JPS586526B2 - Koekibunriki - Google Patents

Koekibunriki

Info

Publication number
JPS586526B2
JPS586526B2 JP50075629A JP7562975A JPS586526B2 JP S586526 B2 JPS586526 B2 JP S586526B2 JP 50075629 A JP50075629 A JP 50075629A JP 7562975 A JP7562975 A JP 7562975A JP S586526 B2 JPS586526 B2 JP S586526B2
Authority
JP
Japan
Prior art keywords
hollow shaft
solid
filtration chamber
filtration
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.)
Expired
Application number
JP50075629A
Other languages
Japanese (ja)
Other versions
JPS51151867A (en
Inventor
川島勇
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.)
Sumitomo Coal Mining Co Ltd
Original Assignee
Sumitomo Coal Mining 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 Sumitomo Coal Mining Co Ltd filed Critical Sumitomo Coal Mining Co Ltd
Priority to JP50075629A priority Critical patent/JPS586526B2/en
Publication of JPS51151867A publication Critical patent/JPS51151867A/en
Publication of JPS586526B2 publication Critical patent/JPS586526B2/en
Expired legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 本発明は固相と液相との混合物、即ち固液混合物を固相
と液相とに分離するための分離機に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a separator for separating a mixture of a solid phase and a liquid phase, that is, a solid-liquid mixture into a solid phase and a liquid phase.

従来の固液分離機即ちろ過機、湿式サイクロン及び遠心
分離機等は何れもその特徴を生かした分離機として使用
されているが、特に高粘度の固液分離は困難とされてい
る。
Conventional solid-liquid separators, such as filters, wet cyclones, and centrifugal separators, are all used as separators that take advantage of their characteristics, but it is particularly difficult to separate high viscosity solids and liquids.

本発明は、この問題点の解決を計るために高温高圧下で
も使用可能な機構、構造として、特に高温下で低粘性下
する固液混合物の分離に好適な新規な固液分離機を提供
するものである。
In order to solve this problem, the present invention provides a novel solid-liquid separator, which has a mechanism and structure that can be used even under high temperature and high pressure, and is particularly suitable for separating solid-liquid mixtures that have low viscosity at high temperatures. It is something.

即ち本発明は、円筒状容器の上下中央部に中空軸を取付
け、上面を傘形プレートとし、かつ底面をろ過板とした
円錐型チャンバーよりなるろ過室を、その中央部を上記
中空軸が貫通するように中空軸に固定し、上記ろ過室と
上記中空軸の接続部分にはろ過板を通してろ過室に流入
するろ過液が中空軸に流れ込むための孔隙が設けられ、
中空軸を通してろ過液を排出すると共に、中空軸に接続
した駆動装置により中空軸を介してろ過室にクイックリ
ターン運動が与えられるようにしたことを特徴とする固
液分離機である。
That is, the present invention has a hollow shaft attached to the upper and lower center of a cylindrical container, and the hollow shaft passes through a filtration chamber consisting of a conical chamber whose top surface is an umbrella-shaped plate and whose bottom surface is a filtration plate. The filtration chamber is fixed to the hollow shaft as shown in FIG.
This solid-liquid separator is characterized in that a filtrate is discharged through a hollow shaft, and a drive device connected to the hollow shaft provides quick return motion to the filtration chamber through the hollow shaft.

添付図面は本発明固液分離機の一実施例を示す。The accompanying drawings show an embodiment of the solid-liquid separator of the present invention.

第1図は固液分離機の縦断面図、第2図および第3図は
それぞれろ過室の縦断面図および底面図、第4図は駆動
装置の平面図を示す。
FIG. 1 is a longitudinal sectional view of the solid-liquid separator, FIGS. 2 and 3 are a longitudinal sectional view and a bottom view of the filtration chamber, respectively, and FIG. 4 is a plan view of the drive device.

本発明の固液分離機を添付図面に従って説明すれば、容
器1は下部を円錐状にした円筒型密閉構造とし、容器内
部は容器中央に取り付けられている中空軸2とろ過室3
とより構成されている。
To explain the solid-liquid separator of the present invention according to the attached drawings, a container 1 has a cylindrical sealed structure with a conical bottom, and inside the container is a hollow shaft 2 attached to the center of the container and a filtration chamber 3.
It is composed of.

ろ過室3は傘形プレート4を上面とし、底面をろ過面5
とする円錐型チャンバーで、このろ過室3の中央を貫通
する中空軸2に固定されている。
The filtration chamber 3 has an umbrella-shaped plate 4 on the top and a filtration surface 5 on the bottom.
It is a conical chamber, and is fixed to a hollow shaft 2 that passes through the center of this filtration chamber 3.

ろ過室3が取り付けられている中空軸2の部分にはろ過
液が流れ込むための孔隙6が設けられている。
A hole 6 through which the filtrate flows is provided in the portion of the hollow shaft 2 to which the filtration chamber 3 is attached.

中空軸2は容器上部に設けられたエヤーシリンダー、電
動方式等による駆動装置7に接続しており、この駆動装
置7によりろ過室3に中空軸2を介してクイックリター
ン運動が与えられる。
The hollow shaft 2 is connected to a drive device 7 such as an air cylinder or an electric type provided at the top of the container, and the drive device 7 provides a quick return motion to the filtration chamber 3 via the hollow shaft 2.

容器1内に流入した固液混合物はろ過面5でろ過され、
ろ過液はろ過室3内より中空軸2に入り中空軸より外部
に流出する。
The solid-liquid mixture flowing into the container 1 is filtered by the filtration surface 5,
The filtrate enters the hollow shaft 2 from inside the filtration chamber 3 and flows out from the hollow shaft.

一方固相は容器内を沈降して器底に沈澱するものと、ろ
過面5に附着または傘形プレート4に堆積するものとが
ある。
On the other hand, the solid phase is divided into two types: one that settles inside the container and settles on the bottom of the container, and the other that adheres to the filtration surface 5 or is deposited on the umbrella-shaped plate 4.

この中後者はクイックリターン運動により離脱または振
り落され器底に落下する。
The latter is detached or shaken off by the quick return movement and falls to the bottom of the vessel.

固液混合物は取入口8より容器1に入り、液相部分はろ
過室3のろ過面5を通りろ過室3の室内から孔隙6を経
て中空軸の中を通り、ロータリージョイント9を経て取
出口10より排出される。
The solid-liquid mixture enters the container 1 through the intake port 8, and the liquid phase portion passes through the filtration surface 5 of the filtration chamber 3, passes from the interior of the filtration chamber 3 through the pore 6, through the hollow shaft, and passes through the rotary joint 9 to the outlet. It is discharged from 10.

固相部分は容器1内を直接底部まで沈降するものと、ろ
過室3のろ過面5に附着または傘形プレート4に堆積す
るものとがあるが、この中ろ過室3のろ過面5に附着し
たものと、傘形プレート4に堆積した固相は駆動装置7
によるクイックリターン運動により離脱または振り落さ
れ直接沈降する固相と共に器底に沈澱する。
Some solid phase parts settle directly to the bottom of the container 1, while others adhere to the filtration surface 5 of the filtration chamber 3 or accumulate on the umbrella-shaped plate 4. The solid phase deposited on the umbrella plate 4 is transferred to the drive device 7.
The solid phase is separated or shaken off by the quick return movement of the solid phase, and is deposited at the bottom of the vessel along with the solid phase that settles directly.

沈澱した固相は自動弁11により抜き取られる。The precipitated solid phase is extracted by an automatic valve 11.

本発明の固液分離液は、容器を耐熱耐圧構造とすれば高
温下で低粘性化する高粘度固液混合物の分離が容易に可
能である。
The solid-liquid separation liquid of the present invention can easily separate a highly viscous solid-liquid mixture whose viscosity decreases at high temperatures if the container has a heat-resistant and pressure-resistant structure.

また、ろ過室3を第1図の如く数段取り付けることによ
りろ過面積の増大が可能となる。
Further, by installing the filtration chambers 3 in several stages as shown in FIG. 1, the filtration area can be increased.

更に固液混合物を円筒状容器1の切線方向から取り入れ
ることにより、サイクロン効果も発揮できる。
Furthermore, by introducing the solid-liquid mixture from the cutting line direction of the cylindrical container 1, a cyclone effect can also be exerted.

本発明に係る分離機は構造、機構が簡単で、無理が無く
連続運転が容易であり、分離効果、ろ過能力も優れてい
る。
The separator according to the present invention has a simple structure and mechanism, is easy to operate continuously, and has excellent separation effect and filtration ability.

また、製作費も比較的低廉で経済性に優れている。In addition, the production cost is relatively low, making it highly economical.

特に本発明の固液分離機は、石英の液化過程における固
液分離の如く高温下で低粘性下する固液混合物の分離に
利用すれば顕著な効果を発揮できる。
In particular, the solid-liquid separator of the present invention can exhibit remarkable effects when used for separating solid-liquid mixtures that have low viscosity at high temperatures, such as solid-liquid separation in the liquefaction process of quartz.

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

添付図面は本発明固液分離機の一実施例で、第1図は固
液分離機の縦断面図、第2図および第3図はそれぞれろ
過室の縦断面図および底面図、第4図は駆動装置の平面
図を示す。 図面において1は円筒状容器、2は中空軸、3はろ過室
、4は傘形プレート、5はろ過板、7は駆動装置である
The attached drawings show one embodiment of the solid-liquid separator of the present invention, in which Fig. 1 is a longitudinal sectional view of the solid-liquid separator, Figs. 2 and 3 are longitudinal sectional views and bottom views of the filtration chamber, respectively, and Fig. 4 is a longitudinal sectional view of the solid-liquid separator. shows a plan view of the drive device. In the drawings, 1 is a cylindrical container, 2 is a hollow shaft, 3 is a filtration chamber, 4 is an umbrella-shaped plate, 5 is a filter plate, and 7 is a drive device.

Claims (1)

【特許請求の範囲】[Claims] 1 円筒状容器1の上下中央部に中空軸2を取付け、上
面を傘形プレート4とし、かつ底面をろ過板5とした円
錐型チャンバーよりなるろ過室3を、その中央部を上記
中空軸2が貫通するように中空軸2に固定し、上記ろ過
室3と上記中空軸2の接続部分にはろ過板5を通してろ
過室3に流入するろ過液が中空軸2に流れ込むための孔
隙6が設けられ、中空軸2を通してろ過液を排出すると
共に、中空軸2に接続した駆動装置7により中空軸2を
介してろ過室3にクイックリターン運動が与えられるよ
うにしたことを特徴とする固液分離機。
1 A hollow shaft 2 is attached to the upper and lower center of a cylindrical container 1, and a filtration chamber 3 is constructed of a conical chamber with an umbrella-shaped plate 4 on the top surface and a filter plate 5 on the bottom surface, and the center portion thereof is attached to the hollow shaft 2. is fixed to the hollow shaft 2 so as to pass through the hollow shaft 2, and a hole 6 is provided at the connecting portion between the filtration chamber 3 and the hollow shaft 2 so that the filtrate flowing into the filtration chamber 3 through the filtration plate 5 flows into the hollow shaft 2. solid-liquid separation, characterized in that the filtrate is discharged through the hollow shaft 2, and a quick return motion is applied to the filtration chamber 3 via the hollow shaft 2 by a drive device 7 connected to the hollow shaft 2. Machine.
JP50075629A 1975-06-23 1975-06-23 Koekibunriki Expired JPS586526B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50075629A JPS586526B2 (en) 1975-06-23 1975-06-23 Koekibunriki

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50075629A JPS586526B2 (en) 1975-06-23 1975-06-23 Koekibunriki

Publications (2)

Publication Number Publication Date
JPS51151867A JPS51151867A (en) 1976-12-27
JPS586526B2 true JPS586526B2 (en) 1983-02-04

Family

ID=13581713

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50075629A Expired JPS586526B2 (en) 1975-06-23 1975-06-23 Koekibunriki

Country Status (1)

Country Link
JP (1) JPS586526B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111686490A (en) * 2020-06-23 2020-09-22 夏春辉 Self-cleaning formula grinds trigger copper powder recovery unit

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111686490A (en) * 2020-06-23 2020-09-22 夏春辉 Self-cleaning formula grinds trigger copper powder recovery unit

Also Published As

Publication number Publication date
JPS51151867A (en) 1976-12-27

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