JPH09176231A - Production of vinyl chloride resin - Google Patents

Production of vinyl chloride resin

Info

Publication number
JPH09176231A
JPH09176231A JP7340796A JP34079695A JPH09176231A JP H09176231 A JPH09176231 A JP H09176231A JP 7340796 A JP7340796 A JP 7340796A JP 34079695 A JP34079695 A JP 34079695A JP H09176231 A JPH09176231 A JP H09176231A
Authority
JP
Japan
Prior art keywords
vinyl chloride
chloride resin
vinyl
resin
monomer
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
JP7340796A
Other languages
Japanese (ja)
Inventor
Satoru Yamada
悟 山田
Kazuya Kamimura
和也 上村
Toshihiko Tanaka
利彦 田中
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 JP7340796A priority Critical patent/JPH09176231A/en
Publication of JPH09176231A publication Critical patent/JPH09176231A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a good-quality vinyl chloride resin which suffers little from a decrease in bulk density due to electronic charging by adding a specified compound to a resin powder obtained from a slurry containing a vinyl chloride resin. SOLUTION: A slurry containing a vinyl chloride resin is obtained by a suspension polymerization process comprising polymerizing a vinyl chloride monomer or a mixture thereof with a vinyl monomer such as an alkyl vinyl ester (e.g. vinyl acetate, an alkyl vinyl ether (e.g. cetyl vinyl ether or an olefin monomer (e.g. ethylene) in an aqueous medium in the presence of a suspending agent and a polymerization initiator. To a cake obtained by dehydrating this slurry or a resin powder obtained by drying this cake, a solution of dispersion of 0.001-0.5 pt.wt., per 100 pts.wt. vinyl chloride resin, compound represented by the formula (wherein R<1> to R<3> are each a 1-20C alkyl, provided that at least one of them is an 8-18C alkyl) in water, methanol, acetone or the like is added.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、懸濁重合法により
塩化ビニル系樹脂を製造する方法に関するものであり、
更に詳しくは優れた粉体流動性を有する塩化ビニル系樹
脂の製造方法に関するものである。
TECHNICAL FIELD The present invention relates to a method for producing a vinyl chloride resin by a suspension polymerization method,
More specifically, it relates to a method for producing a vinyl chloride resin having excellent powder fluidity.

【0002】[0002]

【従来の技術】塩化ビニル系樹脂は、一般的に懸濁重合
法により製造され、重合後のスラリーからの分離、乾燥
等の後、空気輸送により搬送後保管又は袋詰めされる。
2. Description of the Related Art Vinyl chloride resins are generally produced by a suspension polymerization method, and after separation from the slurry after polymerization, drying, etc., they are transported by air and stored or packed.

【0003】しかしながら、塩化ビニル系樹脂は、搬送
や袋詰の過程でそれ自体又は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樹脂
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。こ
のような樹脂の帯電による悪影響を低減する方法とし
て、従来、界面活性剤を塩化ビニル系樹脂に添加する方
法又はスチームを塩化ビニル系樹脂に吹込んで湿度を調
整する方法が知られている。
However, the vinyl chloride resin is charged with static electricity due to friction with itself or other substances during transport and bagging, and its fluidity is lowered, and its bulk specific gravity is higher than that of the vinyl chloride resin immediately after production. Since it decreases, it becomes extremely difficult to handle, and there is a problem that work is seriously hindered. Conventionally known methods for reducing the adverse effects of such resin charging are adding a surfactant to the vinyl chloride resin or blowing steam into the vinyl chloride resin to adjust the humidity.

【0004】[0004]

【発明が解決しようとする課題】しかし、従来の界面活
性剤を添加する方法においては、樹脂の帯電による嵩比
重の減少を十分に防止することができないばかりか、さ
らに樹脂の熱安定性、初期着色性等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に
おいては、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, in the conventional method of adding a surfactant, not only the decrease in bulk specific gravity due to the charging of the resin cannot be sufficiently prevented, but also the thermal stability and the initial temperature of the resin are improved. It has a drawback that it adversely affects the colorability and the like. In addition, the method of blowing steam has drawbacks such as an increase in required labor force and complication of equipment.

【0005】そこで、本発明の目的は、特定の化合物を
添加することにより、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樹脂
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 resin having good quality, which is less likely to cause a decrease in bulk specific gravity due to electrification by adding a specific compound. is there.

【0006】[0006]

【課題を解決するための手段】本発明者らは、上記課題
を解決するために鋭意検討した結果、特定の化合物を添
加することにより、塩化ビニル系樹脂の帯電による嵩比
重の減少が起こりにくく、しかも、良好な品質を有する
塩化ビニル系樹脂を製造する方法を見出し本発明を完成
させるに至った。
Means for Solving the Problems As a result of intensive studies for solving the above problems, the present inventors have found that addition of a specific compound makes it difficult for the vinyl chloride resin to be reduced in bulk specific gravity due to charging. Moreover, a method for producing a vinyl chloride resin having good quality has been found, and the present invention has been completed.

【0007】即ち、本発明は、塩化ビニル系単量体を水
性媒体中で懸濁重合し、塩化ビニル系樹脂を製造するに
際し、塩化ビニル系樹脂を含有するスラリー、該スラリ
ーを脱水した後に得られるケーキ状物又は該ケーキ状物
を乾燥して得られた樹脂粉体に、下記式(1)で示され
る化合物を前記塩化ビニル系樹脂100重量部に対して
0.001〜0.5重量部添加することを特徴とする塩
化ビニル系樹脂の製造方法を提供するものである。
That is, according to the present invention, when a vinyl chloride resin is suspension polymerized in an aqueous medium to produce a vinyl chloride resin, the vinyl chloride resin-containing slurry is obtained by dehydrating the slurry. 0.001 to 0.5 parts by weight of the compound represented by the following formula (1) in 100 parts by weight of the vinyl chloride resin described above is added to the obtained cake or the resin powder obtained by drying the cake. The present invention provides a method for producing a vinyl chloride-based resin, which is characterized by adding a part thereof.

【0008】[0008]

【化2】 Embedded image

【0009】(式中のR1、R2、R3は、それぞれ独
立していてもよい炭素数1〜20のアルキル基を示
す。) 以下に、本発明を詳細に説明する。
(In the formula, R1, R2 and R3 each independently represent an alkyl group having 1 to 20 carbon atoms.) The present invention is described in detail below.

【0010】本発明においては、塩化ビニル系樹脂は懸
濁重合方法により製造される。
In the present invention, the vinyl chloride resin is produced by the suspension polymerization method.

【0011】本発明における塩化ビニル系樹脂として
は、例えば塩化ビニル単独重合樹脂、塩化ビニル共重合
樹脂が挙げられる。
Examples of the vinyl chloride resin in the present invention include vinyl chloride homopolymer resin and vinyl chloride copolymer resin.

【0012】本発明において、塩化ビニル系樹脂を製造
するための塩化ビニル系単量体としては、塩化ビニル単
量体又は塩化ビニル単量体と塩化ビニル単量体と共重合
可能なビニル系単量体との混合物が挙げられる。そし
て、塩化ビニル単量体と共重合可能なビニル系単量体と
しては、例えば酢酸ビニル等のアルキルビニルエステ
ル;セチルビニルエーテル等のアルキルビニルエーテ
ル;エチレン、プロピレン等のオレフィン系単量体;ア
クリル酸メチル、アクリル酸エチル、アクリル酸プロピ
ル等のアクリル酸アルキルエステル;メタクリル酸メチ
ル、メタクリル酸エチル、メタクリル酸プロピル等のメ
タクリル酸アルキルエステルなどがが挙げられる。
In the present invention, the vinyl chloride-based monomer for producing the vinyl chloride-based resin is a vinyl-based monomer that can be copolymerized with a vinyl chloride monomer or a vinyl chloride monomer and a vinyl chloride monomer. Examples include a mixture with a monomer. Examples of vinyl monomers copolymerizable with vinyl chloride monomers include alkyl vinyl esters such as vinyl acetate; alkyl vinyl ethers such as cetyl vinyl ether; olefinic monomers such as ethylene and propylene; methyl acrylate. , Alkyl acrylates such as ethyl acrylate and propyl acrylate; and methacrylic acid alkyl esters such as methyl methacrylate, ethyl methacrylate and propyl methacrylate.

【0013】本発明における塩化ビニル系樹脂の懸濁重
合は、一般的に知られている方法を行ってもよく、例え
ば塩化ビニル系単量体を懸濁剤、重合開始剤の存在下、
水性媒体中で重合させる方法を挙げることができ、この
ような懸濁重合法により塩化ビニル系樹脂を含有するス
ラリーを得ることができる。
The suspension polymerization of the vinyl chloride resin in the present invention may be carried out by a generally known method, for example, in the presence of a vinyl chloride monomer in the presence of a suspending agent and a polymerization initiator.
A method of polymerizing in an aqueous medium can be mentioned, and a slurry containing a vinyl chloride resin can be obtained by such a suspension polymerization method.

【0014】本発明において、塩化ビニル系樹脂を含有
するスラリー、該スラリーを脱水した後に得られるケー
キ状物又は該ケーキ状物を乾燥して得られた樹脂粉体に
添加する式(1)で示される化合物は、R1、R2、R
3は、それぞれ独立していてもよい炭素数1〜20のア
ルキル基よりなり、式(1)で示されるかぎりいかなる
化合物も使用することができる。そして、より効率的に
帯電による嵩比重の低下を防止することが可能となるこ
とからR1、R2、R3で示されるアルキル基のうち少
なくとも1つは炭素数8〜18のアルキル基を有するも
のがより好ましい。
In the present invention, a slurry containing a vinyl chloride resin, a cake obtained by dehydrating the slurry or a resin powder obtained by drying the cake is added by the formula (1). The compounds shown are R1, R2, R
3 are each independently an alkyl group having 1 to 20 carbon atoms, and any compound can be used as long as it is represented by the formula (1). Since it is possible to more effectively prevent the decrease in bulk specific gravity due to charging, at least one of the alkyl groups represented by R1, R2, and R3 has an alkyl group having 8 to 18 carbon atoms. More preferable.

【0015】本発明における式(1)で示される化合物
としては、例えばデシルジメチルカルボキシメチルベタ
イン、ドデシルジメチルカルボキシメチルベタイン、テ
トラデシルジメチルカルボキメチルシベタイン、ヘキサ
デシルジメチルカルボキシメチルベタイン、オクタデシ
ルジメチルカルボキメチルベタイン等を挙げることがで
きる。
Examples of the compound represented by the formula (1) in the present invention include decyldimethylcarboxymethylbetaine, dodecyldimethylcarboxymethylbetaine, tetradecyldimethylcarboxymethylcybetaine, hexadecyldimethylcarboxymethylbetaine, octadecyldimethylcarboxymethylbetaine. Etc. can be mentioned.

【0016】本発明における式(1)で示される化合物
の添加量は、塩化ビニル系樹脂100重量部に対して
0.001〜0.5重量部添加である。その添加量が
0.001重量部未満である場合、得られる塩化ビニル
系樹脂の帯電によるかさ比重の極端な低下を防止できな
い。また、添加量が0.5重量部を超えても目的とする
効果はそれ以上高まらないので経済的でない。
The addition amount of the compound represented by the formula (1) in the present invention is 0.001 to 0.5 parts by weight based on 100 parts by weight of the vinyl chloride resin. If the addition amount is less than 0.001 part by weight, it is impossible to prevent the bulk specific gravity from being extremely reduced due to the electrification of the obtained vinyl chloride resin. Further, even if the amount added exceeds 0.5 parts by weight, the desired effect does not increase any more, which is not economical.

【0017】本発明における式(1)で示される化合物
の添加方法は、塩化ビニル系樹脂を含有するスラリー、
該スラリーを脱水した後に得られるケーキ状物又は該ケ
ーキ状物を乾燥して得られた樹脂粉体に添加することが
可能であれば、いかなる方法を用いてもよく、粉体、溶
液、分散液等の状態で添加することが可能であり、容易
に均一に添加できることから、溶液又は分散液で添加す
ることが好ましい。そして、式(1)で示される化合物
の溶液又は分散液を調製するための溶媒としては、とく
に限定されないが、例えば水、メタノール、エタノー
ル、イソプロピルアルコール、アセトン又はその混合溶
媒が挙げられる。
The method of adding the compound represented by the formula (1) in the present invention is a slurry containing a vinyl chloride resin,
Any method may be used as long as it can be added to the cake obtained after dehydrating the slurry or the resin powder obtained by drying the cake, powder, solution or dispersion. Since it can be added in a liquid state or the like and can be easily and uniformly added, it is preferable to add it in the form of a solution or dispersion. The solvent for preparing the solution or dispersion of the compound represented by the formula (1) is not particularly limited, but examples thereof include water, methanol, ethanol, isopropyl alcohol, acetone, or a mixed solvent thereof.

【0018】[0018]

【実施例】以下、本発明を実施例により詳細に説明する
が、本発明はこれらに限定されるものではない。
The present invention will be described below in more detail with reference to examples, but the present invention is not limited to these examples.

【0019】実施例及び比較例で得られた樹脂につい
て、下記に示す条件において評価を行った。
The resins obtained in Examples and Comparative Examples were evaluated under the conditions shown below.

【0020】〜かさ比重測定試験〜 得られた樹脂を温度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 6
721の方法により測定した。
-Bulk Specific Gravity Measurement Test- The obtained resin is left in a constant temperature and humidity chamber at a temperature of 23 ° C. and a relative humidity of 50% for 48 hours, and then the bulk specific gravity is measured according to JIS K 6
It was measured by the method of 721.

【0021】また、上記と同様の条件で48時間放置し
た樹脂を、ブラベンダープラネタリーミキサーで60r
pm、2分間撹拌後、上記と同じ方法でかさ比重を求
め、それらを比較することにより帯電防止性を評価し
た。
The resin left for 48 hours under the same conditions as above was treated with a Brabender planetary mixer at 60r.
After stirring for 2 minutes at pm, bulk specific gravity was determined by the same method as above, and the antistatic properties were evaluated by comparing them.

【0022】〜熱安定性〜 得られた樹脂100重量部に対して、 三塩基性硫酸鉛 1. 0部 ステアリン酸鉛 1. 5部 ステアリン酸カルシウム 0. 5部 を配合し、190℃のロール加工機で、5分間混練した
後、厚さ1mmのシートを作製し、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。
-Heat Stability- 100 parts by weight of the obtained resin was mixed with 1.0 part of tribasic lead sulfate, 1.5 parts of lead stearate and 0.5 part of calcium stearate, and rolled at 190 ° C. After kneading with a machine for 5 minutes, a sheet with a thickness of 1 mm is prepared, and this sheet is
It was placed in an oven at ℃ and the time until blackening was measured.

【0023】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、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樹脂ケーキを得た。こ
うして得られた樹脂ケーキに、塩化ビニル樹脂100重
量部に対しオクタメチルジメチルカルボキシメチルベタ
インの添加量が0.01重量部となるようにオクタメチ
ルジメチルカルボキシメチルベタインの1%水溶液を添
加した後、70℃で2時間流動乾燥し塩化ビニル樹脂を
得た。
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, 0.04 part by weight of 2-ethylhexyl peroxydicarbonate were placed in a stainless steel polymerization vessel. Was charged, polymerization was carried out at a temperature of 57 ° C., and when the pressure in the polymerization vessel reached 6.0 kg / cm 2 G, unreacted vinyl chloride monomer was recovered and dehydrated to contain 20% by weight of water. A vinyl chloride resin cake was obtained. After adding a 1% aqueous solution of octamethyldimethylcarboxymethyl betaine to the resin cake thus obtained so that the addition amount of octamethyldimethylcarboxymethyl betaine is 0.01 parts by weight with respect to 100 parts by weight of vinyl chloride resin, It was fluidized and dried at 70 ° C. for 2 hours to obtain a vinyl chloride resin.

【0024】得られた塩化ビニル樹脂の評価結果を表1
に示す。
Table 1 shows the evaluation results of the obtained vinyl chloride resin.
Shown in

【0025】得られた塩化ビニル樹脂は、優れた帯電防
止性を有し、熱的安定性の低下のないものであった。
The obtained vinyl chloride resin had an excellent antistatic property and did not deteriorate in thermal stability.

【0026】実施例2〜5 オクタメチルジメチルカルボキシメチルベタインの添加
量、添加条件を表1に示す条件とした以外は、実施例1
と同様にして塩化ビニル樹脂を得た。
Examples 2 to 5 Example 1 was repeated except that the addition amount and addition conditions of octamethyldimethylcarboxymethyl betaine were changed to those shown in Table 1.
A vinyl chloride resin was obtained in the same manner as in.

【0027】得られた塩化ビニル樹脂の評価結果を表1
に示す。
Table 1 shows the evaluation results of the obtained vinyl chloride resin.
Shown in

【0028】得られた塩化ビニル樹脂は、優れた帯電防
止性を有し、熱的安定性の低下のないものであった。
The obtained vinyl chloride resin had an excellent antistatic property and did not deteriorate in thermal stability.

【0029】比較例1 オクタメチルジメチルカルボキシメチルベタインを添加
しない以外は、実施例1と同様にして塩化ビニル樹脂を
得た。
Comparative Example 1 A vinyl chloride resin was obtained in the same manner as in Example 1 except that octamethyldimethylcarboxymethyl betaine was not added.

【0030】得られた塩化ビニル樹脂の評価結果を表1
に示す。
Table 1 shows the evaluation results of the obtained vinyl chloride resin.
Shown in

【0031】得られた塩化ビニル樹脂は、帯電防止性に
劣るものであった。
The obtained vinyl chloride resin was inferior in antistatic property.

【0032】[0032]

【表1】 [Table 1]

【0033】[0033]

【発明の効果】本発明は、帯電による嵩比重の減少が起
こりにくく、良好な熱安定性を有する塩化ビニル系樹脂
の製造方法に関するものであり、その工業的価値は高い
ものである。
INDUSTRIAL APPLICABILITY The present invention relates to a method for producing a vinyl chloride resin having good thermal stability, which is unlikely to cause a decrease in bulk specific gravity due to charging, and has a high industrial value.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】塩化ビニル単量体又は塩化ビニル単量体を
主成分とするビニル系単量体の混合物(以下、塩化ビニ
ル系単量体という。)を水性媒体中で懸濁重合し、塩化
ビニル系樹脂を製造するに際し、塩化ビニル系樹脂を含
有するスラリー、該スラリーを脱水した後に得られるケ
ーキ状物又は該ケーキ状物を乾燥して得られた樹脂粉体
に、下記式(1)で示される化合物を前記塩化ビニル系
樹脂100重量部に対して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樹脂の製造方法。 【化1】 (式中のR1、R2、R3は、それぞれ独立していても
よい炭素数1〜20のアルキル基を示す。)
1. A suspension-polymerization of a vinyl chloride monomer or a mixture of vinyl-based monomers having vinyl chloride monomer as a main component (hereinafter referred to as vinyl chloride-based monomer) in an aqueous medium, In producing a vinyl chloride resin, a slurry containing the vinyl chloride resin, a cake obtained after dehydrating the slurry, or a resin powder obtained by drying the cake is added with the following formula (1 ) 0.001 to 0.5 part by weight of the compound represented by the formula (1) is added to 100 parts by weight of the vinyl chloride resin, and a method for producing a vinyl chloride resin. Embedded image (In the formula, R1, R2, and R3 each independently represent an alkyl group having 1 to 20 carbon atoms.)
JP7340796A 1995-12-27 1995-12-27 Production of vinyl chloride resin Pending JPH09176231A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7340796A JPH09176231A (en) 1995-12-27 1995-12-27 Production of vinyl chloride resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7340796A JPH09176231A (en) 1995-12-27 1995-12-27 Production of vinyl chloride resin

Publications (1)

Publication Number Publication Date
JPH09176231A true JPH09176231A (en) 1997-07-08

Family

ID=18340375

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7340796A Pending JPH09176231A (en) 1995-12-27 1995-12-27 Production of vinyl chloride resin

Country Status (1)

Country Link
JP (1) JPH09176231A (en)

Similar Documents

Publication Publication Date Title
US5478900A (en) Process for preparing vinyl chloride polymer of quality
JPH06184217A (en) Production of vinyl chloride-based polymer
EP0177956B1 (en) Low molecular weight vinyl halide/vinyl ester copolymers by aqueous polymerization
JPH09176231A (en) Production of vinyl chloride resin
JPH09176423A (en) Production of vinyl chloride polymer
JPH09176419A (en) Production of polyvinyl chloride resin
JPH09176422A (en) Production of vinyl chloride resin
EP0601586B1 (en) Method of producing vinyl chloride type polymer
JPH09176418A (en) Production of polyvinyl chloride resin
JPH09176232A (en) Production of vinyl chloride polymer
JP3316891B2 (en) Method for producing vinyl chloride polymer
JPH09176421A (en) Production of vinyl chloride polymer
JPH06184218A (en) Production of vinyl chloride-based polymer
JP2003238606A (en) Method for producing vinyl chloride resin
JPH09194509A (en) Production of vinyl chloride polymer having high powder fluidity
JPH06184220A (en) Production of vinyl chloride-based polymer
JP3316890B2 (en) Method for producing vinyl chloride polymer
JPH09194530A (en) Production of vinyl chloride-based polymer having good powder flowability
JPH06179714A (en) Production of vinyl chloride polymer
JPH0827206A (en) Manufacture of vinyl chloride polymer
JPH06179715A (en) Production of vinyl chloride polymer
JPH10212306A (en) Production of vinyl chloride polymer
JP2912955B2 (en) Suspension polymerization of vinyl chloride
JPH09194508A (en) Production of vinyl chloride polymer having excellent powder fluidity
JPH06184219A (en) Production of vinyl chloride-based polymer

Legal Events

Date Code Title Description
A977 Report on retrieval

Effective date: 20041008

Free format text: JAPANESE INTERMEDIATE CODE: A971007

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20041019

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20050304