JPH0431401A - Polymerization machine extraction device - Google Patents
Polymerization machine extraction deviceInfo
- Publication number
- JPH0431401A JPH0431401A JP13521090A JP13521090A JPH0431401A JP H0431401 A JPH0431401 A JP H0431401A JP 13521090 A JP13521090 A JP 13521090A JP 13521090 A JP13521090 A JP 13521090A JP H0431401 A JPH0431401 A JP H0431401A
- Authority
- JP
- Japan
- Prior art keywords
- extraction device
- extraction
- polymerization machine
- polymerization
- liquid
- 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
Links
Landscapes
- Polymerisation Methods In General (AREA)
- Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は重合処理装置に係り、特に高粘度処理液の重合
機からの被処理液の抜出しに好適な重合処Ｍｉ＆厘の被
処理液の抜出装置に関するものである。Detailed Description of the Invention [Industrial Field of Application] The present invention relates to a polymerization processing apparatus, and in particular to a polymerization processing system suitable for extracting a high viscosity processing liquid from a polymerization machine. This relates to an extraction device.
従来の重合処理は粘度的に６３０００ポアズから５００
０ポアズのものが多かったために、被処理液の抜出しも
ｉ！素加圧又はギヤポンプ等で抜き出されていた。Conventional polymerization treatment has a viscosity of 63,000 poise to 500 poise.
Since most of the liquids were 0 poise, it was difficult to extract the liquid to be treated. It was extracted using elementary pressurization or a gear pump.
ところが、近年エンジニアリングプラスチックにおいて
種々のポリマーが製造されており５ｏ。However, in recent years, various polymers have been produced as engineering plastics.
００・ポアズから１０００００ポアズのものもあり、そ
の上、弾力性のみるポリマーや、流動性の良くないポリ
マーもあり、従来の方法では、液の抜出しが困難となっ
てきた。なお、この権の！＆置として関連するものには
、例えば、夾公昭５８−１５４６６号が挙げられる。There are polymers with a size of 0.00 to 100,000 poise, and in addition, there are polymers with high elasticity and polymers with poor fluidity, making it difficult to extract the liquid using conventional methods. In addition, this right! Related works include, for example, Kyo Kosho No. 58-15466.
上記従来技術は重合機、の高粘度液の抜出しについて配
慮がされておらず、高粘度になると液が抜出せない等の
不具合があった。The above-mentioned conventional technology does not take into consideration the extraction of high viscosity liquid from the polymerization machine, and has problems such as the inability to extract the liquid when the viscosity becomes high.
本発明の目的は高粘度液を容易に抜出せ、かっデプドス
ペースを極力少なくできる重合機の抜出装置を提供する
ことにある。SUMMARY OF THE INVENTION An object of the present invention is to provide a withdrawal device for a polymerization machine that can easily withdraw a high viscosity liquid and minimize the amount of depleted space.
（ｌｌＪＩｉｌを解決するための手段〕上記目的は、重
合機の下部に吐出弁と、抜出しスクリューとを一体化し
た抜出！！錠を般け５銭抜出装厘の抜出速度を極々のポ
リマーの性状に合った抜出速度に制−する町夏速モータ
を具備したものである。(Means for solving the problem) The above purpose is to increase the extraction speed of the 5-sen extraction device by installing an extraction lock that integrates a discharge valve and an extraction screw at the bottom of the polymerization machine. It is equipped with a speed motor that controls the extraction speed to match the properties of the polymer.
抜出装置に吐出弁を内蔵しているので、重合機で反応が
完了するまでは吐出弁を閉とし、反応が終了し、被処理
液の抜出しが始まれば吐出弁を開として被処理液を抜出
すことができる。なお、抜出！！置を可変速可能な構造
とすれば被処理液の抜出速度は任意に設定することがで
きる。Since the extraction device has a built-in discharge valve, the discharge valve is closed until the reaction is completed in the polymerization machine, and when the reaction is completed and the extraction of the liquid to be treated begins, the discharge valve is opened and the liquid to be treated is discharged. It can be extracted. In addition, excerpts! ! If the structure is such that the position can be set at variable speed, the withdrawal speed of the liquid to be treated can be set arbitrarily.
Ｃ冥 施 例〕 以下、本発明の一実施例を第１図により説明する。C example An embodiment of the present invention will be described below with reference to FIG.
図において、重合機ｌの下部に抜出装置２を装備したも
のにおいて、吐出弁３と抜出しスクリュー４とを一体化
して抜出装置２を構成すると共に、抜出装［２の下部に
抜出速度を制御する可変速モーター６を歯車５を介して
連結した構造である。In the figure, in a polymerization machine 1 equipped with an extraction device 2 at the bottom, a discharge valve 3 and an extraction screw 4 are integrated to constitute the extraction device 2, and an extraction device 2 is installed at the bottom of the extraction device [2]. It has a structure in which a variable speed motor 6 that controls speed is connected via a gear 5.
以上の構成において、重合ｌｌｌで重合反応中は吐出弁
３の弁座を閉として、運転を行ない、重合反応終了後は
吐出弁３の弁座な開とする。該弁座の開閉はａ隔操作で
も可能である。次に、可変速モーター６を起動すれば、
歯車５を介して抜出しスクリ：、−４が回転し、被処理
液は強制的に重合機外へ抜出される。この時可変速モー
ター６を用いたことにより、ポリマーの性状に合ゼ任意
に抜出しスクリュー４の回転数が設定でき、払出速度を
所定のものにできる。回転数の設定は遠隔操作でも可能
である。重合機１．抜出装！２とも熱媒体で加熱できる
よう、シャケブト付構造で構成している。洗浄は吐出弁
３と弁７を閉とすることで重合機ｌ、抜出！ｉＩｅ！２
をそれぞれ単独に洗浄液を溜めることができ、系内とし
てはほぼ全体を洗浄できる構造としており、多品檜用の
ボッマー製造設備として広ζ利用できる。In the above configuration, operation is performed with the valve seat of the discharge valve 3 closed during the polymerization reaction, and after the polymerization reaction is completed, the valve seat of the discharge valve 3 is opened. The opening and closing of the valve seat can also be performed by a-separate operation. Next, if you start the variable speed motor 6,
The extractor screen 4 rotates through the gear 5, and the liquid to be treated is forcibly extracted out of the polymerization machine. At this time, by using the variable speed motor 6, the rotational speed of the extraction screw 4 can be arbitrarily set according to the properties of the polymer, and the delivery speed can be set to a predetermined value. The rotation speed can also be set by remote control. Polymerization machine 1. Extraction! Both of them have a structure with a heat exchanger so that they can be heated with a heat medium. For cleaning, close the discharge valves 3 and 7 and remove the polymerizer l! iIe! 2
The system is structured so that cleaning liquid can be stored independently in each, and almost the entire system can be cleaned, and can be widely used as a Bommer production facility for multi-grade Japanese cypress.
本実施例によれば高粘度およびポリマーの特性に合わせ
た被処理液の抜出しに効果がある。According to this embodiment, it is effective to extract a liquid to be treated that has a high viscosity and is suitable for the characteristics of the polymer.
望だ、洗浄もできるので多品種ポリマー製造設備として
も効果がある。Hopefully, since it can be cleaned, it will also be effective as a multi-product polymer production facility.
本発明によれば、重合反応後の、高粘度ポリマーの抜出
し、およびポリマー・の特性に合せ任意に抜出速度を設
定できるので、種々のポリマーの抜出しが容易にできる
効果がある。According to the present invention, the high viscosity polymer can be extracted after the polymerization reaction, and the extraction speed can be arbitrarily set according to the characteristics of the polymer, so that various polymers can be easily extracted.
第１図は本発明の一実施例の重合機の抜出５ｋＭである
。FIG. 1 shows a polymerization machine according to an embodiment of the present invention with an output of 5 km.
Claims (1)
化した抜出装置を設け、該抜出装置の抜出速度を所定の
速さに制御する可変速モーターを具備したことを特徴と
する重合機の抜出し装置。1. An extraction device that integrates a discharge valve and an extraction screw is provided at the lower part of the polymerization machine, and is equipped with a variable speed motor that controls the extraction speed of the extraction device to a predetermined speed. Extraction device of polymerization machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13521090A JPH0431401A (en) | 1990-05-28 | 1990-05-28 | Polymerization machine extraction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13521090A JPH0431401A (en) | 1990-05-28 | 1990-05-28 | Polymerization machine extraction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0431401A true JPH0431401A (en) | 1992-02-03 |
Family
ID=15146424
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13521090A Pending JPH0431401A (en) | 1990-05-28 | 1990-05-28 | Polymerization machine extraction device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0431401A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102008000432A1 (en) * | 2008-02-28 | 2009-09-03 | Evonik Röhm Gmbh | Rührkesselreaktor and methods for carrying out a polymerization reaction using such a stirred tank reactor |
-
1990
- 1990-05-28 JP JP13521090A patent/JPH0431401A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102008000432A1 (en) * | 2008-02-28 | 2009-09-03 | Evonik Röhm Gmbh | Rührkesselreaktor and methods for carrying out a polymerization reaction using such a stirred tank reactor |
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