JPH0749485B2 - Post-treatment method for polyarylene sulfide polymer suspension and apparatus therefor - Google Patents

Post-treatment method for polyarylene sulfide polymer suspension and apparatus therefor

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Publication number
JPH0749485B2
JPH0749485B2 JP62188950A JP18895087A JPH0749485B2 JP H0749485 B2 JPH0749485 B2 JP H0749485B2 JP 62188950 A JP62188950 A JP 62188950A JP 18895087 A JP18895087 A JP 18895087A JP H0749485 B2 JPH0749485 B2 JP H0749485B2
Authority
JP
Japan
Prior art keywords
post
polyarylene sulfide
sieve
polymer suspension
suspension
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 - Lifetime
Application number
JP62188950A
Other languages
Japanese (ja)
Other versions
JPS6433136A (en
Inventor
大吾 城田
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.)
Idemitsu Petrochemical Co Ltd
Original Assignee
Idemitsu Petrochemical Co Ltd
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Filing date
Publication date
Application filed by Idemitsu Petrochemical Co Ltd filed Critical Idemitsu Petrochemical Co Ltd
Priority to JP62188950A priority Critical patent/JPH0749485B2/en
Publication of JPS6433136A publication Critical patent/JPS6433136A/en
Publication of JPH0749485B2 publication Critical patent/JPH0749485B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はポリアリーレンスルフィド重合体懸濁物の後処
理方法及びその装置に関し、詳しくは重合反応によって
得られたポリアリーレンスルフィド重合体懸濁物を、一
つの後処理装置内で分離,洗浄,乾燥の一連の後処理を
効率よく行うことのできる方法ならびにこの方法を行う
に適した装置に関する。
TECHNICAL FIELD The present invention relates to a method for post-treatment of a polyarylene sulfide polymer suspension and an apparatus therefor, and more specifically, a polyarylene sulfide polymer suspension obtained by a polymerization reaction. The present invention relates to a method capable of efficiently performing a series of post-treatments of separation, washing, and drying in one post-treatment apparatus, and an apparatus suitable for performing this method.

〔従来の技術及び発明が解決しようとする問題点〕[Problems to be Solved by Prior Art and Invention]

従来から、ポリフェニレンスルフィド(PPS)をはじめ
とするポリアリーレンスルフィドは、重合反応終了後、
得られる重合体懸濁物を分離,洗浄,乾燥という一連の
後処理工程にかけて製造されているが、この際に行う後
処理の方法としては、所謂溶剤フラッシュ法(米国特許
法第3,956,000号明細書)や篩分け法(特開昭61−255,9
33号公報)などが知られている。しかし、これらの方法
はいずれも重合体スラリー移送時に閉塞等のトラブルが
生じやすく、また処理操作にあたってスラリー貯槽以外
にフラッシュタンク,振動篩,移送ポンプ等の設備が必
要であるなどの様々な問題をかかえている。特に、フラ
ッシュ法ではオリゴマー等の固形不純物を除去すること
ができず、一方、篩分け法では特に湿分の除去率が悪
く、大きな仕上用乾燥機を用いる必要があるなどの問題
がある。
Conventionally, polyarylene sulfides such as polyphenylene sulfide (PPS) are
The polymer suspension obtained is manufactured through a series of post-treatment steps of separation, washing, and drying. The post-treatment carried out at this time is the so-called solvent flash method (US Pat. No. 3,956,000). ) And sieving method (JP-A-61-255,9
No. 33) is known. However, all of these methods are prone to problems such as clogging when transferring the polymer slurry, and require various equipment such as a flash tank, a vibrating screen, and a transfer pump in addition to the slurry storage tank for the processing operation. I have it. In particular, the flash method cannot remove solid impurities such as oligomers, while the sieving method has a problem that the removal rate of moisture is particularly poor, and a large finishing dryer is required.

さらに、前述した後処理の方法として、反応槽内蒸発法
(特開昭61−136,523号公報)なるものも知られている
が、この方法は、溶剤を蒸発させる間、反応器内で反応
を行うことができないため、バッチサイクルが長くな
り、結果的に生産性が低下し、しかもオリゴマー等の固
形不純物の除去もできず、その上、反応と蒸発・乾燥の
両方に適した攪拌翼やバッフル等がないため、処理効果
が不充分であるなど様々な問題がある。
Further, as the above-mentioned post-treatment method, there is also known an in-reaction tank evaporation method (Japanese Patent Laid-Open No. 61-136,523). However, in this method, the reaction is carried out in the reactor while the solvent is evaporated. Since it can not be performed, the batch cycle becomes long, the productivity is reduced as a result, solid impurities such as oligomers cannot be removed, and moreover, a stirring blade and a baffle suitable for both reaction and evaporation / drying Therefore, there are various problems such as insufficient treatment effect.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者は、上記従来技術の問題点を解消し、特にポリ
アリーレンスルフィド重合体のスラリー移送時の閉塞ト
ラブルを防止するとともに、バッチスラリー重合の冗長
な後処理操作に伴う生産性の低下と設備費の増大を抑制
して、極めて効率のよい後処理方法を開発すべく鋭意研
究を重ねた。
The present inventor has solved the above-mentioned problems of the prior art, in particular, while preventing clogging trouble during the transfer of slurry of polyarylene sulfide polymer, a decrease in productivity and equipment accompanying redundant post-treatment operation of batch slurry polymerization. We have conducted intensive research to develop an extremely efficient post-treatment method while suppressing an increase in cost.

その結果、重合反応によって得られるポリアリーレンス
ルフィド重合体の懸濁分を後処理する際に、工夫された
一つの処理装置内で分離,洗浄,乾燥の一連の処理を行
うことにより、所期の目的を達成しうることを見出し、
本発明を完成するに至った。
As a result, when the suspension of the polyarylene sulfide polymer obtained by the polymerization reaction is post-treated, a series of treatments of separation, washing, and drying are carried out in one devised treatment device, and Find that you can achieve your goals,
The present invention has been completed.

すなわち本発明は、重合反応終了後に得られるポリアリ
ーレンスルフィド重合体懸濁物の後処理を行うにあた
り、該重合体懸濁物を、下部に篩を具備した排出口を有
すると共に内部に攪拌機構を有する後処理装置に導入し
て篩分により排液し、次いで該装置内の残留物に溶剤を
加えて攪拌洗浄後、篩分により排液し、続いて該装置内
の残留物に水を加えて攪拌洗浄後、篩分により排液し、
しかる後に該装置を減圧下で加熱して該装置内の残留物
を減圧乾燥することを特徴とするポリアリーレンスルフ
ィド重合体懸濁物の後処理方法を提供すると共に、ポリ
アリーレンスルフィド重合体懸濁物の後処理装置におい
て、逆円錐状底部を有する筒状容器本体、該本体に取付
けられた加熱機構、該本体内に設置された攪拌機構、該
本体上部に設けられた重合体懸濁物および洗浄液の供給
口、ならびに該本体の逆円錐状底部側面に設けられた篩
を具備した排出口からなることを特徴とするポリアリー
レンスルフィド重合体懸濁物の後処理装置をも提供する
ものである。
That is, in the present invention, in the post-treatment of the polyarylene sulfide polymer suspension obtained after the completion of the polymerization reaction, the polymer suspension is provided with an outlet equipped with a sieve at the bottom and a stirring mechanism inside. It is introduced into a post-treatment device that has it and drained by a sieve, then a solvent is added to the residue in the device and washed by stirring, and then drained by a sieve, and then water is added to the residue in the device. After stirring and washing, drain with a sieve,
Then, the apparatus is heated under reduced pressure and the residue in the apparatus is dried under reduced pressure to provide a post-treatment method for a polyarylene sulfide polymer suspension, and a polyarylene sulfide polymer suspension. In a post-processing apparatus for articles, a cylindrical container body having an inverted conical bottom portion, a heating mechanism attached to the body, a stirring mechanism installed in the body, a polymer suspension provided on the upper portion of the body, and The present invention also provides a post-treatment device for a suspension of a polyarylene sulfide polymer, which is characterized by comprising a supply port for a cleaning liquid and an outlet provided with a sieve provided on a side surface of an inverted conical bottom of the main body. .

本発明の後処理方法は、重合反応によって得られるポリ
アリーレンスルフィド重合体懸濁物を対象とするが、こ
のポリアリーレンスルフィド重合体懸濁物は通常の重合
反応によって得られるものである。例えばp−ジクロロ
ベンゼン等のジハロゲン化芳香族化合物と硫化ナトリウ
ム,硫化リチウム等のアルカリ金属硫化物をN−メチル
−2−ピロリドン(NMP)やヘキサメチルリン酸アミド
(HMPA)等の極性溶媒中で重縮合させることにより、ポ
リフェニレンスルフィド(PPS)をはじめとするポリア
リーレンスルフィドの重合体懸濁物が得られる。
The post-treatment method of the present invention is intended for a polyarylene sulfide polymer suspension obtained by a polymerization reaction, and this polyarylene sulfide polymer suspension is obtained by an ordinary polymerization reaction. For example, dihalogenated aromatic compounds such as p-dichlorobenzene and alkali metal sulfides such as sodium sulfide and lithium sulfide in a polar solvent such as N-methyl-2-pyrrolidone (NMP) and hexamethylphosphoramide (HMPA). By polycondensation, a polymer suspension of polyarylene sulfide including polyphenylene sulfide (PPS) is obtained.

本発明の後処理方法は、このようにして得られるポリア
リーレンスルフィド重合体懸濁物を、分離,洗浄および
乾燥処理の行える後処理装置内に導入して所定の処理を
順次行えばよい。この後処理装置としては各種の態様が
考えられるが、上述した本発明の後処理装置が好まし
い。本発明の後処理装置の一例を第1図に示すが、この
第1図に基いて本発明の方法及び装置を説明すれば以下
のとおりである。
In the post-treatment method of the present invention, the thus-obtained polyarylene sulfide polymer suspension may be introduced into a post-treatment device capable of separation, washing and drying treatments, and predetermined treatments may be sequentially performed. Although various modes are conceivable as this post-processing apparatus, the above-mentioned post-processing apparatus of the present invention is preferable. An example of the post-processing apparatus of the present invention is shown in FIG. 1, and the method and apparatus of the present invention will be described based on FIG. 1 as follows.

まず、重合反応槽(図示せず)で得られたポリアリーレ
ンスルフィド重合体懸濁物を該反応槽から抜き出して、
これを筒状容器本体1の上部に設けられた重合体懸濁物
供給口3から、該容器本体1内に供給する。なお、この
重合体懸濁物は、ポリアリーレンスルフィド重合体,NMP
等の重合体の溶媒および副生物(オリゴマー,塩化ナト
リウム等)からなるものである。また、この容器本体1
は底部2が逆円錐状となっているとともに、逆円錐状底
部2の側面には篩4を具備した排出口5が設けられてい
る。
First, the polyarylene sulfide polymer suspension obtained in a polymerization reaction tank (not shown) is extracted from the reaction tank,
This is supplied into the container body 1 from the polymer suspension supply port 3 provided in the upper portion of the cylindrical container body 1. In addition, this polymer suspension is a polyarylene sulfide polymer, NMP
And a by-product (oligomer, sodium chloride, etc.) of the polymer such as. Also, this container body 1
The bottom part 2 has an inverted conical shape, and a discharge port 5 having a sieve 4 is provided on the side surface of the inverted conical bottom part 2.

筒状容器本体1に供給された重合体懸濁物は、上記の篩
4付きの排出口5で篩分しながら排液され、重合用溶媒
と副生物の大部分が除去されて、容器本体1内にはポリ
アリーレンスルフィド重合体と少量の重合用溶媒ならび
に副生物が残留する。ここで、篩4付き排出口5は、容
器本体1の下部であれば様々な位置に設置でき、本体1
の最下端でもよいが、通常は逆円錐状底部2の側面位置
に設置することが好ましい。また、この排出口5には弁
7を取付け開閉自在としておく。なお、逆円錐状底部2
の最下端位置には後処理を経て最終的に得られる乾燥重
合体の抜出口6を設けておくことが好ましい。
The polymer suspension supplied to the cylindrical container body 1 is drained while being sifted through the discharge port 5 with the above-mentioned sieve 4, and most of the polymerization solvent and by-products are removed, and the container body is A polyarylene sulfide polymer, a small amount of a solvent for polymerization, and a by-product remain in 1. Here, the discharge port 5 with the sieve 4 can be installed in various positions as long as it is below the container body 1.
Although it may be the lowermost end, it is usually preferable to install it at the side surface position of the inverted conical bottom portion 2. A valve 7 is attached to the discharge port 5 so that it can be opened and closed. The inverted conical bottom 2
It is preferable to provide an outlet 6 for the dried polymer finally obtained after the post-treatment at the lowermost position.

次に容器本体1内の残留物に、本体1上部の洗浄液供給
口8から溶剤、好ましくは水と相溶性のある溶剤(NMP,
HMPA,アセトン,メタノールなど)を加え、これを本体
1内に設置された攪拌機構9、例えば攪拌翼などで充分
に攪拌して洗浄し、その後篩4付き排出口5から篩分排
液する。続いて、溶剤の代わりに水を、洗浄液供給口8
から容器本体1内の残留物に加えて、以下同様に充分攪
拌洗浄し、さらに排出口5から篩分排液する。なお、こ
こで洗浄液供給口8は、前述した重合体懸濁物供給口3
で代用(兼用)してもよいが、通常は第1図に示す如く
専用の供給口として設ける。
Next, the residue in the container main body 1 is mixed with a solvent, preferably a solvent compatible with water (NMP, NMP,
(HMPA, acetone, methanol, etc.) is added, and this is thoroughly stirred and washed by a stirring mechanism 9 installed in the main body 1, for example, a stirring blade, and then sieved and discharged from a discharge port 5 with a sieve 4. Subsequently, water is used instead of the solvent, and the cleaning liquid supply port 8
In addition to the residue in the container main body 1 as described above, washing with sufficient stirring is performed in the same manner as described below, and the liquid is sieved and discharged from the discharge port 5. The cleaning liquid supply port 8 is the polymer suspension supply port 3 described above.
However, it is usually provided as a dedicated supply port as shown in FIG.

このように、溶剤ならびに水で充分に洗浄し、篩分排液
すると、排液中に重合用溶剤(NMPなど)や洗浄用溶剤
ならびに副生物が留去するため、容器本体1の残留物
は、少量の水を含んだポリアリーレンスルフィド重合体
となる。
Thus, when thoroughly washed with a solvent and water and sieved and drained, the solvent for polymerization (such as NMP), the solvent for washing and by-products are distilled off in the drained liquid, so that the residue of the container body 1 is , A polyarylene sulfide polymer containing a small amount of water.

しかる後に、容器本体1を減圧下で加熱して前述の残留
物を減圧乾燥する。容器本体1に取り付けられる加熱機
構は様々なものが考えられるが、第1図に示される如
く、容器本体1を取り囲むようにジャケット11を設け、
その中に熱媒を通すことによって加熱する機構などが、
構造ならびに操作が簡単で便利である。この加熱にあた
っては、容器本体1内部を減圧状態にするとともに、攪
拌しながら加熱機構で加熱し、また必要に応じて逆円錐
状底部2の下端位置または更に最下端位置の抜出口6か
ら加熱した不活性ガス(窒素など)を送入することも有
効である。
Then, the container body 1 is heated under reduced pressure to dry the above-mentioned residue under reduced pressure. Although various heating mechanisms may be attached to the container body 1, as shown in FIG. 1, a jacket 11 is provided so as to surround the container body 1,
A mechanism to heat by passing a heat medium through it,
The structure and operation are simple and convenient. In this heating, the inside of the container body 1 was depressurized and heated by a heating mechanism while stirring, and if necessary, it was heated from the lower end position of the inverted conical bottom part 2 or further from the outlet 6 at the lowermost position. It is also effective to feed in an inert gas (such as nitrogen).

この減圧乾燥を行った後、冷却し、抜出口6から乾燥し
たポリアリーレンスルフィド重合体を抜き出せばよい。
なお、この抜出口6には弁12を備え、所望により開閉自
在としておくことが好ましい。
After performing the drying under reduced pressure, it may be cooled and the dried polyarylene sulfide polymer may be extracted from the outlet 6.
The outlet 6 is preferably provided with a valve 12 so that it can be opened and closed as desired.

〔実施例〕〔Example〕

次に、本発明を実施例に基いて更に詳しく説明する。 Next, the present invention will be described in more detail based on examples.

実施例 ポリフェニレンスルフィド(PPS)102kg,N−メチル−2
−ピロリドン(NMP)429kg,塩化ナトリウム(NaCl)122
kg及びオリゴマー9kgからなるPPS懸濁物を、第1図に示
される如き装置の容器本体1(容積1m3)内に懸濁物供
給口3を通して供給し、同時に篩4付きの排出口5で篩
分しながら排液した。
Example Polyphenylene sulfide (PPS) 102 kg, N-methyl-2
-Pyrrolidone (NMP) 429kg, Sodium chloride (NaCl) 122
A PPS suspension consisting of 9 kg and oligomers 9 kg was fed into the container body 1 (volume of 1 m 3 ) of the apparatus as shown in FIG. 1 through the suspension feed port 3 and, at the same time, at the discharge port 5 with the sieve 4. The liquid was drained while sieving.

次に、容器本体1の残留物に溶剤としてNMP350kgを、洗
浄液供給口8から注入し、30分間攪拌して充分に洗浄し
た後、篩4付きの排出口5から篩分排液した。
Next, 350 kg of NMP as a solvent was poured into the residue of the container body 1 from the cleaning liquid supply port 8, stirred for 30 minutes to thoroughly wash, and then drained from the discharge port 5 with the sieve 4 by sieving.

さらに、溶剤で洗浄した容器本体1内の残留物に純水35
0kgを、洗浄液供給口8から注入し、30分間攪拌して充
分に洗浄した後、篩4付きの排出口5から篩分排液し
た。この純水による洗浄,排液を三回繰り返し行った。
Furthermore, deionized water is added to the residue in the container body 1 washed with a solvent.
0 kg was injected from the cleaning liquid supply port 8, stirred for 30 minutes to thoroughly wash, and then drained through a discharge port 5 equipped with a sieve 4 through a sieve. This washing with pure water and drainage were repeated three times.

しかる後に、ジャケット11内を通す熱媒の温度を140℃
とすると共に、140℃の加熱窒素を1m3/hrの割合で容器
本体1の底部最下端にある抜出口6から吹き込んだ。容
器本体1内を100torr.の減圧下で上述の状態を3時間持
続して、容器本体1内の残留物を乾燥してほぼ純枠のPP
Sとし、これを冷却した後、抜出口6から抜き出した。
After that, the temperature of the heat medium passing through the jacket 11 is 140 ° C.
At the same time, heated nitrogen at 140 ° C. was blown at a rate of 1 m 3 / hr from the outlet 6 at the bottom bottom of the container body 1. The above condition is maintained for 3 hours under the reduced pressure of 100 torr. In the container body 1 to dry the residue in the container body 1 and to make the PP of almost pure frame.
It was designated as S, cooled, and then extracted from the outlet 6.

得られたPPSには不純物がほとんどなく、高純度のPPSフ
レークであった。また、このPPSフレークを成型したと
ころ、極白色のペレットが得られた。
The obtained PPS had almost no impurities and was highly pure PPS flakes. When this PPS flake was molded, a very white pellet was obtained.

なお、この一連の後処理操作を行うにあたっては、閉塞
トラブル等は皆無であり、特に注意を払わずとも操作を
円滑に行うことができた。
When performing this series of post-processing operations, there were no blockage troubles, and the operations could be performed smoothly without paying particular attention.

〔発明の効果〕〔The invention's effect〕

本発明によれば、ポリアリーレンスルフィド重合体懸濁
物の後処理操作を一つの装置内で行うことができるた
め、重合体懸濁物の移送時の閉塞トラブルが防止でき、
生産性の向上と補修費の低減を図ることができる。ま
た、装置ならびに操作が簡素化できるため、生産性の向
上と設備費の低減を図ることができる。しかも、得られ
るポリアリーレンスルフィドは、充分に精製されたもの
であって純度が高く、成型すれば極白色のペレットとな
る。
According to the present invention, since the post-treatment operation of the polyarylene sulfide polymer suspension can be performed in one device, it is possible to prevent the clogging trouble during the transfer of the polymer suspension,
It is possible to improve productivity and reduce repair costs. Further, since the device and the operation can be simplified, the productivity can be improved and the equipment cost can be reduced. Moreover, the obtained polyarylene sulfide is a sufficiently purified product and has a high purity, and when molded, it becomes a very white pellet.

したがって、本発明はポリアリーレンスルフィド重合体
懸濁物の後処理をはじめとするスラリー型の重合反応の
後処理に有効に適用でき、その工業的価値は極めて高
い。
Therefore, the present invention can be effectively applied to a post-treatment of a slurry type polymerization reaction including a post-treatment of a suspension of a polyarylene sulfide polymer, and its industrial value is extremely high.

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

第1図は本発明の装置の一例の断面形状を模式的に示す
説明図である。 図中、1は筒状容器本体,2は逆円錐状底部,3は重合体懸
濁物供給口,4は篩,5は篩付き排出口,6は抜出口,7は弁,8
は洗浄液供給口,9は攪拌機構,10はモーター,11はジャケ
ット,12は弁をそれぞれ示す。
FIG. 1 is an explanatory view schematically showing the cross-sectional shape of an example of the device of the present invention. In the figure, 1 is a cylindrical container body, 2 is an inverted conical bottom, 3 is a polymer suspension supply port, 4 is a sieve, 5 is a discharge port with a sieve, 6 is an outlet, 7 is a valve, 8
Is a cleaning liquid supply port, 9 is a stirring mechanism, 10 is a motor, 11 is a jacket, and 12 is a valve.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】重合反応終了後に得られるポリアリーレン
スルフィド重合体懸濁物の後処理を行うにあたり、該重
合体懸濁物を、下部に篩を具備した排出口を有すると共
に内部に攪拌機構を有する後処理装置に導入して篩分に
より排液し、次いで該装置内の残留物に溶剤を加えて攪
拌洗浄後、篩分により排液し、続いて該装置内の残留物
に水を加えて攪拌洗浄後、篩分により排液し、しかる後
に該装置を減圧下で加熱して該装置内の残留物を減圧乾
燥することを特徴とするポリアリーレンスルフィド重合
体懸濁物の後処理方法。
1. In the post-treatment of a polyarylene sulfide polymer suspension obtained after the completion of a polymerization reaction, the polymer suspension has a discharge port equipped with a sieve at the bottom and a stirring mechanism inside. It is introduced into a post-treatment device that has it and drained by a sieve, then a solvent is added to the residue in the device and washed by stirring, and then drained by a sieve, and then water is added to the residue in the device. After stirring and washing, the mixture is drained through a sieve, and then the apparatus is heated under reduced pressure to dry the residue in the apparatus under reduced pressure, which is a post-treatment method for a suspension of polyarylene sulfide polymer. .
【請求項2】ポリアリーレンスルフィド重合体懸濁物の
後処理装置において、逆円錐状底部を有する筒状容器本
体、該本体に取付けられた加熱機構、該本体内に設置さ
れた攪拌機構、該本体上部に設けられた重合体懸濁物お
よび洗浄液の供給口、ならびに該本体の逆円錐状底部側
面に設けられた篩を具備した排出口からなることを特徴
とするポリアリーレンスルフィド重合体懸濁物の後処理
装置。
2. A post-treatment device for a suspension of a polyarylene sulfide polymer, a tubular container body having an inverted conical bottom, a heating mechanism attached to the body, a stirring mechanism installed in the body, Polyarylene sulfide polymer suspension characterized in that it comprises a supply port for the polymer suspension and the washing liquid provided on the upper part of the main body, and an outlet provided with a sieve provided on the side surface of the inverted conical bottom part of the main body. Post-processing equipment for materials.
JP62188950A 1987-07-30 1987-07-30 Post-treatment method for polyarylene sulfide polymer suspension and apparatus therefor Expired - Lifetime JPH0749485B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62188950A JPH0749485B2 (en) 1987-07-30 1987-07-30 Post-treatment method for polyarylene sulfide polymer suspension and apparatus therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62188950A JPH0749485B2 (en) 1987-07-30 1987-07-30 Post-treatment method for polyarylene sulfide polymer suspension and apparatus therefor

Publications (2)

Publication Number Publication Date
JPS6433136A JPS6433136A (en) 1989-02-03
JPH0749485B2 true JPH0749485B2 (en) 1995-05-31

Family

ID=16232753

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62188950A Expired - Lifetime JPH0749485B2 (en) 1987-07-30 1987-07-30 Post-treatment method for polyarylene sulfide polymer suspension and apparatus therefor

Country Status (1)

Country Link
JP (1) JPH0749485B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10207122A (en) * 1997-01-23 1998-08-07 Nippon Zeon Co Ltd Manufacture of toner
WO2017073875A1 (en) * 2015-10-29 2017-05-04 주식회사 엘지화학 Device and method for washing off reactant residues of polymers

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5128445A (en) * 1990-06-14 1992-07-07 Phillips Petroleum Company Method to recover poly(arylene sulfide) polymers with water-polar organic compound

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10207122A (en) * 1997-01-23 1998-08-07 Nippon Zeon Co Ltd Manufacture of toner
WO2017073875A1 (en) * 2015-10-29 2017-05-04 주식회사 엘지화학 Device and method for washing off reactant residues of polymers

Also Published As

Publication number Publication date
JPS6433136A (en) 1989-02-03

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