The vinyl chloride polymers obtained in Examples 1 to 3 and Comparative Examples 1 to 3 were subjected to the bulk specific gravity measurement test and thermal stability test shown below. The results are shown in Table 1.

【0019】1.かさ比重測定試験 塩化ビニル重合体を温度23℃、相対湿度50%の恒温
恒湿室内に48時間放置した後、かさ比重をJIS K
−6721の方法により測定した。
1. Bulk specific gravity measurement test After leaving the vinyl chloride polymer in a constant temperature and humidity room at a temperature of 23 ° C. and a relative humidity of 50% for 48 hours, the bulk specific gravity is measured according to JIS K.
It was measured by the method of -6721.

【0020】また、上記と同様な条件で48時間放置し
た塩化ビニル重合体を、ブラベンダープラネタリーミキ
サーで60rpm、2分間撹拌後、上記と同じ方法でか
さ比重を比較した。
Further, the vinyl chloride polymer left under the same conditions as above for 48 hours was stirred at 60 rpm for 2 minutes with a Brabender planetary mixer, and the bulk specific gravity was compared by the same method as above.

【0021】2.熱安定性 塩化ビニル重合体100重量部に対して、 三塩基性硫酸鉛 1.0重量部 ステアリン酸鉛 1.5 〃 ステアリン酸カルシウム 0.5 〃 を配合し、190℃のロールで5分間混練した後、厚さ
1mmのシートを作成し、このシートを190℃のオー
ブンに入れて黒化するまでの時間を測定した。
2. Thermal stability To 100 parts by weight of vinyl chloride polymer, 1.0 part by weight of tribasic lead sulfate, 1.5 parts of lead stearate, 1.5 parts of calcium stearate, and 0.5 parts of calcium stearate were mixed and kneaded for 5 minutes with a roll at 190 ° C. Then, a sheet having a thickness of 1 mm was prepared, and the sheet was placed in an oven at 190 ° C. and the time until blackening was measured.

【0022】[0022]

【表1】 [Table 1]

【0023】[0023]

【発明の効果】以上述べたとおり、本発明によれば帯電
による嵩比重の減少が起こりにくく、優れた粉体流動性
を有し、また熱安定性などの品質が良好な塩化ビニル系
重合体を得ることができる。
As described above, according to the present invention, a vinyl chloride polymer which is less likely to decrease in bulk specific gravity due to electrification, has excellent powder fluidity, and has good quality such as thermal stability. Can be obtained.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】塩化ビニル単量体または塩化ビニルを主成
分とするビニル系単量体の混合物を水性媒体中で懸濁重
合し、塩化ビニル系重合体を製造するに際し、塩化ビニ
ル系重合体を含有するスラリーを脱水した後に、ホウ酸
を水溶液として前記塩化ビニル系重合体に対して0.0
01〜0.5重量部添加することを特徴とする塩化ビニ
ル系重合体の製造方法。
1. A vinyl chloride polymer, which is prepared by suspension polymerization of a vinyl chloride monomer or a mixture of vinyl monomers containing vinyl chloride as a main component in an aqueous medium to produce a vinyl chloride polymer. After dehydrating the slurry containing the above, boric acid as an aqueous solution is added to the vinyl chloride polymer in an amount of 0.0
A method for producing a vinyl chloride-based polymer, which comprises adding 01 to 0.5 part by weight.
JP33711392A 1992-12-17 1992-12-17 Production of vinyl chloride-based polymer Pending JPH06184218A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33711392A JPH06184218A (en) 1992-12-17 1992-12-17 Production of vinyl chloride-based polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33711392A JPH06184218A (en) 1992-12-17 1992-12-17 Production of vinyl chloride-based polymer

Publications (1)

Publication Number Publication Date
JPH06184218A true JPH06184218A (en) 1994-07-05

Family

ID=18305565

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33711392A Pending JPH06184218A (en) 1992-12-17 1992-12-17 Production of vinyl chloride-based polymer

Country Status (1)

Country Link
JP (1) JPH06184218A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1988000123A1 (en) * 1986-07-03 1988-01-14 Fanuc Ltd Method of controlling an injection motor having overheat preventing function

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1988000123A1 (en) * 1986-07-03 1988-01-14 Fanuc Ltd Method of controlling an injection motor having overheat preventing function
US4847023A (en) * 1986-07-03 1989-07-11 Fanuc Ltd. Method for controlling an injection motor to prevent overheating

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