JP2003238615A - Method for washing chlorinated vinyl chloride resin and apparatus therefor - Google Patents

Method for washing chlorinated vinyl chloride resin and apparatus therefor

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Publication number
JP2003238615A
JP2003238615A JP2002044456A JP2002044456A JP2003238615A JP 2003238615 A JP2003238615 A JP 2003238615A JP 2002044456 A JP2002044456 A JP 2002044456A JP 2002044456 A JP2002044456 A JP 2002044456A JP 2003238615 A JP2003238615 A JP 2003238615A
Authority
JP
Japan
Prior art keywords
vinyl chloride
chloride resin
chlorinated vinyl
water
cleaning
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.)
Granted
Application number
JP2002044456A
Other languages
Japanese (ja)
Other versions
JP3792582B2 (en
Inventor
Ryuji Tamura
柳二 田村
Takaaki Tanaka
隆昭 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.)
Tokuyama Sekisui Co Ltd
Original Assignee
Tokuyama Sekisui 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.)
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Publication of JP2003238615A publication Critical patent/JP2003238615A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method and an apparatus for washing chlorinated vinyl chloride resin slurry with small amount of water in a small-scale apparatus. <P>SOLUTION: This method for washing a chlorinated vinyl chloride resin comprises a first step of forming a cake layer by feeding the chlorinated vinyl chloride resin slurry to a washing tank equipped with a filtering device and filtering the slurry, a second step of feeding washing water to the cake layer from above the washing tank to wash and filter to form the cake layer again, and a third step of feeding water to the vicinity of upper part of the washed cake layer to make the chlorinated vinyl chloride resin at the lower part of the cake layer into slurry state, and thereafter taking out the washed chlorinated vinyl chloride resin slurry from the washing tank while feeding water from above the washing tank. <P>COPYRIGHT: (C)2003,JPO

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、塩素化塩化ビニル
系樹脂の洗浄方法及びその装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for cleaning chlorinated vinyl chloride resin and an apparatus therefor.

【0002】[0002]

【従来の技術】塩素化塩化ビニル系樹脂は、一般に塩化
ビニル系樹脂を水懸濁状態で塩素化することにより製造
されているが、塩素化する際に塩酸が副成される。
2. Description of the Related Art Chlorinated vinyl chloride resins are generally produced by chlorinating vinyl chloride resins in a water suspension state, but when chlorinating, hydrochloric acid is by-produced.

【0003】副成された塩酸は後工程である乾燥設備で
除去することが可能であるが、塩酸耐蝕性を有する設備
及び乾燥排気の塩酸処理設備が必要となり高価な設備と
なる。又、塩酸を中和剤を用いて中和した場合、中和後
の残留金属塩が製品の品質に悪影響を及ぼすと共に、中
和剤が高価なものにつくので一般に塩酸は水で洗浄除去
されている。
The hydrochloric acid produced as a by-product can be removed in a drying process which is a post-process, but a hydrochloric acid corrosion resistant facility and a dry exhaust hydrochloric acid treatment facility are required, which is an expensive facility. When hydrochloric acid is neutralized with a neutralizing agent, the residual metal salt after neutralization adversely affects the quality of the product, and the neutralizing agent becomes expensive, so hydrochloric acid is generally washed and removed with water. ing.

【0004】従来から採用されている洗浄方法は流動洗
浄法とデカンタ洗浄法である。流動洗浄法は、塩素化塩
化ビニル系樹脂スラリーを洗浄槽に供給し、下部から洗
浄水を通水し、攪拌して上部より塩酸排水をオーバーフ
ローさせる方法であり、デカンタ洗浄法は塩素化塩化ビ
ニル系樹脂スラリーを洗浄槽に供給し、水洗浄と遠心分
離を繰り返す方法である。
Conventionally adopted cleaning methods are a fluidized cleaning method and a decanter cleaning method. The fluidized cleaning method is a method in which the chlorinated vinyl chloride resin slurry is supplied to the cleaning tank, the cleaning water is passed from the lower part, and the hydrochloric acid drainage is overflowed from the upper part.The decanter cleaning method is the chlorinated vinyl chloride method. This is a method in which the system resin slurry is supplied to a cleaning tank, and water cleaning and centrifugation are repeated.

【0005】[0005]

【発明が解決しようとする課題】しかし、上記洗浄方法
の場合は洗浄装置が大きく設備費が非常に高く、洗浄す
る際には洗浄水が大量に必要であるという欠点があっ
た。
However, in the case of the above-mentioned cleaning method, there is a drawback that the cleaning apparatus is large and the equipment cost is very high, and a large amount of cleaning water is required for cleaning.

【0006】本発明の目的は、上記欠点に鑑み、塩素化
塩化ビニル系樹脂スラリーを小型の装置で、少量の洗浄
水で洗浄することのできる洗浄方法及び洗浄装置を提供
することにある。
In view of the above-mentioned drawbacks, an object of the present invention is to provide a cleaning method and a cleaning apparatus capable of cleaning a chlorinated vinyl chloride resin slurry with a small apparatus with a small amount of cleaning water.

【0007】[0007]

【課題を解決するための手段】すなわち、本発明は、塩
素化塩化ビニル系樹脂スラリーを、濾過手段を有する洗
浄槽に供給・濾過してケーキ層を形成する第1工程、ケ
ーキ層に、洗浄槽の上部から洗浄水を供給し、洗浄・濾
過し、再度ケーキ層を形成する第2工程及び洗浄された
ケーキ層の濾過手段の上部近傍に水を供給してケーキ層
下部の塩素化塩化ビニル系樹脂をスラリー状にした後、
洗浄槽上部から水を供給しながら洗浄された塩素化塩化
ビニル系樹脂スラリーを洗浄槽から抜き出す第3工程か
らなることを特徴とする塩素化塩化ビニル系樹脂の洗浄
方法を提供するものである。
[Means for Solving the Problems] That is, the present invention provides a first step of forming a cake layer by supplying and filtering the chlorinated vinyl chloride resin slurry into a washing tank having a filtering means, and washing the cake layer. The second step of supplying washing water from the upper part of the tank, washing and filtering, and again forming a cake layer, and supplying water to the vicinity of the upper part of the filter means of the washed cake layer to chlorinated vinyl chloride at the lower part of the cake layer. After making the system resin slurry,
A method for cleaning a chlorinated vinyl chloride resin, comprising a third step of extracting a chlorinated vinyl chloride resin slurry that has been cleaned while supplying water from the upper part of the cleaning tank, from the cleaning tank.

【0008】また、本発明は、上端部付近に塩素化塩化
ビニル系樹脂スラリー供給配管と洗浄水供給配管が設置
され、下端部付近に洗浄水除去配管が設置されている洗
浄槽の、下部であって洗浄水除去配管より上方に濾過手
段が設置されると共に濾過手段の上部近傍に開口部を有
する塩素化塩化ビニル系樹脂スラリー移送配管が設置さ
れており、塩素化塩化ビニル系樹脂スラリー移送配管に
は水供給配管が接続されていることを特徴とする塩素化
塩化ビニル系樹脂の洗浄装置を提供するものである。
Further, according to the present invention, the chlorinated vinyl chloride resin slurry supply pipe and the cleaning water supply pipe are installed near the upper end, and the cleaning water removing pipe is installed near the lower end in the lower part of the cleaning tank. Therefore, the filter means is installed above the cleaning water removal pipe, and the chlorinated vinyl chloride resin slurry transfer pipe having an opening is installed near the upper part of the filter means. The present invention provides a cleaning device for chlorinated vinyl chloride resin, characterized in that a water supply pipe is connected to.

【0009】[0009]

【発明の実施の形態】請求項1記載の塩素化塩化ビニル
系樹脂の洗浄方法は、塩素化塩化ビニル系樹脂スラリー
を、濾過手段を有する洗浄槽に供給・濾過してケーキ層
を形成する第1工程、ケーキ層に、洗浄槽の上部から洗
浄水を供給し、洗浄・濾過し、再度ケーキ層を形成する
第2工程及び洗浄されたケーキ層の濾過手段の上部近傍
に水を供給してケーキ層下部の塩素化塩化ビニル系樹脂
をスラリー状にした後、洗浄槽上部から水を供給しなが
ら洗浄された塩素化塩化ビニル系樹脂スラリーを洗浄槽
から抜き出す第3工程からなることを特徴とする。
BEST MODE FOR CARRYING OUT THE INVENTION A method of cleaning a chlorinated vinyl chloride resin according to claim 1, wherein a chlorinated vinyl chloride resin slurry is supplied to a cleaning tank having a filtering means and filtered to form a cake layer. In the first step, the washing water is supplied to the cake layer from the upper portion of the washing tank, and the cake layer is washed and filtered to form the cake layer again. A chlorinated vinyl chloride resin in the lower portion of the cake layer is made into a slurry, and the third step is to extract the washed chlorinated vinyl chloride resin slurry while supplying water from the upper portion of the washing tank from the washing tank. To do.

【0010】本発明で使用される塩素化塩化ビニル系樹
脂スラリーは、塩化ビニル系樹脂の懸濁液に塩素を供給
し、塩化ビニル系樹脂を塩素化して得られたスラリーで
あり、一般に塩素化塩化ビニル系樹脂と塩酸と水からな
る。
The chlorinated vinyl chloride resin slurry used in the present invention is a slurry obtained by supplying chlorine to a suspension of the vinyl chloride resin to chlorinate the vinyl chloride resin, and is generally chlorinated. Consists of vinyl chloride resin, hydrochloric acid and water.

【0011】上記塩化ビニル系樹脂は、塩化ビニルモノ
マー単独重合体若しくは塩化ビニルモノマーを主体(5
0重量%以上含む)とする、塩化ビニルモノマーと共重
合可能なビニルモノマーとの共重合体である。
The above vinyl chloride resin is mainly composed of vinyl chloride monomer homopolymer or vinyl chloride monomer (5
It is a copolymer of vinyl chloride monomer and copolymerizable vinyl monomer.

【0012】上記ビニルモノマーとしては、例えば、酢
酸ビニル、プロピオン酸ビニル等のビニルエステル;メ
チル(メタ)アクリレート、エチル(メタ)アクリレー
ト等のアルキル(メタ)アクリレートモノマー;エチレ
ン、プロピレン等のオレフィン;(メタ)アクリル酸、
無水マレイン酸、アクリロニトリル、スチレン、塩化ビ
ニリデンなどがあげられる。
Examples of the vinyl monomer include vinyl esters such as vinyl acetate and vinyl propionate; alkyl (meth) acrylate monomers such as methyl (meth) acrylate and ethyl (meth) acrylate; olefins such as ethylene and propylene; (Meth) acrylic acid,
Examples thereof include maleic anhydride, acrylonitrile, styrene and vinylidene chloride.

【0013】本発明における第1工程は、上記塩素化塩
化ビニル系樹脂スラリーを、濾過手段を有する洗浄槽に
供給・濾過してケーキ層を形成する工程である。
The first step in the present invention is a step of forming the cake layer by supplying and filtering the above chlorinated vinyl chloride resin slurry into a washing tank having a filtering means.

【0014】上記濾過手段としては、一般に濾材が使用
されるが、濾材としては上記塩素化塩化ビニル系樹脂を
濾過しうるものであればよく、例えば、織布、不織布、
ガラス繊維、金網、有孔金属板、セラミックス多孔体等
があげられる。
A filter medium is generally used as the filtering means. Any filter medium may be used as long as it can filter the chlorinated vinyl chloride resin, for example, woven fabric, non-woven fabric,
Examples thereof include glass fiber, wire mesh, perforated metal plate, and ceramic porous body.

【0015】上記洗浄槽は、濾過手段が洗浄槽の下部に
設けられているのが好ましく、スラリー中には塩酸が存
在するので、耐酸性の材料で製造されているのが好まし
い。
In the above washing tank, it is preferable that the filtering means is provided below the washing tank. Since hydrochloric acid is present in the slurry, it is preferable that the washing tank is made of an acid resistant material.

【0016】洗浄槽に塩素化塩化ビニル系樹脂スラリー
を供給すると、濾過手段により濾過されて、水及び塩酸
は除去され、濾過手段の上にケーキ層が形成される。
When the chlorinated vinyl chloride resin slurry is supplied to the washing tank, it is filtered by the filtering means to remove water and hydrochloric acid, and a cake layer is formed on the filtering means.

【0017】本発明における第2工程は、ケーキ層に、
洗浄槽の上部から洗浄水を供給し、洗浄・濾過し、再度
ケーキ層を形成する工程である。この工程はケーキ層中
の塩酸が除去されるまで1回又は複数回行われる。
The second step in the present invention is to form a cake layer,
This is a process of supplying washing water from the upper part of the washing tank, washing and filtering, and forming a cake layer again. This step is performed once or multiple times until the hydrochloric acid in the cake layer is removed.

【0018】濾過すると、ケーキ層中の水位は次第に低
下していく。ケーキ層の水位が高い時に洗浄水を供給す
るとケーキ層中の塩酸が洗浄水中に拡散して洗浄効果が
低下するので、ケーキ層中の水位がケーキ層表面から5
cm以上低下してから洗浄水を供給するのが好ましい。
When filtered, the water level in the cake layer gradually decreases. If the washing water is supplied when the water level of the cake layer is high, the hydrochloric acid in the cake layer diffuses into the washing water and the washing effect decreases, so the water level in the cake layer is 5
It is preferable to supply the washing water after the water has dropped by not less than cm.

【0019】本発明における第3工程は、洗浄されたケ
ーキ層の濾過手段の上部近傍に水を供給してケーキ層下
部の塩素化塩化ビニル系樹脂をスラリー状にした後、洗
浄槽上部から水を供給しながら洗浄された塩素化塩化ビ
ニル系樹脂スラリーを洗浄槽から抜き出す工程である。
In the third step of the present invention, water is supplied near the upper part of the filter means of the washed cake layer to make the chlorinated vinyl chloride resin in the lower part of the cake layer into a slurry, and then water is washed from the upper part of the washing tank. Is a step of extracting the chlorinated vinyl chloride resin slurry that has been washed from the washing tank while supplying.

【0020】洗浄された塩素化塩化ビニル系樹脂は抜き
出して乾燥する必要があるが、ケーキになった塩素化塩
化ビニル系樹脂は容易に抜き出すことができないので、
再度スラリー状にして抜き出す。
The washed chlorinated vinyl chloride resin needs to be extracted and dried, but since the caked chlorinated vinyl chloride resin cannot be easily extracted,
Slurry again and extract.

【0021】ケーキになった塩素化塩化ビニル系樹脂に
上部から水を供給したのでは、スラリー化に時間がかか
り抜き出しにくいので、ケーキ層の濾過手段の上部近傍
に水を供給してケーキ層下部の塩素化塩化ビニル系樹脂
をスラリー状にした後、洗浄槽上部から水を供給してス
ラリー状にして抜き出す。
If water is supplied to the caked chlorinated vinyl chloride resin from the upper portion, it takes time to form the slurry and it is difficult to extract it. Therefore, water is supplied near the upper portion of the cake layer filtering means to lower the cake layer. After making the chlorinated vinyl chloride resin of (1) into a slurry form, water is supplied from the upper part of the washing tank to make a slurry form and the slurry is extracted.

【0022】スラリー状になった塩素化塩化ビニル系樹
脂を抜き出すには、ポンプで抜き出してもよいし、洗浄
槽上部から加圧して抜き出してもよいが、抜き出し用の
配管を濾過手段の上部近傍に、即ち、ケーキ層下部の塩
素化塩化ビニル系樹脂がスラリー状にされる位置に開口
して抜き出すのが好ましい。
In order to extract the chlorinated vinyl chloride resin in the form of a slurry, it may be extracted with a pump or pressurized from the upper part of the washing tank, but the extraction pipe is provided near the upper part of the filtering means. That is, it is preferable that the chlorinated vinyl chloride resin at the bottom of the cake layer is opened and extracted at a position where the resin is slurried.

【0023】請求項2に記載の塩素化塩化ビニル系樹脂
の洗浄装置は、上端部付近に塩素化塩化ビニル系樹脂ス
ラリー供給配管と洗浄水供給配管が設置され、下端部付
近に洗浄水除去配管が設置されている洗浄槽の、下部で
あって洗浄水除去配管より上方に濾過手段が設置される
と共に濾過手段の上部近傍に開口部を有する塩素化塩化
ビニル系樹脂スラリー移送配管が設置されており、塩素
化塩化ビニル系樹脂スラリー移送配管には水供給配管が
接続されていることを特徴とする。
In the cleaning device for chlorinated vinyl chloride resin according to claim 2, a chlorinated vinyl chloride resin slurry supply pipe and a cleaning water supply pipe are installed near the upper end, and a cleaning water removal pipe is installed near the lower end. In the cleaning tank in which the filter is installed, the filtering means is installed in the lower part and above the cleaning water removing pipe, and the chlorinated vinyl chloride resin slurry transfer pipe having an opening is installed in the vicinity of the upper part of the filtering device. The water supply pipe is connected to the chlorinated vinyl chloride resin slurry transfer pipe.

【0024】上記塩素化塩化ビニル系樹脂の洗浄装置
は、請求項1記載の洗浄方法を実施するのに好適な洗浄
装置である。本発明の洗浄装置を図面を参照して説明す
る。図1は本発明の洗浄装置の一例を示す模式図であ
る。
The cleaning device for chlorinated vinyl chloride resin is a cleaning device suitable for carrying out the cleaning method according to the first aspect. The cleaning apparatus of the present invention will be described with reference to the drawings. FIG. 1 is a schematic view showing an example of the cleaning device of the present invention.

【0025】図中1は内面がチタンコーティングされて
いる洗浄槽である。洗浄槽1の上端部にバルブ21を介
して塩素化塩化ビニル系樹脂の反応槽(図示せず)と接
続されている塩素化塩化ビニル系樹脂スラリー供給配管
2と、バルブ31を介して洗浄水供給配管3が接続され
ている。
In the figure, reference numeral 1 is a cleaning tank having an inner surface coated with titanium. A chlorinated vinyl chloride resin slurry supply pipe 2 connected to a chlorinated vinyl chloride resin reaction tank (not shown) through a valve 21 at the upper end of the cleaning tank 1, and a washing water through a valve 31. The supply pipe 3 is connected.

【0026】4は、洗浄槽1の下端部に設置されている
洗浄水除去配管であり、洗浄水除去配管4の途中にもバ
ルブ41が設置されている。5は濾材であり、洗浄槽1
内であって、洗浄水除去配管4の上部に設置されてい
る。
Reference numeral 4 is a cleaning water removing pipe installed at the lower end of the cleaning tank 1, and a valve 41 is installed in the middle of the cleaning water removing pipe 4. 5 is a filter medium, and a cleaning tank 1
Inside, it is installed above the cleaning water removal pipe 4.

【0027】6は、開口部62が濾材5の上部近傍に位
置するように設置された塩素化塩化ビニル系樹脂スラリ
ー移送配管であり、塩素化塩化ビニル系樹脂スラリー移
送配管6はバルブ61を介して乾燥装置(図示せず)に
接続されている。
Numeral 6 is a chlorinated vinyl chloride resin slurry transfer pipe installed so that the opening 62 is located in the vicinity of the upper portion of the filter medium 5. The chlorinated vinyl chloride resin slurry transfer pipe 6 is provided with a valve 61. Connected to a drying device (not shown).

【0028】7は、バルブ71を介して洗浄水供給配管
3と、塩素化塩化ビニル系樹脂スラリー移送配管6のバ
ルブ61より開口部62側に接続されている水供給配管
である。
Reference numeral 7 is a water supply pipe connected to the washing water supply pipe 3 via a valve 71 and to the opening 62 side of the chlorinated vinyl chloride resin slurry transfer pipe 6 from the valve 61.

【0029】尚、8は、洗浄槽1の上部に設置された窒
素供給配管であり、バルブ81を介して窒素ボンベ(図
示せず)と接続されている。
Reference numeral 8 denotes a nitrogen supply pipe installed in the upper part of the cleaning tank 1, and is connected to a nitrogen cylinder (not shown) via a valve 81.

【0030】次に、上記洗浄装置で塩素化塩化ビニル系
樹脂を洗浄する方法を説明する。まず、バルブ31、6
1及び81を閉鎖し、バルブ21及び41を開放して塩
素化塩化ビニル系樹脂スラリー供給配管2から洗浄槽1
に塩素化塩化ビニル系樹脂スラリーを供給する。
Next, a method of cleaning the chlorinated vinyl chloride resin with the above cleaning device will be described. First, the valves 31, 6
1 and 81 are closed, valves 21 and 41 are opened, and the chlorinated vinyl chloride resin slurry supply pipe 2 is connected to the cleaning tank 1.
A chlorinated vinyl chloride resin slurry is supplied to.

【0031】供給された塩素化塩化ビニル系樹脂スラリ
ーは濾材5で濾過され、濾材5にケーキ層が形成され濾
過された水は洗浄水除去配管4から除去される。この
時、塩酸水が塩素化塩化ビニル系樹脂スラリー移送配管
6に入らないようにバルブ71を少し開放して洗浄水を
少量ずつ流し続けるのが好ましい。
The supplied chlorinated vinyl chloride resin slurry is filtered by the filter medium 5, a cake layer is formed on the filter medium 5, and the filtered water is removed from the cleaning water removing pipe 4. At this time, it is preferable to open the valve 71 a little so that the hydrochloric acid water does not enter the chlorinated vinyl chloride resin slurry transfer pipe 6 and continue to flow the cleaning water little by little.

【0032】次に、バルブ21を閉鎖すると共にバルブ
31を開放し、洗浄水供給配管3からケーキ層に洗浄水
を供給して塩素化塩化ビニル樹脂を洗浄し、濾過して再
度ケーキ層を形成する。洗浄水の供給は塩素化塩化ビニ
ル樹脂から塩酸が除去されるまで1回若しくは複数回行
う。
Next, the valve 21 is closed and the valve 31 is opened, washing water is supplied from the washing water supply pipe 3 to the cake layer to wash the chlorinated vinyl chloride resin, and the cake layer is formed again by filtration. To do. The washing water is supplied once or plural times until the hydrochloric acid is removed from the chlorinated vinyl chloride resin.

【0033】尚、前述の通り、洗浄水の供給はケーキ層
中の水位がケーキ層表面から5cm以上低下してから行
うのが好ましく、この工程中も、塩素化塩化ビニル系樹
脂スラリー移送配管6に入らないようにバルブ71を少
し開放して洗浄水を少量ずつ流し続けるのが好ましい。
又、濾過を速やかに行うために、バルブ81を開放して
窒素を供給し加圧してもよい。
As described above, it is preferable to supply the wash water after the water level in the cake layer has dropped from the surface of the cake layer by 5 cm or more. During this step, the chlorinated vinyl chloride resin slurry transfer pipe 6 is also provided. It is preferable to open the valve 71 a little and keep flushing water flowing little by little so that it does not enter into.
Further, in order to carry out filtration quickly, the valve 81 may be opened to supply nitrogen and pressurize.

【0034】洗浄された塩素化塩化ビニル系樹脂は乾燥
装置に移送され乾燥されるが、移送するには、まず、バ
ルブ31及び41を閉鎖し、バルブ71をゆるめ洗浄水
の供給量を増加し、塩素化塩化ビニル系樹脂スラリー移
送配管6の開口部62付近のケーキをスラリー化する。
The washed chlorinated vinyl chloride resin is transferred to a drier and dried. To transfer the chlorinated vinyl chloride resin, first close valves 31 and 41 and loosen valve 71 to increase the supply amount of cleaning water. The cake in the vicinity of the opening 62 of the chlorinated vinyl chloride resin slurry transfer pipe 6 is slurried.

【0035】次に、バルブ71を閉鎖すると共にバルブ
31を開放して洗浄水を供給してケーキ層全体をスラリ
ー化する。バルブ31の開放と同時若しくは直後にバル
ブ61を開放して、再度スラリー化された塩素化塩化ビ
ニル系樹脂スラリーを塩素化塩化ビニル系樹脂スラリー
移送配管6を通して乾燥装置に移送する。
Next, the valve 71 is closed and the valve 31 is opened to supply washing water to make the entire cake layer into a slurry. Simultaneously with or immediately after opening the valve 31, the valve 61 is opened to transfer the reslurried chlorinated vinyl chloride resin slurry to the drying device through the chlorinated vinyl chloride resin slurry transfer pipe 6.

【0036】スラリーの移送は、塩素化塩化ビニル系樹
脂スラリー移送配管6の途中にポンプを設けてもよい
し、バルブ81を開放して窒素で加圧することによって
行ってもよい。
The slurry may be transferred by providing a pump in the chlorinated vinyl chloride resin slurry transfer pipe 6 or by opening the valve 81 and pressurizing with nitrogen.

【0037】[0037]

【発明の効果】請求項1記載の塩素化塩化ビニル系樹脂
の洗浄方法は、上述の通りであるから、塩素化塩化ビニ
ル系樹脂スラリーを小型の装置で、少量の洗浄水で洗浄
することができる。
Since the method for cleaning a chlorinated vinyl chloride resin according to claim 1 is as described above, the chlorinated vinyl chloride resin slurry can be cleaned with a small amount of cleaning water in a small apparatus. it can.

【0038】又、請求項2記載の塩素化塩化ビニル系樹
脂の洗浄装置は、上述の通りであるから、装置が小型で
あり設備コストが安価であり、少量の洗浄水で効率よく
洗浄することができる。
Since the cleaning device for chlorinated vinyl chloride resin according to claim 2 is as described above, the device is small and the equipment cost is low, and the cleaning can be efficiently performed with a small amount of cleaning water. You can

【0039】[0039]

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

【図1】本発明の洗浄装置の一例を示す模式図である。FIG. 1 is a schematic view showing an example of a cleaning device of the present invention.

【符号の説明】[Explanation of symbols]

1 洗浄槽 2 塩素化塩化ビニル系樹脂スラリー供給配管 3 洗浄水供給配管 4 洗浄水除去配管 5 濾材 6 塩素化塩化ビニル系樹脂スラリー移送配管 7 水供給配管 1 cleaning tank 2 Chlorinated vinyl chloride resin slurry supply pipe 3 Wash water supply piping 4 Cleaning water removal piping 5 filter media 6 Chlorinated vinyl chloride resin slurry transfer pipe 7 Water supply piping

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4J100 AC03P BB01H CA01 CA31 EA06 GC35 GC37 HA21 HA61 HB04 HE06    ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 4J100 AC03P BB01H CA01 CA31                       EA06 GC35 GC37 HA21 HA61                       HB04 HE06

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 塩素化塩化ビニル系樹脂スラリーを、濾
過手段を有する洗浄槽に供給・濾過してケーキ層を形成
する第1工程、ケーキ層に、洗浄槽の上部から洗浄水を
供給し、洗浄・濾過し、再度ケーキ層を形成する第2工
程及び洗浄されたケーキ層の濾過手段の上部近傍に水を
供給してケーキ層下部の塩素化塩化ビニル系樹脂をスラ
リー状にした後、洗浄槽上部から水を供給しながら洗浄
された塩素化塩化ビニル系樹脂スラリーを洗浄槽から抜
き出す第3工程からなることを特徴とする塩素化塩化ビ
ニル系樹脂の洗浄方法。
1. A first step of supplying and filtering a chlorinated vinyl chloride resin slurry into a washing tank having a filtering means to form a cake layer, the washing water is supplied to the cake layer from the upper part of the washing tank, Second step of washing and filtering to form a cake layer again, and water is supplied to the washed cake layer near the upper part of the filtering means to make the chlorinated vinyl chloride resin in the lower part of the cake layer into a slurry, and then washed. A method for cleaning a chlorinated vinyl chloride resin, comprising a third step of extracting from the cleaning tank a chlorinated vinyl chloride resin slurry that has been cleaned while supplying water from the upper part of the tank.
【請求項2】 上端部付近に塩素化塩化ビニル系樹脂ス
ラリー供給配管と洗浄水供給配管が設置され、下端部付
近に洗浄水除去配管が設置されている洗浄槽の、下部で
あって洗浄水除去配管より上方に濾過手段が設置される
と共に濾過手段の上部近傍に開口部を有する塩素化塩化
ビニル系樹脂スラリー移送配管が設置されており、塩素
化塩化ビニル系樹脂スラリー移送配管には水供給配管が
接続されていることを特徴とする塩素化塩化ビニル系樹
脂の洗浄装置。
2. A cleaning water which is a lower part of a cleaning tank in which a chlorinated vinyl chloride resin slurry supply pipe and a cleaning water supply pipe are installed near the upper end and a cleaning water removal pipe is installed near the lower end. The filtration means is installed above the removal pipe, and the chlorinated vinyl chloride resin slurry transfer pipe with an opening is installed near the upper part of the filtration means. Water is supplied to the chlorinated vinyl chloride resin slurry transfer pipe. Cleaning equipment for chlorinated vinyl chloride resin, which is characterized by connecting pipes.
JP2002044456A 2002-02-21 2002-02-21 Cleaning method and apparatus for chlorinated vinyl chloride resin Expired - Lifetime JP3792582B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002044456A JP3792582B2 (en) 2002-02-21 2002-02-21 Cleaning method and apparatus for chlorinated vinyl chloride resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002044456A JP3792582B2 (en) 2002-02-21 2002-02-21 Cleaning method and apparatus for chlorinated vinyl chloride resin

Publications (2)

Publication Number Publication Date
JP2003238615A true JP2003238615A (en) 2003-08-27
JP3792582B2 JP3792582B2 (en) 2006-07-05

Family

ID=27783836

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002044456A Expired - Lifetime JP3792582B2 (en) 2002-02-21 2002-02-21 Cleaning method and apparatus for chlorinated vinyl chloride resin

Country Status (1)

Country Link
JP (1) JP3792582B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7345114B2 (en) 2006-01-26 2008-03-18 Kaneka Corporation Method for producing chlorinated vinyl chloride resin
JP2016525607A (en) * 2013-07-24 2016-08-25 リライアンス インダストリーズ リミテッドReliance Industries Ltd. Process for reducing residual acidity of halogenated polymers

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7345114B2 (en) 2006-01-26 2008-03-18 Kaneka Corporation Method for producing chlorinated vinyl chloride resin
JP2016525607A (en) * 2013-07-24 2016-08-25 リライアンス インダストリーズ リミテッドReliance Industries Ltd. Process for reducing residual acidity of halogenated polymers

Also Published As

Publication number Publication date
JP3792582B2 (en) 2006-07-05

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