JPS5929299B2 - Resin wet classification method and device - Google Patents

Resin wet classification method and device

Info

Publication number
JPS5929299B2
JPS5929299B2 JP3726977A JP3726977A JPS5929299B2 JP S5929299 B2 JPS5929299 B2 JP S5929299B2 JP 3726977 A JP3726977 A JP 3726977A JP 3726977 A JP3726977 A JP 3726977A JP S5929299 B2 JPS5929299 B2 JP S5929299B2
Authority
JP
Japan
Prior art keywords
resin
tower
classification
particle size
column
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
JP3726977A
Other languages
Japanese (ja)
Other versions
JPS53122177A (en
Inventor
祥市 奥
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP3726977A priority Critical patent/JPS5929299B2/en
Publication of JPS53122177A publication Critical patent/JPS53122177A/en
Publication of JPS5929299B2 publication Critical patent/JPS5929299B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Description

【発明の詳細な説明】 本発明はイオン交換樹脂で代表されるような小球状樹脂
(以下単に樹脂と称す)製造において副生ずることが避
けられない不必要な微粒子、微粉及び粗粒子樹脂と規格
樹脂とを選別する湿式分級方法および装置に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention deals with unnecessary fine particles, fine powders, and coarse particle resins that are unavoidably produced as by-products in the production of small spherical resins (hereinafter simply referred to as resins) such as ion exchange resins. The present invention relates to a wet classification method and apparatus for separating resins.

未分級樹脂を母集団にとれば規格内樹脂を中心として粗
粒子と微粒子への粒度分布ができる。
If unclassified resin is taken as the population, a particle size distribution can be created centering on resin within specifications into coarse particles and fine particles.

従来の篩による乾式分級においては粗粒子の除去は容易
であるが、微粒子並びに微粉の除去は粗粒子との密着等
により不充分であった。
In conventional dry classification using a sieve, it is easy to remove coarse particles, but the removal of fine particles and fine powder is insufficient due to their close contact with the coarse particles.

又、従来からの湿式分級においても廃水処理時に不都合
が生じる微粉、微粒子並びに破さい球を規格内樹脂と分
けるに留まっていた。
In addition, conventional wet classification only separates fine powder, fine particles, and broken spheres, which cause inconvenience during wastewater treatment, from resins that meet specifications.

本発明はか5る欠点を克服すべく研究した結果、複数の
格子筒をそれぞれ間隔を設けて塔長方向に装着し、格子
部間の空間の壁面に取出口を設けた湿式分級装置を用い
ることにより上記欠点を解消し、本発明に到達したもの
である。
As a result of research to overcome these drawbacks, the present invention uses a wet classifier in which a plurality of lattice cylinders are installed in the column length direction with intervals, and an outlet is provided on the wall of the space between the lattice parts. In this way, the above-mentioned drawbacks have been solved and the present invention has been achieved.

すなわち本発明は複数の格子筒を間隔をもうけて塔長方
向に装着した分級塔内に所定量の未分級樹脂をスラリー
状で導入した後肢塔下部より上昇流体を供給し、該樹脂
を流動化して塔長方向に粒度分布を形成した後、格子部
間の空間の塔壁面に設けた樹脂取出口より任意の粒径樹
脂を排出することを特徴とする樹脂の湿式分級方法であ
り、本発明方法を実施するための装置は複数の格子筒を
それぞれ間隔をもうけて上部および下部を除いた塔長方
向に装着し、該格子部間の分級塔壁面には樹脂仕込口と
適宜数の樹脂取出口を設け、かつ該塔上部に戻り水管、
該塔下部には循環水移送管を設けてなる湿式分級装置で
ある。
That is, in the present invention, a predetermined amount of unclassified resin is introduced in the form of a slurry into a classification tower in which a plurality of grid cylinders are installed at intervals in the direction of the tower length, and rising fluid is supplied from the lower part of the hind limb tower to fluidize the resin. This wet classification method for resin is characterized in that after forming a particle size distribution in the column length direction, resin of a desired particle size is discharged from a resin outlet provided on the column wall surface in the space between the lattice parts, and the present invention The apparatus for carrying out the method is equipped with a plurality of lattice cylinders spaced apart from each other in the lengthwise direction of the column excluding the upper and lower parts, and a resin inlet and an appropriate number of resin ports are installed on the wall of the classification tower between the lattice parts. Provide an outlet and return water pipe to the top of the tower,
This is a wet classifier equipped with a circulating water transfer pipe at the bottom of the column.

本発明においては分級基(以下単に塔と称す)側面塔長
方向に樹脂取出口を等間隔に数個所設け、塔下部から供
給する一定量の上昇流により塔内に軽、重樹脂層を形成
分布させ、浮遊状態を保ちつつ抜出しを必要とする粒径
樹脂の存在する取出口から任意の粒径樹脂を抜出すこと
が可能であり、塔内部に装着した格子筒により塔長方向
への上昇整流を乱すことなく樹脂を水平方向に均一抜出
することを特徴とする。
In the present invention, several resin outlets are provided at equal intervals in the column length direction on the side of the classification group (hereinafter simply referred to as column), and light and heavy resin layers are formed in the column by a certain amount of upward flow supplied from the bottom of the column. It is possible to distribute and extract resin of any particle size from the outlet where the resin of particle size that needs to be extracted is present while keeping it in a suspended state, and the lattice tube installed inside the tower allows it to be lifted in the direction of the tower length. It is characterized by uniformly extracting the resin in the horizontal direction without disturbing the flow.

次に本発明の実施の一例を図面に従って詳細に説明する
Next, an example of implementation of the present invention will be described in detail with reference to the drawings.

第1図は本発明装置の一実施例を示す断面図であり、図
中1は分級を行なう塔で上、下部を鏡板状に構成し、下
部鏡板中央部に上昇流を発生させる循環水ポンプ(図示
せず)に連通ずる循環水移送管2を連結する。
FIG. 1 is a cross-sectional view showing an embodiment of the apparatus of the present invention. In the figure, 1 is a column for performing classification, and the upper and lower parts are configured in the shape of mirror plates, and a circulating water pump that generates an upward flow in the center of the lower mirror plate. A circulating water transfer pipe 2 is connected to the pipe (not shown).

又、塔1内部直胴部と下部鏡板との境に集水板3を設け
、該集水板3には塔内へ均一に循環水が流通し、塔内樹
脂の逆流を防止する目的でスリットボール4を螺着する
In addition, a water collection plate 3 is provided at the boundary between the inner straight body of the tower 1 and the lower head plate, and the water collection plate 3 has the purpose of uniformly circulating water inside the tower and preventing backflow of resin in the tower. Screw on the slit ball 4.

集水板直上の塔側面に規格樹脂抜出口5を連着し、塔1
側面壁の塔長方向には樹脂取出口6を等間隔で数個所連
着する。
A standard resin outlet 5 is connected to the side of the tower directly above the water collection plate, and the tower 1
Several resin outlet ports 6 are connected at equal intervals in the column length direction of the side wall.

塔内部にはそれぞれの樹脂取出口6と水平方向に格子筒
7を該上端を合せて装着し、次段格子筒との間に50M
/M〜100 M/M程度の側面取出し用空隙部を各々
設ける。
Inside the tower, a lattice cylinder 7 is installed horizontally with each resin outlet 6, with the upper ends aligned, and there is a gap of 50M between the next stage lattice cylinder.
/M to 100M/M, respectively, are provided with side-side extraction cavities.

第2図は格子筒7の詳細斜視図である。FIG. 2 is a detailed perspective view of the lattice cylinder 7.

図中8はスラリー状樹脂を塔1内に仕込む為の樹脂仕込
口で、塔入口には逆流防止用の逆止弁9を装着する。
In the figure, reference numeral 8 denotes a resin inlet for charging slurry resin into the tower 1, and a check valve 9 for preventing backflow is installed at the inlet of the tower.

図中10は戻り水管で、上昇流をつくる循環水を該戻り
水管10から帰すため管開口部が塔1内中央部に位置す
る様塔側面に連着するが、該戻り水管10は自然流出に
つき循環水移送管2より大きい管径を必要とする。
In the figure, 10 is a return water pipe, and in order to return the circulating water that creates an upward flow from the return water pipe 10, the pipe opening is connected to the side of the tower located in the center of the tower 1, but the return water pipe 10 is a natural flow. Therefore, a pipe diameter larger than that of the circulating water transfer pipe 2 is required.

図中11は塔1内給水を兼ねた塔内清掃用散水管で塔1
内壁にそってリング状管を装着したものである。
In the figure, 11 is a sprinkler pipe for cleaning the tower that also serves as the water supply for tower 1.
A ring-shaped tube is attached along the inner wall.

肢管11は分級終了後、塔内壁及び格子筒7に付着した
樹脂を洗浄するのが目的なので、下方向に均一に飛散す
る様、角度に変化をもたせた数百の孔を有するリング状
管である。
The purpose of the limb tube 11 is to clean the resin adhering to the inner wall of the tower and the lattice tube 7 after classification, so it is a ring-shaped tube with hundreds of holes with varying angles so that the resin is uniformly scattered downward. It is.

なお、塔1の側面で樹脂仕込口8より上方に塔1内の樹
脂の状態を確認する覗窓12を取付ける。
A viewing window 12 for checking the state of the resin in the tower 1 is installed on the side of the tower 1 above the resin inlet 8.

次に本発明装置の操作の順序を説明すると、まず塔1に
直結するバルブを全て閉じた後、散水管11より散水し
て樹脂仕込口8より上まで貯水する。
Next, the order of operation of the apparatus of the present invention will be explained. First, all the valves directly connected to the column 1 are closed, and then water is sprayed from the sprinkler pipe 11 and the water is stored above the resin feed port 8.

貯水するのは仕込まれるスラリー状樹脂が気泡を噛んで
分級に支障をきたすのを防止するためである。
The purpose of storing water is to prevent the slurry resin being charged from trapping air bubbles and interfering with classification.

次に樹脂貯槽(図示せず)からスラリーポンプ(図示せ
ず)を用いて樹脂仕込み口8、逆止弁9を経て分級塔1
内水位を保ちつ5所定量のスラリー状樹脂を塔1内へ仕
込む。
Next, a slurry pump (not shown) is used to feed the resin from the resin storage tank (not shown) through the resin charging port 8 and the check valve 9 to the classification tower 1.
A predetermined amount of slurry resin is charged into tower 1 while maintaining the internal water level.

分級塔1内の水位を保つには集水板3、スリットボール
4および格子筒群の格子間を経て運転開始時の貯水レベ
ルに達する溢流管(図示せず)を設け、該溢流管より水
のみを排出すればよい。
In order to maintain the water level in the classification tower 1, an overflow pipe (not shown) is provided that reaches the water storage level at the start of operation through the water collecting plate 3, slit balls 4, and the lattices of the lattice cylinder group, and the overflow pipe Only the water needs to be drained.

次にスラリー状樹脂の仕込み紙工後、循環水系各バルブ
を開き循環水ポンプを駆動させ循環水移送管2、集水板
3、スリットボール4を経た上昇流により塔1内樹脂を
浮遊させ戻り水管10より排水しながら分級を開始する
が、循環水ポンプ(図示せず)を運転するにあたり管内
の空気を抜出しておく必要がある。
Next, after the slurry resin is loaded, each valve in the circulating water system is opened to drive the circulating water pump, and the upward flow through the circulating water transfer pipe 2, water collection plate 3, and slit ball 4 causes the resin in the tower 1 to float, and the return water pipe Classification is started while draining water from 10, but it is necessary to remove the air inside the pipe before operating a circulating water pump (not shown).

又、あらかじめ一定流量となるようコントロールバルブ
を調整しておき運転開始後流量計にて流量の微調整を行
うことが重要である。
Furthermore, it is important to adjust the control valve in advance to maintain a constant flow rate, and then fine-tune the flow rate using a flow meter after the start of operation.

覗窓12により浮遊展開樹脂上面の位置を確認するが、
樹脂上面より上で浮遊している少量の微粉は、約2時間
程度で戻り水管10を通り塔1外へ排出され、さらに約
4時間で塔内樹脂の粒度分布が形成されるので分級作業
は終了する。
The position of the top surface of the floating developing resin is confirmed through the viewing window 12.
A small amount of fine powder floating above the top of the resin will be discharged to the outside of the tower 1 through the return water pipe 10 in about 2 hours, and the particle size distribution of the resin in the tower will be formed in about 4 hours, so the classification work will be completed. finish.

さらに上昇流を継続しつ5粗粒子樹脂は分級塔1下方の
、微粒子樹脂は上方の所定樹脂取出口6より排出する。
Further, the upward flow is continued, and the coarse particle resin is discharged from the lower part of the classification tower 1, and the fine particle resin is discharged from a predetermined resin outlet 6 at the upper part.

微粒子および粗粒子樹脂の排出終了後、塔内の残存規格
樹脂を規格樹脂抜出口5から総量抜出すことにより本発
明のイオン交換樹脂の分級は完了するが、上昇流により
樹脂の粒度分布を形成した後、規格樹脂を直接所定の樹
脂取出口6より排出することも可能である。
After discharging the fine particles and coarse particle resin, the total amount of the standard resin remaining in the column is extracted from the standard resin extraction port 5 to complete the classification of the ion exchange resin of the present invention, but the upward flow forms the particle size distribution of the resin. After that, it is also possible to directly discharge the standard resin from a predetermined resin outlet 6.

以上のように本発明方法および装置はイオン交換樹脂の
分級を短時間に完全に行なうことが出来、かつ微粉樹脂
を塔外へ循環水と共に排出し、又微粒子から粗粒子樹脂
までを任意に選択除外出来る優れた機能を有するもので
ある。
As described above, the method and apparatus of the present invention can completely classify ion exchange resins in a short period of time, discharge fine powder resin to the outside of the column together with circulating water, and arbitrarily select resin particles from fine particles to coarse particle resins. It has an excellent function that can be excluded.

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

第1図は本発明になる湿式分級装置の一実施例を示す断
面図であり、第2図は格子筒の斜視図である。 1・・・・・・分級塔、2・・・・・・循環水移送管、
3・・・・・・集水板、4・・・・・・スリットボール
、5・・・・・・規格樹脂抜出口、6・・・・・・樹脂
取出口、7・・・・・・格子筒、8・・・・・・樹脂仕
込口、9・・・・・・逆止弁、10・・・・・・戻り水
管、11・・・・・・塔内清掃用散水管、12・・・・
・・覗窓。
FIG. 1 is a sectional view showing an embodiment of the wet classifier according to the present invention, and FIG. 2 is a perspective view of a lattice tube. 1... Classifying tower, 2... Circulating water transfer pipe,
3...Water collection plate, 4...Slit ball, 5...Standard resin outlet, 6...Resin outlet, 7...・Grate tube, 8...Resin charging port, 9...Check valve, 10...Return water pipe, 11...Water pipe for cleaning inside the tower, 12...
...Peephole.

Claims (1)

【特許請求の範囲】 1 複数の格子筒を間隔をもうけて塔長方向に装着した
分級塔内に所定量の未分級樹脂をスラリー状で導入した
後、該塔下部より上昇流体を供給し、該樹脂を流動化し
て塔長方向に粒度分布を形成した後、格子部間の空間の
塔壁面に設けた樹脂取出口より任意の粒径樹脂を排出す
ることを特徴とする樹脂の湿式分級方法。 2 樹脂を粒度で選別する分級基において、複数の格子
筒をそれぞれ間隔をもうけて上部および下部を除いた塔
長方向に装着し、該格子部間の分級塔壁面には樹脂仕込
口と適宜数の樹脂取出口を設け、かつ該塔上部に戻り水
管、該塔下部には循環水移送管を設けてなる樹脂の湿式
分級装置。
[Scope of Claims] 1. A predetermined amount of unclassified resin is introduced in the form of slurry into a classification tower in which a plurality of grid cylinders are installed at intervals in the direction of the tower length, and then a rising fluid is supplied from the lower part of the tower, A wet classification method for resin, which comprises fluidizing the resin to form a particle size distribution in the column length direction, and then discharging resin of a desired particle size from a resin outlet provided on the column wall in the space between the lattice sections. . 2. In a classification group that sorts resins by particle size, a plurality of grid cylinders are installed at intervals in the column length direction excluding the upper and lower parts, and a resin charging port and an appropriate number of resin charging ports are installed on the wall surface of the classification tower between the grid parts. A wet classifier for resin, which is provided with a resin outlet, a return water pipe in the upper part of the tower, and a circulating water transfer pipe in the lower part of the tower.
JP3726977A 1977-03-31 1977-03-31 Resin wet classification method and device Expired JPS5929299B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3726977A JPS5929299B2 (en) 1977-03-31 1977-03-31 Resin wet classification method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3726977A JPS5929299B2 (en) 1977-03-31 1977-03-31 Resin wet classification method and device

Publications (2)

Publication Number Publication Date
JPS53122177A JPS53122177A (en) 1978-10-25
JPS5929299B2 true JPS5929299B2 (en) 1984-07-19

Family

ID=12492943

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3726977A Expired JPS5929299B2 (en) 1977-03-31 1977-03-31 Resin wet classification method and device

Country Status (1)

Country Link
JP (1) JPS5929299B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6142352B2 (en) * 2012-12-18 2017-06-07 日立化成株式会社 Classification device, classification method, and classification particle manufacturing method

Also Published As

Publication number Publication date
JPS53122177A (en) 1978-10-25

Similar Documents

Publication Publication Date Title
US2351864A (en) Dust collector
CN207694404U (en) A kind of vertical grease filter separator
CN103285629A (en) Multi-direction flow gravitational settling apparatus for recirculating aquaculture system
JPS5929299B2 (en) Resin wet classification method and device
US4062697A (en) Method and apparatus for countercurrent washing of particulate solids
US5009776A (en) Filter system
CN104787866A (en) Water circulation treatment system for wet electric dust collector
SU797554A3 (en) Method and device for density separating of mineral mixture
CN206351083U (en) A kind of full enclosed cyclone dust collectors
CN108992998A (en) A kind of phosphate ore pulp particle sorting apparatus based on multi_layer extraction
CN109260872A (en) Liquid separator
EP0128234A1 (en) Sand filtration apparatus
JPS626845B2 (en)
KR102003120B1 (en) A Sand Reduction System From Water Getting Underground Water
US3740929A (en) Apparatus for collecting finely divided sticky material
CN102430271B (en) Inclined plate type rotational flow sand setting system
US3042204A (en) Process and apparatus for separating granular solids into two or more end fractions
JPS60212205A (en) Wet dust removing apparatus
CN210279489U (en) Magnetic separator for kaolin
US2913116A (en) Method and apparatus for separating usable particles from collecting liquid
CN209185432U (en) Device for the removal of breeding water body particulate matter
JP2013081906A (en) Apparatus and method for producing ion exchange treatment water
CN217748396U (en) A categorised cleaning machine for chinese-medicinal material
US2733810A (en) murry
CN2223138Y (en) Solid-liquid phase physico-chemical self-controling reactor