JPS5928680Y2 - centrifugal concentrator - Google Patents

centrifugal concentrator

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Publication number
JPS5928680Y2
JPS5928680Y2 JP3365781U JP3365781U JPS5928680Y2 JP S5928680 Y2 JPS5928680 Y2 JP S5928680Y2 JP 3365781 U JP3365781 U JP 3365781U JP 3365781 U JP3365781 U JP 3365781U JP S5928680 Y2 JPS5928680 Y2 JP S5928680Y2
Authority
JP
Japan
Prior art keywords
separated liquid
cylindrical body
suspension
vertical wall
flow path
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
JP3365781U
Other languages
Japanese (ja)
Other versions
JPS57145554U (en
Inventor
洽 清水
浩良 水上
Original Assignee
株式会社クボタ
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 株式会社クボタ filed Critical 株式会社クボタ
Priority to JP3365781U priority Critical patent/JPS5928680Y2/en
Publication of JPS57145554U publication Critical patent/JPS57145554U/ja
Application granted granted Critical
Publication of JPS5928680Y2 publication Critical patent/JPS5928680Y2/en
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 本考案は、濃縮用−紙筒状体に対して、処理すべき懸濁
液を供給する流路、及び、回転軸芯側に集められた分離
液を排出する流路を前記回転軸芯方向上部側に設けであ
る遠心濃縮機に関する。
[Detailed description of the invention] The present invention provides a flow path for supplying the suspension to be treated and a flow path for discharging the separated liquid collected on the rotation axis side to the paper cylinder for concentration. The present invention relates to a centrifugal concentrator in which a passage is provided on the upper side in the direction of the rotation axis.

上記の−ものでは、懸濁液の連続的な供給に伴い、その
供給懸濁液が分離液液面に衝突して飛散される状態とな
り、その飛散した懸濁液が直接的に分離液排出流路に流
入して排出されるとか、又、懸濁液の分離液液面への突
入に伴って分離液の液面に近い部分で撹乱を生じ、その
撹乱状態の分離液が排出流路に流入して排出される等、
排出される分離液の固形分濃度が痛く、固形分の回収効
率が低下していた。
In the above method, as the suspension is continuously supplied, the supplied suspension collides with the surface of the separated liquid and is scattered, and the scattered suspension is directly discharged from the separated liquid. When the suspension enters the flow path and is discharged, or when the suspension enters the surface of the separated liquid, disturbance occurs near the surface of the separated liquid, and the disturbed separated liquid flows into the discharge flow path. such as flowing into and being discharged, etc.
The solid content concentration of the separated liquid discharged was poor, and the solid content recovery efficiency was low.

本考案は、上記の点に鑑み、簡単な構造の付加によって
、連続的に供給する懸濁液分離液排出路への直接的な流
入を確実に防止すると共に、懸濁液供給に起因する撹乱
の影響を回避する状態で分離液を排出し、排出分離液の
濃度を十分低下させて固形分の回収効率を向上できるよ
うにすることを目的とする。
In view of the above points, the present invention reliably prevents the continuously supplied suspension from directly flowing into the separated liquid discharge channel by adding a simple structure, and also prevents disturbance caused by the suspension from being supplied. The purpose of this invention is to discharge the separated liquid in a state that avoids the influence of this, sufficiently lowering the concentration of the discharged separated liquid and improving the solid content recovery efficiency.

本考案の遠心濃縮機は、濃縮用回転筒状体に対して、処
理すべき懸濁液を供給する流路、及び。
The centrifugal concentrator of the present invention includes a flow path for supplying a suspension to be treated to a rotating cylindrical body for concentration;

回転軸芯側に集められた分離液を排出する流路を前記回
転軸芯方向上部側に設けである遠心濃縮機であって、前
記回転筒状体の天井壁内周縁に環状の縦壁を連設すると
共に、この縦壁に周方向に所定間隔をへだてた状態で、
前記分離液排出流路の一部を構成する分離液排出孔を形
成し、前記縦壁の下縁にその全周に亘って前記縦壁より
も径方向やや外方及び径方向内方に突出する状態で遮へ
い板を付設しである。
A centrifugal concentrator in which a flow path for discharging the separated liquid collected on the rotation axis side is provided on the upper side in the direction of the rotation axis, and an annular vertical wall is provided on the inner periphery of the ceiling wall of the rotating cylindrical body. At the same time as being installed in a row and being separated from this vertical wall at a predetermined interval in the circumferential direction,
A separated liquid discharge hole constituting a part of the separated liquid discharge flow path is formed at the lower edge of the vertical wall and protrudes slightly radially outward and radially inward from the vertical wall over its entire circumference. A shielding plate is attached in such a state that the

従って、次の作用効果が得られる。Therefore, the following effects can be obtained.

■ 処理すべき懸濁液を連続的に供給した場合に、その
供給懸濁液が未処理状態で分離液の上層を流動して分離
液排出流路より流出する作用を、縦壁よりも径方向やや
外方及び径方向内方に突出する状態で付設した遮へい板
によって完全に阻ILでき、しかも、懸濁液供給に伴っ
て分離液の液面近くで撹乱される状態となっても、撹乱
状態の分離液が遮へい板相当箇所に到達するまでの間に
十分遠心濃縮作用を受けさせることができ、遮へい板の
径方向外方側をくぐりぬけた分離液のみが排出液路より
排出され、よって固形分の回収効率を向上させながら、
懸濁液の連続供給が可能となった。
■ When the suspension to be treated is continuously supplied, the untreated suspension flows in the upper layer of the separated liquid and flows out from the separated liquid discharge channel. It can be completely blocked by the attached shielding plate that protrudes slightly outward in the direction and inward in the radial direction, and even if it is disturbed near the liquid surface of the separated liquid as the suspension is supplied, Until the separated liquid in a disturbed state reaches the part corresponding to the shielding plate, it can be subjected to sufficient centrifugal concentration action, and only the separated liquid that has passed through the radially outer side of the shielding plate is discharged from the discharge liquid path. Therefore, while improving solid content recovery efficiency,
Continuous supply of suspension became possible.

O、縦壁に周方向に所定間隔をへだてた状態で、分離液
排出流路の一部を構成する分離液排出孔を形成しである
ために、この排出孔より分離液を通過させることによっ
て流動抵抗を付与することができ、そのために、固形分
の流出をより抑制することができる。
O. Since separated liquid discharge holes forming a part of the separated liquid discharge channel are formed in the vertical wall at a predetermined interval in the circumferential direction, by allowing the separated liquid to pass through the discharge holes. Flow resistance can be imparted, and therefore the outflow of solid content can be further suppressed.

次に、本考案の実施例を図面に基いて詳述する。Next, embodiments of the present invention will be described in detail based on the drawings.

断面形状コの字状で環状の被処理物収納空間Sを形成し
た濃縮用回転筒状体1を、駆動機構2を介して縦軸芯1
周りで駆動回転自在に設けると共に、同収槽3に貯留さ
れた懸濁液を前記空間Sの一ド端側近くに供給する流路
rを設け、他方、筒状体1の上部側に、回転に伴って筒
状体1の(ロ)転軸芯P側に東められた分離液10をオ
ーバーフローによって排出する流路Rを設けると共に、
筒状体1の内周壁に張付いた濃縮物11を回収するため
の装置4を、シリンダ5の伸縮によって作用状態と非作
用状態とに切換自在に設け、もって、廃水処理システム
から沈降分離によって回収される汚泥等の懸濁液を、筒
状体1の高速回転に伴う遠心力により濃縮分離し、所定
量の濃縮物11が張り付いた状態において懸濁液の供給
を停止して濃縮物11を回収し、しかる後に再び濃縮分
離を行わせるように、いわゆるバッチ式の遠心濃縮機を
構成しである。
A rotary cylindrical body 1 for concentration, which has a U-shaped cross section and an annular storage space S for the processed material, is connected to a vertical axis 1 via a drive mechanism 2.
A flow path r is provided around the cylindrical body 1 so as to be freely rotatable, and a flow path r is provided for supplying the suspension stored in the storage tank 3 near one end side of the space S, and on the other hand, on the upper side of the cylindrical body 1, In addition to providing a flow path R for discharging the separated liquid 10, which is directed toward the (b) rotation axis P side of the cylindrical body 1 as it rotates, by overflow,
A device 4 for recovering the concentrate 11 stuck to the inner circumferential wall of the cylindrical body 1 is provided so as to be switchable between an active state and a non-active state by expanding and contracting the cylinder 5. The collected suspension such as sludge is concentrated and separated by the centrifugal force caused by the high speed rotation of the cylindrical body 1, and when a predetermined amount of concentrate 11 is stuck, the supply of the suspension is stopped and the concentrate is separated. This is a so-called batch type centrifugal concentrator, which collects 11 and then concentrates and separates it again.

前記分離液排出流路Rを構成するに、筒状体1の天井壁
1a内周縁に連ねて、環状の縦壁6を連設し、その縦壁
6に周方向に所定間隔をへだてる状態で分離液排出孔7
・・・・・・を形成し、そして、前記縦壁6の下縁に、
その全周にわたらせて、分離液10の液面よりやや入り
込んだ位置から液面より筒状体1の径方向内方に突出す
る状態で遮へい板8を設け、供給懸濁液の未処理状態で
の直接的な流出を防■、Lすると共に、懸濁液の供給に
起因して分離液10が撹乱され、その撹乱状態の分離液
10が排出流路R,測に向かって流動しても、遮へい板
8への尚突によって失速され、その状態で遠心力を受げ
させて良好に濃縮分離するように、更には、排出孔γ・
・・・・・を通過させることによって流動抵抗を付与し
、それにより固形分の流出をより抑制するように構成し
である。
To configure the separated liquid discharge flow path R, an annular vertical wall 6 is continuously provided along the inner peripheral edge of the ceiling wall 1a of the cylindrical body 1, and a predetermined interval is spaced from the vertical wall 6 in the circumferential direction. Separated liquid discharge hole 7
... is formed, and at the lower edge of the vertical wall 6,
A shielding plate 8 is provided around the entire circumference of the cylindrical body 1 so as to protrude inward in the radial direction of the cylindrical body 1 from a position slightly below the liquid level of the separated liquid 10, so that the untreated state of the supplied suspension is maintained. In addition to preventing direct outflow at In addition, the discharge holes γ and 8 are stalled by colliding with the shielding plate 8, and are subjected to centrifugal force in that state for good concentration and separation.
... is configured to provide flow resistance by passing through, thereby further suppressing the outflow of solid content.

尚、本考案は、上述実施列のように、懸濁液の濃縮分離
と濃縮物11の回収を行うパッチ式の遠心濃縮機に限ら
ず、第2図に示すように、筒状体1の下端側に隔壁9を
介して濃縮物回収空間S1を形成すると共に、それに濃
縮物回収流路R1を接続し、濃縮分離と濃縮物11回収
のいずれをも連続的に行えるタイプの遠心濃縮機にも適
用できる。
Note that the present invention is not limited to the patch-type centrifugal concentrator that concentrates and separates the suspension and recovers the concentrate 11 as in the above-mentioned series of implementations, but also applies to a cylindrical body 1 as shown in FIG. A centrifugal concentrator of a type in which a concentrate recovery space S1 is formed on the lower end side via a partition wall 9, and a concentrate recovery channel R1 is connected thereto, so that both concentration separation and concentrate 11 recovery can be performed continuously. can also be applied.

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

図面は本考案に係る遠心濃縮機の実施例を示し、第1図
は全体縦断面図、第2図は変形例を示す全体縦断面図で
ある。 1・・・・・・筒状体、1a・・・・・・天井壁、6・
・・・・・縦壁、7・・・・・・分離液排出孔、S・・
・・・・遮へい板、r・・・・・・懸濁液供給流路、R
・・・・・・分離液排出流路、P・・・・・・筒状体の
回転軸芯。
The drawings show an embodiment of the centrifugal concentrator according to the present invention, with FIG. 1 being an overall longitudinal sectional view, and FIG. 2 being an overall longitudinal sectional view showing a modification. 1...Cylindrical body, 1a...Ceiling wall, 6.
... Vertical wall, 7... Separated liquid discharge hole, S...
...shielding plate, r...suspension supply channel, R
...Separated liquid discharge channel, P...Rotation axis of the cylindrical body.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 濃縮用回転筒状体1に対して、処理すべき懸濁液を供給
する流路r、及び、回転軸芯P側に集められた分離液を
排出する流路Rを前記回転軸芯P方向上部側に設けであ
る遠心濃縮機であって、前記回転筒状体1の天井壁1a
内周縁に環状の縦壁6を連設すると共に、この縦壁6に
周方向に所定間隔をへたてた状態で、前記分離液排出流
路Rの一部を構成する分離液排出孔7・・・・・・を形
成し、前記縦壁6の下縁にその全周に亘って前記縦壁6
よりも径方向やや外方及び径方向内方に突出する状態で
遮へい板8を付設しである遠心濃縮機。
A flow path r for supplying the suspension to be treated and a flow path R for discharging the separated liquid collected on the rotation axis P side are connected to the rotation axis P for the concentration rotating cylindrical body 1. A centrifugal concentrator provided on the upper side, the ceiling wall 1a of the rotary cylindrical body 1
An annular vertical wall 6 is continuously provided on the inner peripheral edge, and a separated liquid discharge hole 7 forming a part of the separated liquid discharge channel R is provided at a predetermined interval in the circumferential direction on this vertical wall 6. ... is formed on the lower edge of the vertical wall 6 over the entire circumference.
A centrifugal concentrator equipped with a shielding plate 8 that protrudes slightly outward and inward in the radial direction.
JP3365781U 1981-03-10 1981-03-10 centrifugal concentrator Expired JPS5928680Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3365781U JPS5928680Y2 (en) 1981-03-10 1981-03-10 centrifugal concentrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3365781U JPS5928680Y2 (en) 1981-03-10 1981-03-10 centrifugal concentrator

Publications (2)

Publication Number Publication Date
JPS57145554U JPS57145554U (en) 1982-09-13
JPS5928680Y2 true JPS5928680Y2 (en) 1984-08-18

Family

ID=29831000

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3365781U Expired JPS5928680Y2 (en) 1981-03-10 1981-03-10 centrifugal concentrator

Country Status (1)

Country Link
JP (1) JPS5928680Y2 (en)

Also Published As

Publication number Publication date
JPS57145554U (en) 1982-09-13

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