JPS6012327B2 - Processing method for vinyl chloride polymer slurry - Google Patents

Processing method for vinyl chloride polymer slurry

Info

Publication number
JPS6012327B2
JPS6012327B2 JP2012376A JP2012376A JPS6012327B2 JP S6012327 B2 JPS6012327 B2 JP S6012327B2 JP 2012376 A JP2012376 A JP 2012376A JP 2012376 A JP2012376 A JP 2012376A JP S6012327 B2 JPS6012327 B2 JP S6012327B2
Authority
JP
Japan
Prior art keywords
vinyl chloride
slurry
chloride polymer
polymer slurry
processing method
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.)
Expired
Application number
JP2012376A
Other languages
Japanese (ja)
Other versions
JPS52105106A (en
Inventor
允 合田
寿男 船田
三郎 吉岡
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.)
Toagosei Co Ltd
Original Assignee
Toagosei Co Ltd
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 Toagosei Co Ltd filed Critical Toagosei Co Ltd
Priority to JP2012376A priority Critical patent/JPS6012327B2/en
Publication of JPS52105106A publication Critical patent/JPS52105106A/en
Publication of JPS6012327B2 publication Critical patent/JPS6012327B2/en
Expired legal-status Critical Current

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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】 本発明は、懸濁重合によって得た塩化ビニル重合体スラ
リーの未反応単量体を分離回収する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for separating and recovering unreacted monomers from a vinyl chloride polymer slurry obtained by suspension polymerization.

懸濁重合法により製造された塩化ビニル重合体は多孔質
の粒状物質であるため、その微細孔中に禾反応単豊体を
吸着残存しており、通常重合直後において数千脚を含有
している。
Vinyl chloride polymers produced by the suspension polymerization method are porous granular materials, so they retain adsorbed monopolymers in their micropores, and usually contain several thousand legs immediately after polymerization. There is.

そしてか)る塩化ビニル重合体のスラリーは一般には遠
心分離機により脱水し、通風乾燥器に供給し、脱水乾燥
して製品とするが、この方法によれば乾燥排ガス中に多
量の単量体が同伴され、作業環境を著しく悪化するのみ
ならず製品の歩蟹りを低下させている。
The vinyl chloride polymer slurry is generally dehydrated using a centrifugal separator, supplied to a ventilation dryer, and dehydrated and dried to produce a product, but according to this method, a large amount of monomer is This not only significantly worsens the working environment but also reduces the quality of the product.

一方重合後のスラリー中に含有されている単量体を有効
に回収することは、作業環境の改善に有効であるのみな
らず、製品歩蟹りの向上等の優れた利益が得られ、これ
については種々検討されているが未だ技術的に満足出来
るものは見当らない。
On the other hand, effectively recovering the monomers contained in the slurry after polymerization is not only effective in improving the working environment, but also provides excellent benefits such as improving product quality. Various studies have been made regarding this, but nothing that is technically satisfactory has yet been found.

例えば遠心脱水後の含水スラリーを回転翼を有する乾燥
器中で強制加熱し、含有する単量体を造出す方法が採用
されているが、回転部分のシール機構より空気の侵入す
るおそれがあり、又単量体の回収にも問題がある。
For example, a method has been adopted in which a water-containing slurry after centrifugal dehydration is forcibly heated in a dryer with rotary blades to produce the monomer contained therein, but there is a risk of air entering through the seal mechanism of the rotating part. There are also problems with monomer recovery.

本発明者等は、重合体中の単量体を効果的に排除すると
共に、これを有利に回収することについて検討した結果
、本発明方法を完成するに至った。
The present inventors studied how to effectively eliminate monomers in polymers and to recover them advantageously, and as a result, they completed the method of the present invention.

即ち本発明は、懸濁重合によって得た塩化ピニル重合体
スラリ−を満液型の棚段塔内において直接スチームと接
触させてスラリ−中の禾反応単量体を分離回収すること
を特徴とする塩化ビニル重合体スラリーの処理方法であ
る。
That is, the present invention is characterized in that a pinyl chloride polymer slurry obtained by suspension polymerization is brought into direct contact with steam in a flooded tray column to separate and recover the reactive monomers in the slurry. This is a method for treating vinyl chloride polymer slurry.

本発明方法を図面を引用して説明すれば次の通りである
The method of the present invention will be explained as follows with reference to the drawings.

第1図において、懸濁重合により得られた処理せんとす
るスラリーはタンク1よりポンプ2を経て棚段塔3へ供
V給される。
In FIG. 1, a slurry to be treated obtained by suspension polymerization is supplied from a tank 1 to a plate column 3 via a pump 2.

棚段※は内部に多孔板等によりなる仕切り板を設けてあ
り、塔下部より配管4によってスチームを吹込む。塔内
はェジェクター6により減圧に保持されて、スラリーか
ら発散した単量体はコンデンサー5を経て、分離器7に
至り、配管8より回収される。
The shelves* are equipped with partition plates made of perforated plates, etc., and steam is blown into them through piping 4 from the bottom of the tower. The inside of the column is maintained at reduced pressure by an ejector 6, and the monomer emitted from the slurry passes through a condenser 5, reaches a separator 7, and is recovered through a pipe 8.

スラリーは落下部より配管9を経て遠心分離器(図示せ
ず)に送られる。本発明方法の対象となる塩化ピニル重
合体スラリーにおいて、その中の残留単量体は通常一部
が重合体に吸着され、他は水中に溶解している。
The slurry is sent from the falling part to a centrifugal separator (not shown) via piping 9. In the pinyl chloride polymer slurry that is the subject of the method of the present invention, some of the residual monomers therein are usually adsorbed onto the polymer and the rest are dissolved in water.

従ってこれらの単量体を回収するためには、スラリーを
好ましくは常圧乃至減圧、特に望ましくは減圧下で直接
スチームで加熱し、液温を可能な限り高温且つ長時間保
持することを要する。か)る温度保持は好ましくは80
〜100qo、特に90〜100午○の範囲が望ましく
、処理時間は10〜30分、特に10〜15分程度が望
ましい。
Therefore, in order to recover these monomers, it is necessary to heat the slurry directly with steam, preferably at normal pressure to reduced pressure, particularly preferably under reduced pressure, and to maintain the liquid temperature as high as possible for a long time. The temperature is preferably maintained at 80°C.
~100 qo, particularly preferably from 90 to 100 pm, and the treatment time is preferably from 10 to 30 minutes, particularly from 10 to 15 minutes.

過度の高温や長時間処理は重合体の品質に変化をもたら
すおそれがあり、又低温や短時間に過ぎるときは、充分
な処理効果が期待出釆ない。本発明方法に使用する満液
型の棚段塔とは、内部に1段又は2段以上の棚板を設け
た塔で、系内の液をバックミキシングのない状態で充満
しつ)処理することの出来る装置であり、本発明方法に
おいては棚の段数は1段若しくは2段以上任意に設ける
ことが出来るが、一般には段数の多い程単島体除去の効
果が向上する。
Excessively high temperature or long-time treatment may cause a change in the quality of the polymer, and low temperature or too short treatment time may not produce sufficient treatment effects. The liquid-filled plate column used in the method of the present invention is a column that is equipped with one or more shelves inside, and is filled with the liquid in the system without back-mixing. In the method of the present invention, the number of shelves can be arbitrarily set to one or more than two, but generally the greater the number of shelves, the better the effect of single island removal.

又本発明方法において、バックミキシングを防止しつ)
処理することは、完全混合系などの手段によるよりも著
しく単量体の除去効果を高めることが出来、たとえば完
全混合系において、仕込スラリーの系内平均滞留時間5
分後におけるモノマー残存率((処理後単量体濃度/単
量体初濃度)×100であらわす)23%の操業条件で
これをピストンフローに変えると、モノマー残存率は理
論上3%に減少することが出来る。
In addition, in the method of the present invention, back mixing can be prevented.
Treatment can significantly enhance the monomer removal effect compared to methods such as a complete mixing system. For example, in a complete mixing system, the average residence time of the charged slurry in the system is 5.
If the operating conditions are changed to piston flow at a monomer residual rate of 23% (expressed as (monomer concentration after treatment/initial monomer concentration) x 100) after 10 minutes, the monomer residual rate will theoretically decrease to 3%. You can.

又スチームはジャケット等による外部加熱に比して直接
スラリーに接触させることにより、熱効率及び濃伴効果
等の点で有利である。
In addition, steam is advantageous in terms of thermal efficiency, concentration effect, etc. by bringing it into direct contact with the slurry, compared to external heating using a jacket or the like.

以上の通り本発明方法は、簡単な処理設備によって未反
応単量体を効率よく分離回収出来るものであり、作業環
境の汚染など、安全衛生上の障害も充分回避出来る点で
利用価値の高い発明である。
As described above, the method of the present invention can efficiently separate and recover unreacted monomers using simple processing equipment, and it is an invention with high utility value in that it can sufficiently avoid health and safety hazards such as contamination of the working environment. It is.

.以上実施例を掲げて本発明を説明する。 .. The present invention will be described with reference to Examples above.

実施例 1〜9 懸濁重合法で得た塩化ビニル重合体スラリーを第1図に
示す装置を使用して種々な条件で処理した。
Examples 1 to 9 Vinyl chloride polymer slurries obtained by suspension polymerization were treated under various conditions using the apparatus shown in FIG.

その結果を後記第1表に示す。比較例 1および2 実施例1の棚段塔の各棚段上部よりスラリ−を分割散布
し、非満俵型とする以外は実施例1と同様に処理した結
果を第1表に併記する。
The results are shown in Table 1 below. Comparative Examples 1 and 2 Table 1 also shows the results of processing in the same manner as in Example 1, except that the slurry was spread in portions from the upper part of each tray of the tray column in Example 1 to form a non-full bale shape.

第1表 (註)1 スラリー濃度は35&/100ム2 棚板数
5枚は9枚の棚から1枚すきに取はずし5枚とした。
Table 1 (Note) 1 Slurry concentration was 35mm2.The number of shelves was 5 by removing one from each of the 9 shelves.

段間隔約600物。棚板数1枚は最上段の棚のみを残し
他を撤去した。
Approximately 600 rows apart. As for the number of shelves, only the top shelf was left and the others were removed.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の処理方法を説明する工程略図である。 1…・・・タンク、2・・・・・・ポンプ、3・・・…
棚段落、5……コンデンサー、6……ヱジエクタ−、7
…・・・分離器。第1図
FIG. 1 is a process diagram illustrating the treatment method of the present invention. 1...Tank, 2...Pump, 3...
Shelf row, 5...Condenser, 6...Ejector, 7
...Separator. Figure 1

Claims (1)

【特許請求の範囲】[Claims] 1 懸濁重合によって得た塩化ビニル重合体スラリーを
満液型の棚段塔内において直接スチームと接触させてス
ラリー中の未反応単量体を分離回収することを特徴とす
る塩化ビニル重合体スラリーの処理方法。
1. A vinyl chloride polymer slurry obtained by suspension polymerization, which is characterized in that the unreacted monomers in the slurry are separated and recovered by directly contacting the vinyl chloride polymer slurry with steam in a flooded tray column. processing method.
JP2012376A 1976-02-27 1976-02-27 Processing method for vinyl chloride polymer slurry Expired JPS6012327B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2012376A JPS6012327B2 (en) 1976-02-27 1976-02-27 Processing method for vinyl chloride polymer slurry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2012376A JPS6012327B2 (en) 1976-02-27 1976-02-27 Processing method for vinyl chloride polymer slurry

Publications (2)

Publication Number Publication Date
JPS52105106A JPS52105106A (en) 1977-09-03
JPS6012327B2 true JPS6012327B2 (en) 1985-04-01

Family

ID=12018334

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2012376A Expired JPS6012327B2 (en) 1976-02-27 1976-02-27 Processing method for vinyl chloride polymer slurry

Country Status (1)

Country Link
JP (1) JPS6012327B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4130527A (en) * 1977-12-29 1978-12-19 Stauffer Chemical Company Method of treating a polymer latex to remove unreacted monomer by treatment in a column

Also Published As

Publication number Publication date
JPS52105106A (en) 1977-09-03

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