JP2001113204A - High-performance centrifugal separator for fine particle having synchronized rotation mechanism and magnetic discharge mechanism in separation tank - Google Patents
High-performance centrifugal separator for fine particle having synchronized rotation mechanism and magnetic discharge mechanism in separation tankInfo
- Publication number
- JP2001113204A JP2001113204A JP33037999A JP33037999A JP2001113204A JP 2001113204 A JP2001113204 A JP 2001113204A JP 33037999 A JP33037999 A JP 33037999A JP 33037999 A JP33037999 A JP 33037999A JP 2001113204 A JP2001113204 A JP 2001113204A
- Authority
- JP
- Japan
- Prior art keywords
- separation tank
- tank
- magnet
- fine particles
- separation
- 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
Links
Landscapes
- Centrifugal Separators (AREA)
Abstract
Description
【0001】本発明は微粒子混合液を対象とする固液分
離用高性能遠心分離機の分離機能、及び分離タンク内に
留積した微粒子(濃縮液として)の排出機能の技術改善
により、総体的高性能化を計ろうとするものである。[0001] The present invention provides an overall improvement by improving the separation function of a high-performance centrifugal separator for solid-liquid separation for a mixed liquid of fine particles and the function of discharging fine particles (as a concentrated liquid) accumulated in a separation tank. The goal is to achieve higher performance.
【0002】従来の微粒子高性能遠心分離機は高速回転
する分離タンクと同タンク内対象液が慣性で同調回転せ
ず、分離タンクより対象液が低回転傾向にあり、分離性
能を著しく低下している。又、分離タンク内壁に留積し
た微粒子固形物の剥離排出機能も消極的技法によるもの
で、機能性が極めて低調なのが現状である。In the conventional high-performance fine particle centrifuge, the separation tank rotating at high speed and the target liquid in the tank do not rotate synchronously due to inertia, and the target liquid tends to rotate at a lower speed than the separation tank. I have. In addition, the function of peeling and discharging solid fine particles deposited on the inner wall of the separation tank is also based on a passive technique, and at present the functionality is extremely low.
【0003】本発明は従来の微粒子高性能分離機の分離
タンクと同タンク内対象液の非同調回転に対して同調回
転化の技術的解決機構、及び分離タンク内壁に留積した
微粒子固形物の技術的排出機構とによる技術改善で構成
する本遠心分離機の総合的性能の向上を計ることを目的
とする。[0003] The present invention provides a technical solution mechanism for synchronizing rotation of a separation tank of a conventional high-performance fine particle separator and non-synchronous rotation of a target liquid in the separation tank, and a method of removing fine solid particles deposited on the inner wall of the separation tank. The purpose of the present invention is to improve the overall performance of the centrifuge constituted by the technical improvement by the technical discharge mechanism.
【0004】本遠心分離機の分離タンクの回転に対し
て、同タンク内対象液を同調回転させる機能を付加して
分離性能を高め、又、分離タンク内壁に留積した微粒子
固形物の剥離排出機能の技術的改善として、強力永久磁
石を組み込んだ磁力作用による反発構造の強制振動機構
とによる総体的性能向上を計ろうとするものである。[0004] The function of synchronizing the rotation of the target liquid in the separation tank is added to the rotation of the separation tank of the centrifugal separator to enhance the separation performance, and the solid particles deposited on the inner wall of the separation tank are separated and discharged. As a technical improvement of the function, an attempt is made to improve the overall performance by a forced vibration mechanism of a repulsion structure by a magnetic force incorporating a strong permanent magnet.
【0005】本発明は分離タンクの回転に対して同タン
ク内対象液を同調回転させるために同タンク内に縦方向
に拾数枚の同調回転板を配備した構造の同調回転機構を
構成して、固液分離機能を向上させている。According to the present invention, there is provided a tuning rotary mechanism having a structure in which several tuning rotary plates are provided in the tank in a vertical direction in order to synchronize the target liquid in the tank with the rotation of the separation tank. And the solid-liquid separation function is improved.
【0006】又、同タンク内の内壁に接して、底部より
直立した拾数枚のたんざく形の振動薄板の中高位置に固
定した強力磁石に、同タンク外部より運転中止時の慣性
運転に対して、同極対抗する外部磁石を接近する構造で
振動薄板に振動を与え、その上に留積した微粒子固形物
を剥離し、濃縮液として下方に流す磁力排出機構との二
重効果で、総体的性能を高めている。In addition, a strong magnet fixed to the middle and high positions of a plurality of tangle-shaped vibrating thin plates that are in contact with the inner wall inside the tank and that stand upright from the bottom is used to prevent inertia operation when operation is stopped from outside the tank. Vibration is applied to the vibrating thin plate in a structure in which an external magnet opposing the same pole is approached, the fine solid particles deposited on the vibrating plate are separated, and the magnetic force discharge mechanism that flows downward as a concentrated solution has a double effect. Performance is enhanced.
【0007】本発明を図について説明する。本発明は微
粒子高性能遠心分離機の上下のベアリングで支持され、
直結モーター(M)で回転する中空回転軸(1)に固定
した分離タンク(2)内外諸構造の技術的改善による総
体的性能の向上を目的とするものである。The present invention will be described with reference to the drawings. The invention is supported by the upper and lower bearings of a fine particle centrifuge,
The purpose of the present invention is to improve the overall performance by technically improving the internal and external structures of the separation tank (2) fixed to the hollow rotary shaft (1) rotated by the direct-coupled motor (M).
【0008】分離対象液が浄化液と微粒子濃縮液に分離
排出する経過を説明すると、対象液(図中実線矢印)を
回転中の中空回転軸(1)の上部より供給すると、同軸
の横孔より分離タンク(2)内に放流され、数枚の強制
沈殿板(3)をくぐり抜けつつ浄化液(点線矢印)とな
り、分離タンク(2)の上部の放出孔より浄化液統合装
置(4)を通り、本体(5)の排出孔から排出する構造
を構成している。The process of separating and discharging the liquid to be separated into a purified liquid and a fine particle concentrated liquid will be described. When the liquid to be separated (solid arrow in the drawing) is supplied from above the rotating hollow rotary shaft (1), a coaxial horizontal hole The liquid is discharged into the separation tank (2), passes through several forced sedimentation plates (3) and becomes a purified liquid (dotted arrow). The purified liquid integrating device (4) is discharged from the discharge hole at the top of the separation tank (2). As a result, a structure for discharging from the discharge hole of the main body (5) is configured.
【0009】対象液は、回転中の分離タンク(2)内で
慣性作用のため同タンクと同調回転せず、可成り低回転
となり、対象液に対する遠心作用は低下し、分離能力の
低下となるので、強制沈殿板(3)を利用して、拾数枚
の同調回転板(10)を装着した同調回転機構により固
液分離機能の向上を計った構造で構成している。The target liquid does not rotate synchronously with the rotating separation tank (2) due to inertia in the rotating separation tank (2), but rather rotates at a relatively low speed. The centrifugal action on the target liquid is reduced and the separation capacity is reduced. Therefore, the structure is such that the solid-liquid separation function is improved by using a forced rotating plate (3) and a synchronous rotating mechanism equipped with several synchronous rotating plates (10).
【0010】一方、対象液が上流しつつ遠心分離作用で
浄化されると同時に、分離微粒子は分離タンク(2)の
内壁の全面に内接し、同タンク底より直立して、中高位
置に振動磁石(6)を保有するたんざく形の振動薄板
(7)上に留積する。On the other hand, at the same time as the target liquid is purified by the centrifugal separation action while being upstream, the separated fine particles are inscribed in the entire inner wall of the separation tank (2), stand upright from the bottom of the tank, and are set at the middle and high positions. (6) is piled up on a tangle-shaped vibrating thin plate (7).
【0011】本体(5)には、上記振動磁石(6)に同
極対抗する固定磁石(8)を保有する磁力排出装置
(9)が装着されていて、運転時には同装置の固定磁石
(8)を退去させた状態であるが、運転中止時には分離
タンク(2)の慣性回転中に磁力排出装置(9)を操作
して、固定磁石(8)を分離タンク(2)に接近固定す
ると、振動磁石(6)が連続反発して振動薄板(7)を
振動させ、留積微粒子を剥離し、同タンク内残留液と混
合した濃縮液(二重実線矢印)が回転終了時に落下し
て、分離タンク(2)の底の廃棄孔より排出する構造を
構成している。The main body (5) is provided with a magnetic force discharging device (9) having a fixed magnet (8) having the same polarity as that of the vibrating magnet (6). ), But when the operation is stopped, the magnetic force discharging device (9) is operated during inertial rotation of the separation tank (2) to fix the fixed magnet (8) close to the separation tank (2). The vibrating magnet (6) continuously repels and vibrates the vibrating thin plate (7) to separate the accumulated fine particles, and the concentrated liquid (double solid arrow) mixed with the residual liquid in the tank drops at the end of rotation, It constitutes a structure that discharges from a waste hole at the bottom of the separation tank (2).
【0012】本発明は微粒子高性能遠心分離機におい
て、分離、排出両機能の技術改善により更に高性能化を
促進させるものと思う。It is believed that the present invention further enhances the performance of fine particle high-performance centrifuges by improving both the separation and discharge functions.
【図1】は立面図の破断面図。FIG. 1 is a cutaway view of an elevation view.
【図2】は平面図。FIG. 2 is a plan view.
(1)は中空回転軸、(2)は分離タンク、(3)は強
制沈殿板、(4)は浄化液統合装置、(5)は本体、
(6)は振動磁石、(7)は振動薄板、(8)は固定磁
石、(9)は磁力排出装置、(10)は同調回転板。(1) is a hollow rotary shaft, (2) is a separation tank, (3) is a forced sedimentation plate, (4) is a purified liquid integration device, (5) is a main body,
(6) is a vibrating magnet, (7) is a vibrating thin plate, (8) is a fixed magnet, (9) is a magnetic force discharging device, and (10) is a tuning rotary plate.
Claims (1)
ンク(2)内の分離対象液(図中実線)を同タンクと同
回転まで同調させるために、同タンク内の強制沈殿板
(3)に同調回転板(10)を等配備して構成した同調
回転機構、及び分離タンク(2)内の分離留積微粒子
は、同タンク内の内壁全面に内接して中高位置に振動磁
石(6)を保有するたんざく形の振動薄板(7)上に留
積するが、本体(5)には上記振動磁石(6)に同極対
抗する固定磁石(8)を保有した磁力排出装置(9)が
装備されていて、運転中は同装置の固定磁石(8)を退
去させた状態で続行し、運転中止時には分離タンク
(2)の慣性回転中に同装置を操作して、固定磁石
(8)を同タンクに接近させると、振動磁石(6)が反
発し、振動薄板(7)を振動させ、留積微粒子を残留液
と共に濃縮液(二重実線)として同タンク外に廃棄する
機構を構成している。上記両機構の相乗効果による総対
的性能の向上を計った微粒子高性能遠心分離機。1. A forced sedimentation plate in a separation tank (2) supplied from a hollow rotary shaft (1) to synchronize the liquid to be separated (solid line in the figure) with the same tank until the same rotation. The tuned rotating mechanism, which is configured by equi-dispersing the tuned rotating plate (10) in (3), and the sediment accumulation particulates in the separation tank (2) are in contact with the entire inner wall of the tank and are located at the middle and high positions. A magnetic force discharging device which is piled up on a tangle-shaped vibrating thin plate (7) holding (6), but has a fixed magnet (8) in the main body (5) which has the same polarity as the vibrating magnet (6). (9) is installed, the operation is continued with the fixed magnet (8) of the device removed during operation, and when the operation is stopped, the device is operated and fixed during inertial rotation of the separation tank (2). When the magnet (8) approaches the tank, the vibrating magnet (6) repels and vibrates the vibrating thin plate (7). Constitute a mechanism for discarding out the tank Tomeseki particles as concentrates with retentate (double solid line). A high-performance fine particle centrifuge that improves the overall performance by the synergistic effect of the above two mechanisms.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33037999A JP2001113204A (en) | 1999-10-15 | 1999-10-15 | High-performance centrifugal separator for fine particle having synchronized rotation mechanism and magnetic discharge mechanism in separation tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33037999A JP2001113204A (en) | 1999-10-15 | 1999-10-15 | High-performance centrifugal separator for fine particle having synchronized rotation mechanism and magnetic discharge mechanism in separation tank |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2001113204A true JP2001113204A (en) | 2001-04-24 |
Family
ID=18231954
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33037999A Pending JP2001113204A (en) | 1999-10-15 | 1999-10-15 | High-performance centrifugal separator for fine particle having synchronized rotation mechanism and magnetic discharge mechanism in separation tank |
Country Status (1)
Country | Link |
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JP (1) | JP2001113204A (en) |
Cited By (12)
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WO2003041864A1 (en) * | 2001-11-15 | 2003-05-22 | Phase Inc. | System and method for creating vibrations in a centrifuge |
US6755969B2 (en) | 2001-04-25 | 2004-06-29 | Phase Inc. | Centrifuge |
US6805805B2 (en) | 2001-08-13 | 2004-10-19 | Phase Inc. | System and method for receptacle wall vibration in a centrifuge |
WO2005002734A3 (en) * | 2003-06-25 | 2005-05-26 | Phase Inc | Centrifuge with combinations of multiple features |
US7282147B2 (en) | 2003-10-07 | 2007-10-16 | Phase Inc. | Cleaning hollow core membrane fibers using vibration |
US7294274B2 (en) | 2003-07-30 | 2007-11-13 | Phase Inc. | Filtration system with enhanced cleaning and dynamic fluid separation |
US7320750B2 (en) | 2003-03-11 | 2008-01-22 | Phase Inc. | Centrifuge with controlled discharge of dense material |
US7371322B2 (en) | 2003-07-30 | 2008-05-13 | Phase Inc. | Filtration system and dynamic fluid separation method |
CN102527524A (en) * | 2012-01-19 | 2012-07-04 | 青岛诺凯达机械制造有限公司 | Automatic slag-discharging tube-type separator |
CN102941164A (en) * | 2012-11-28 | 2013-02-27 | 吴江市万事达环保溶剂有限公司 | Anti-vortex rotary drum used for centrifugal machine |
CN104307644A (en) * | 2014-08-26 | 2015-01-28 | 梧州市旺发新工艺品有限公司 | Gem degumming machine |
CN106733237A (en) * | 2016-12-30 | 2017-05-31 | 连云港双惠机械有限公司 | Centrifuge Cylinder Vibration automatic discharge unit |
-
1999
- 1999-10-15 JP JP33037999A patent/JP2001113204A/en active Pending
Cited By (16)
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US6755969B2 (en) | 2001-04-25 | 2004-06-29 | Phase Inc. | Centrifuge |
US6706180B2 (en) | 2001-08-13 | 2004-03-16 | Phase Inc. | System for vibration in a centrifuge |
US6805805B2 (en) | 2001-08-13 | 2004-10-19 | Phase Inc. | System and method for receptacle wall vibration in a centrifuge |
US6932913B2 (en) * | 2001-08-13 | 2005-08-23 | Phase Inc. | Method for vibration in a centrifuge |
WO2003041864A1 (en) * | 2001-11-15 | 2003-05-22 | Phase Inc. | System and method for creating vibrations in a centrifuge |
US7320750B2 (en) | 2003-03-11 | 2008-01-22 | Phase Inc. | Centrifuge with controlled discharge of dense material |
WO2005002734A3 (en) * | 2003-06-25 | 2005-05-26 | Phase Inc | Centrifuge with combinations of multiple features |
US6971525B2 (en) * | 2003-06-25 | 2005-12-06 | Phase Inc. | Centrifuge with combinations of multiple features |
US7335312B2 (en) | 2003-06-25 | 2008-02-26 | Phase Inc. | Centrifuge with combinations of multiple features |
US7294274B2 (en) | 2003-07-30 | 2007-11-13 | Phase Inc. | Filtration system with enhanced cleaning and dynamic fluid separation |
US7371322B2 (en) | 2003-07-30 | 2008-05-13 | Phase Inc. | Filtration system and dynamic fluid separation method |
US7282147B2 (en) | 2003-10-07 | 2007-10-16 | Phase Inc. | Cleaning hollow core membrane fibers using vibration |
CN102527524A (en) * | 2012-01-19 | 2012-07-04 | 青岛诺凯达机械制造有限公司 | Automatic slag-discharging tube-type separator |
CN102941164A (en) * | 2012-11-28 | 2013-02-27 | 吴江市万事达环保溶剂有限公司 | Anti-vortex rotary drum used for centrifugal machine |
CN104307644A (en) * | 2014-08-26 | 2015-01-28 | 梧州市旺发新工艺品有限公司 | Gem degumming machine |
CN106733237A (en) * | 2016-12-30 | 2017-05-31 | 连云港双惠机械有限公司 | Centrifuge Cylinder Vibration automatic discharge unit |
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