JPS58189056A - Screen for centrifugal separator - Google Patents

Screen for centrifugal separator

Info

Publication number
JPS58189056A
JPS58189056A JP7278082A JP7278082A JPS58189056A JP S58189056 A JPS58189056 A JP S58189056A JP 7278082 A JP7278082 A JP 7278082A JP 7278082 A JP7278082 A JP 7278082A JP S58189056 A JPS58189056 A JP S58189056A
Authority
JP
Japan
Prior art keywords
screen
surface side
cylinder
slits
cylindrical
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
Application number
JP7278082A
Other languages
Japanese (ja)
Inventor
Minoru Yoshida
実 吉田
Seishiro Yoshinaga
吉永 征四郎
Koji Tanaka
耕二 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.)
MARUSHICHI TEKKOSHO KK
Nippon Steel Chemical and Materials Co Ltd
Original Assignee
MARUSHICHI TEKKOSHO KK
Nippon Steel Chemical 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 MARUSHICHI TEKKOSHO KK, Nippon Steel Chemical Co Ltd filed Critical MARUSHICHI TEKKOSHO KK
Priority to JP7278082A priority Critical patent/JPS58189056A/en
Publication of JPS58189056A publication Critical patent/JPS58189056A/en
Pending legal-status Critical Current

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  • Centrifugal Separators (AREA)

Abstract

PURPOSE:To obtain a screen having long life and high economical efficiency, by providing plural slits to each circumferential segmental pieces constituting a cylindrical screen in such a manner that said slits are formed in almost same parallel relation from the inner surface side of a cylinder to the outer surface side thereof. CONSTITUTION:Plural slits 3 arranged to the circumferential segmental pieces 2 and the adjusting spacer segmental pieces 2' of a screen 1 in parallel with the axial direction of a cylinder are formed in almost parallel relation from the inner surface side of the thickness of the cylinder to the outer surface side thereof. As the result, even if contact friction due to a hard particle such as an ammonium sulfate particle is generated to the inner peripheral surface of the screen 1 to advance friction, a slit width is not changed from the inner surface side to the outer surface side and, therefor, the screen 1 can be used without replacing the same until the plate material thereof becomes thin by abrasion. As the result, the screen capable of accomplishing sufficient function over a long period of time and having high economical efficiency is obtained.

Description

【発明の詳細な説明】 本発明は、遠心分離機用のスクリーンに関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a screen for a centrifuge.

バスケット型遠心分離機には固体と液体とを遠心分離す
るために、バスケット内側に円筒型スクリーンが設置さ
れている。%(イニ1円筒押出型の連続遠心分離機に使
用するスクリーンの場合は、細巾に成るスリットが円筒
の軸方向に多数配設されたものが使用されている。しか
し、このスクリーンのスリット巾は、結晶の種類によっ
て異なるも1通常05W1以下の微細な間隙を必要とす
る場合は、スリット部分のカツテングの問題や閉塞防止
と脱水効果を重視して、従来から円筒体内面の開口巾に
比して外面の開口巾が角度6〜12程度の末広がり状に
大きいものとなっていた。このような構成のスクリーン
を使用して結晶スラリー溶液の遠心分離作業を行うと、
分離液体の流出速度は高まり、%に開口巾の小さい円筒
体内面側のスリットの入口部分が最大の流出速度になる
。したがって、硫安のように粒径分布が比較的広範囲な
スラリー溶液を連続的に遠心分離したとき、結晶粒子は
微小であってもきわめて硬質であるため、流出速度の大
きい円筒体内内側のスリットの入口部分が接触摩擦によ
って急激に摩耗し9次第にスリットrj]が拡大され、
その結果、結晶の液中への流出が起こるようになる。こ
のため、スリットは分離機能を果すことが不可能となっ
てしまい、きわめて寿命の短い経済性の悪いスクリーン
となっていた。
A basket centrifuge has a cylindrical screen installed inside the basket to centrifugally separate solids and liquids. % (1) In the case of a screen used in a cylindrical extrusion type continuous centrifuge, a screen with a large number of narrow slits arranged in the axial direction of the cylinder is used. However, the slit width of this screen Although it differs depending on the type of crystal1, if a fine gap of 05W1 or less is required, it has been conventionally compared to the opening width of the inner surface of the cylinder, with emphasis on the problem of cutting the slit part, prevention of blockage, and dehydration effect. The width of the opening on the outer surface was wide at an angle of about 6 to 12 degrees.When centrifuging a crystal slurry solution using a screen with such a configuration,
The outflow speed of the separated liquid increases, and the outflow speed reaches the maximum at the entrance of the slit on the inner surface of the cylinder, which has a relatively small opening width. Therefore, when a slurry solution with a relatively wide particle size distribution such as ammonium sulfate is centrifuged continuously, the crystal particles are extremely hard even if they are minute, so the entrance of the slit inside the cylinder has a high flow rate. The part wears out rapidly due to contact friction, and the slit rj] is gradually enlarged,
As a result, the crystals begin to flow out into the liquid. For this reason, the slits were unable to perform the separation function, resulting in an economically uneconomical screen with an extremely short lifespan.

そこで、本発明者らは従来スクリーンのこのような欠点
を除去することを目的に研究した結果、スリット中を円
筒体の内面側から外面側にかけてほぼ同一の平行部分に
形成させたとき、ススリットを通過する分離液体の流出
速度が一定となるため、スリットの入口部分の摩耗程度
が著しく減少するとともに、たとえ摩耗が進展しても結
晶の液中への流出割合は初期段階とほとんど変わらず、
長期間にわたり良好な遠心分離作業を行うことができる
経済性の高いスクリーンを得ることのできることがわか
ったのである。
The inventors of the present invention conducted research aimed at eliminating these drawbacks of conventional screens, and found that when the slits were formed in almost the same parallel portion from the inner surface to the outer surface of the cylinder, the slits Since the outflow speed of the separated liquid passing through the slit remains constant, the degree of wear at the entrance of the slit is significantly reduced, and even if the wear progresses, the rate of crystal outflow into the liquid remains almost unchanged from the initial stage.
It has been found that it is possible to obtain a highly economical screen that can perform good centrifugation work over a long period of time.

本発明の構成および作用を図面の実施例に基いて説明す
る。
The structure and operation of the present invention will be explained based on embodiments of the drawings.

(1)は遠心分離様用の円筒形のスクリーンを示し、こ
のスクリーンは通常同一の曲率半径を有する複数個の円
周分片(2)および調整スペーサ分片(i)によって構
成されている1、調整スペーサ分片(2)は必要があれ
ば用いるものである。(3)はこのスクリーン(1)の
円周分片(2)および調整スペーサ分片(21に円筒体
の軸方向に平行に多数配設したスリットであり、このス
リットの開口巾は0.5順以下で、好ましくは01〜0
.3 a程度のものにする。そして、このスリット(3
1は円筒体の厚さの内面側から外面側にかけてほぼ同一
の平行部分に形成する。この円筒体を構成する円周分片
(2)および調整スペーサ分片(2)の肉厚は1〜5日
が好ましく、厚みを大きくすると圧損が増し。
(1) shows a cylindrical screen for centrifugal separation, which screen is usually constituted by a plurality of circumferential sections (2) and adjustment spacer sections (i) with the same radius of curvature. , the adjustment spacer piece (2) is used if necessary. (3) is a large number of slits arranged parallel to the axial direction of the cylindrical body in the circumferential segment (2) and the adjustment spacer segment (21) of this screen (1), and the opening width of this slit is 0.5 Below the order, preferably 01 to 0
.. 3 Make it about a grade. And this slit (3
1 is formed in substantially the same parallel portion from the inner surface side to the outer surface side of the cylindrical body. The wall thickness of the circumferential segment (2) and the adjustment spacer segment (2) constituting this cylindrical body is preferably 1 to 5 days, and as the thickness increases, pressure loss increases.

厚みを小さくすると損耗が早い。前記スリット(3)の
開口巾は、その外面側の一部分は内面側に比してやや拡
大して構成してもよい。また、スリット(3)の隣接間
隔はスリット中の5〜20倍が好ましい。(4)は前記
円周分片(2)の外周面の半径方向に適当間隔をおいて
ほぼ平行に設けた補強リブで、前記多数のスリットを一
体化している。この補強リブ(4)は、その軸方向の巾
の2〜5倍の間隔をおいて設け、また補強リブの内面側
の一部にもスリットの延長となる開口部(3°)1を設
けることが好ましい。
The smaller the thickness, the faster the wear and tear. The opening width of the slit (3) may be slightly larger on the outer surface side than on the inner surface side. Further, the distance between adjacent slits (3) is preferably 5 to 20 times the distance between the slits. (4) are reinforcing ribs provided approximately parallel to each other at appropriate intervals in the radial direction of the outer circumferential surface of the circumferential segment (2), and integrate the plurality of slits. These reinforcing ribs (4) are provided at intervals of 2 to 5 times the width in the axial direction, and openings (3°) 1, which are extensions of the slits, are also provided on a part of the inner surface of the reinforcing ribs. It is preferable.

而して、円周分片(2)を製造するときは、まず任意長
さの平板(例えばステンレス鋼板)を所望する円筒体ス
クリーンの曲率半径となるように彎曲した後に、所定間
隔に平行にスリットを任意の方法によって切截すること
によって内面側と外面側の開口巾をほぼ同一の平行部分
に構成するものである。
Therefore, when manufacturing the circumferential pieces (2), first, a flat plate (for example, a stainless steel plate) of an arbitrary length is curved so as to have the desired radius of curvature of the cylindrical screen, and then it is curved in parallel at predetermined intervals. By cutting the slit using an arbitrary method, the opening widths on the inner surface and the outer surface are formed into substantially the same parallel portions.

第5図は、以上説明した本発明のスクリーン(1)を円
筒押出型の連続遠心分離機に取付けた状態を示した概略
図である。(5)は一端の軸部がモータ(図示せず)で
回転すると同時に一定ストロークで往復運動する円筒形
の第1段バスケットで、その外周先端部には結晶押出し
用セグメント(6)が設けられ、またその内側部には押
出板(7)が設置されている。(8)は一端の軸部がモ
ータ(図示せず)で回転する円筒形の第2段バスケット
である。(9)は結晶スラリー供給管、(10)はスラ
リー分配器である。
FIG. 5 is a schematic diagram showing a state in which the screen (1) of the present invention described above is attached to a cylindrical extrusion type continuous centrifugal separator. (5) is a cylindrical first stage basket whose shaft at one end is rotated by a motor (not shown) and at the same time reciprocates at a constant stroke, and a crystal extrusion segment (6) is provided at the tip of its outer periphery. , and an extrusion plate (7) is installed on the inside thereof. (8) is a cylindrical second-stage basket whose shaft portion at one end is rotated by a motor (not shown). (9) is a crystal slurry supply pipe, and (10) is a slurry distributor.

第5図に示した実施例は、第1段バスケット(5)と第
2段バスケット(8)との内側にそれぞれ本発明のスク
リーン(1)が設置された二段スクリーン式の遠心分離
機である。いま結晶スラリー供給管(9)から連続的に
供給される結晶スラリーは、スラリー分配器(101か
らまず第1段バスケット(5)のスクリーン(1a)へ
分配され、液体はスクリーン(1)の外側面から排出さ
れて第2段バスケット(5)のスクリーン(1b)へ落
下し、スクリーン(1a)(1b)の内側面に分離され
た結晶ケーキ■は第1段バスケット(5)が一定ストロ
ークで往復運動することによって、結晶押出セグメント
(6)と押出板(7)とで往復ストローク分で連続的に
外部へ排出することができるようになっている。
The embodiment shown in FIG. 5 is a two-stage screen type centrifuge in which the screen (1) of the present invention is installed inside a first-stage basket (5) and a second-stage basket (8), respectively. be. The crystal slurry that is now continuously supplied from the crystal slurry supply pipe (9) is first distributed from the slurry distributor (101) to the screen (1a) of the first stage basket (5), and the liquid is distributed outside the screen (1). The crystal cake ■ is discharged from the side and falls onto the screen (1b) of the second stage basket (5), and is separated on the inner surface of the screen (1a) (1b). By reciprocating, the crystal extrusion segment (6) and the extrusion plate (7) can continuously discharge the crystal to the outside in a reciprocating stroke.

本発明のスクリーンは、上記した円筒押出型の連続遠心
分離機において最適であるが、しかしこれ以外にも例え
ば結晶スラリーをバッチ処理してスクリーン上の結晶ケ
ーキを往復運動する掻取刃で掻き取るバスケット型遠心
分離機にももちろん利用することができるものである。
The screen of the present invention is most suitable for the above-mentioned cylindrical extrusion type continuous centrifugal separator, but it can also be used, for example, for batch processing of crystal slurry and scraping off the crystal cake on the screen with a reciprocating scraping blade. Of course, it can also be used in a basket type centrifuge.

本発明はこのように、円筒形のスクリーンを構成する各
円周分片(2)に多数のスリット(3)が円筒内面側か
ら外面側にかけてほぼ同一の平行部・分を設けて成るこ
とを特徴とするものであるため、硫安のような硬質粒子
による接触摩擦がスクリーンの内周面に起って摩耗が進
行してもスリット巾が内面側から外面側にかけて変わら
ないから、これを取り換えることなくスクリーンの板材
全体が摩耗して薄くなるまで使用することができ、長期
間にわたりその機能を十分果たすことができる経済蛙の
高いスクリーンとなり、その効果はきわめて大きいもの
である。
In this way, the present invention provides a plurality of slits (3) in each of the circumferential segments (2) constituting a cylindrical screen, with substantially the same parallel portions extending from the inner surface to the outer surface of the cylinder. Because of this characteristic, the slit width does not change from the inner surface to the outer surface even if wear progresses due to contact friction caused by hard particles such as ammonium sulfate on the inner peripheral surface of the screen, so it is recommended to replace it. It can be used until the entire screen plate material wears out and becomes thin, making it a highly economical screen that can fully perform its functions for a long period of time, and its effects are extremely large.

なお、本発明の実施例を示せば次のとおりである。ここ
Vこ示す比較データは、第5図に示した二段式バスケッ
ト円筒押出型の連続遠心分離機に、硫安スラリー水溶液
(スラリー濃度4゜vo1%以上)を連続供給して硫安
結晶製出量4000 kf/ Hの割合で運転処理した
ものである。
Examples of the present invention are as follows. The comparative data shown here is based on the amount of ammonium sulfate crystals produced by continuously feeding an ammonium sulfate slurry aqueous solution (slurry concentration 4° VO 1% or more) to a two-stage basket cylindrical extrusion type continuous centrifuge shown in Figure 5. It was operated at a rate of 4000 kf/H.

(1)  従来のスクリーン(第1段バスケット側−直
径347+a+1.7′/x長さ8Q rm X 2列
、肉厚3 ran 。
(1) Conventional screen (first stage basket side - diameter 347+a+1.7'/x length 8Q rm x 2 rows, wall thickness 3 ran).

第2段バスケット側−直径410mm%x長さ8゜■×
2列、肉厚3 rrm 、スリット巾は第1・第2段と
も内面側02■、外面側1咽以上(末広がり角度9°)
で、隣接間隔3關ピツチで穿設)によって処理した場合
ニ スクリーン内面のスリット縁部から硫安結晶による摩耗
が急激に進行し、2か月経過後には母液側へ流出するス
ラリー濃度はl Ovol 96以上となり、スクリー
ン全体を全面的に取換えなければならなかった。
2nd stage basket side - diameter 410mm% x length 8゜■
2 rows, wall thickness 3 rrm, slit width for both 1st and 2nd stage is 02mm on the inner side and 1mm or more on the outer side (spreading angle 9°)
When the slurry is processed by drilling with 3 adjacent pitches), wear due to ammonium sulfate crystals rapidly progresses from the slit edges on the inner surface of the Niscreen, and after 2 months, the concentration of slurry flowing out to the mother liquor side is 1 Ovol 96 As a result, the entire screen had to be completely replaced.

(2)  本発明のスクリーン(スリット巾は第1・第
2段バスケット側とも内面側0.2311111.外面
側025關とほぼ同一中にした以外は、前記従来スクリ
ーンの場合と同じ)によって処理した場合:5か月経過
しても内面側スリット縁部分の摩耗は認められても、母
液側へ流出するスラリー濃度および硫安結晶製出量は作
業開始時の状態とほとんど変わらず、スクリーン自体は
さらに長期間同一機能を果すために使用できることが確
認できた。
(2) Processed with the screen of the present invention (the slit width is 0.2311111 on the inner side for both the first and second stage basket sides, and is the same as the conventional screen except that it is almost the same as the 0.25 mm on the outer side) Case: Although wear is observed on the inner slit edges after 5 months, the concentration of slurry flowing to the mother liquor side and the amount of ammonium sulfate crystals produced are almost the same as at the start of work, and the screen itself is even worse. It was confirmed that it can be used to perform the same function for a long period of time.

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

図面は本発明の一実施例を示したもので、第1図はスク
リーン全体の正面図、第2図は同上要部の正面図、第3
図は同上の平面図、第4図は同上A−A線の拡大断面図
、第5図は実施時の遠心分離機の概略側断面図である。 特許出願人 株式会社 九七鉄工所
The drawings show one embodiment of the present invention; FIG. 1 is a front view of the entire screen, FIG. 2 is a front view of the main parts of the same, and FIG.
The figure is a plan view of the same as above, FIG. 4 is an enlarged sectional view taken along line A--A of the above, and FIG. 5 is a schematic side sectional view of the centrifugal separator in operation. Patent applicant: Kushichi Iron Works Co., Ltd.

Claims (1)

【特許請求の範囲】 1 多数のスリットを備えた円筒形に成るスクリーンに
おいて、スリットが円筒の軸方向に多数平行に設けられ
るとともにスリット巾が円筒の内面側力・ら外面側にか
けてほぼ同一の平行部分に形成されていることを特徴と
する遠心分離機用スクリーン。 2 スリット巾は0.5 a以下で、好ましくは01〜
03哩である特許請求の範囲第1項記載の遠心分離機用
スクリーン。 3 円筒体は同一の曲率半径を有する複数枚の円周分片
と調整スペーサ分片とによって構成される特許請求の範
囲第1項記載の遠心分離機用スクリーン。 4 遠心分離機は円筒押出型連続遠心分離機である特許
請求の範囲第1項記載の遠心分離様用スククリーン。
[Claims] 1. In a cylindrical screen with a large number of slits, a large number of slits are provided parallel to each other in the axial direction of the cylinder, and the slit widths are approximately the same in parallel from the inner surface to the outer surface of the cylinder. A screen for a centrifuge, characterized in that the screen is formed in a portion. 2 The slit width is 0.5a or less, preferably 01~
The screen for a centrifuge according to claim 1, which has a diameter of 0.03 mm. 3. The screen for a centrifuge according to claim 1, wherein the cylindrical body is constituted by a plurality of circumferential pieces having the same radius of curvature and adjustment spacer pieces. 4. The screen for centrifugal separation according to claim 1, wherein the centrifugal separator is a cylindrical extrusion type continuous centrifugal separator.
JP7278082A 1982-04-30 1982-04-30 Screen for centrifugal separator Pending JPS58189056A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7278082A JPS58189056A (en) 1982-04-30 1982-04-30 Screen for centrifugal separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7278082A JPS58189056A (en) 1982-04-30 1982-04-30 Screen for centrifugal separator

Publications (1)

Publication Number Publication Date
JPS58189056A true JPS58189056A (en) 1983-11-04

Family

ID=13499239

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7278082A Pending JPS58189056A (en) 1982-04-30 1982-04-30 Screen for centrifugal separator

Country Status (1)

Country Link
JP (1) JPS58189056A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61120611A (en) * 1984-11-16 1986-06-07 マツクス・アー・ゲー Metal filter foil
JP2013128898A (en) * 2011-12-22 2013-07-04 Mitsubishi Chemicals Corp Centrifugal separator and method for producing bisphenol a

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61120611A (en) * 1984-11-16 1986-06-07 マツクス・アー・ゲー Metal filter foil
JPH058042B2 (en) * 1984-11-16 1993-02-01 Max Ag
JP2013128898A (en) * 2011-12-22 2013-07-04 Mitsubishi Chemicals Corp Centrifugal separator and method for producing bisphenol a

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