JPH0822395B2 - Continuous centrifuge - Google Patents
Continuous centrifugeInfo
- Publication number
- JPH0822395B2 JPH0822395B2 JP62091616A JP9161687A JPH0822395B2 JP H0822395 B2 JPH0822395 B2 JP H0822395B2 JP 62091616 A JP62091616 A JP 62091616A JP 9161687 A JP9161687 A JP 9161687A JP H0822395 B2 JPH0822395 B2 JP H0822395B2
- Authority
- JP
- Japan
- Prior art keywords
- ball
- conical
- washing
- cleaning
- 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 - Fee Related
Links
- 239000007787 solid Substances 0.000 claims description 49
- 239000007788 liquid Substances 0.000 claims description 45
- 238000004140 cleaning Methods 0.000 claims description 35
- 238000005406 washing Methods 0.000 claims description 35
- 239000012452 mother liquor Substances 0.000 claims description 13
- 230000002093 peripheral effect Effects 0.000 claims description 3
- 230000007246 mechanism Effects 0.000 claims description 2
- 230000000694 effects Effects 0.000 description 11
- 239000002245 particle Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 230000005484 gravity Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- -1 chlorine ions Chemical class 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012508 resin bead Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B15/00—Other accessories for centrifuges
- B04B15/12—Other accessories for centrifuges for drying or washing the separated solid particles
Landscapes
- Centrifugal Separators (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明はデカンター連続遠心分離機(以下「連続遠心
分離機」という。)内で固形物の洗浄を行うプール式固
形物洗浄型の連続遠心分離機に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a pool-type solid substance washing type continuous centrifuge for washing solid substances in a decanter continuous centrifuge (hereinafter referred to as "continuous centrifuge"). It concerns a separator.
連続遠心分離機は、固液分離を連続的、かつ能率良く
行うことができるため、広範囲に利用されている。Continuous centrifuges are widely used because they can perform solid-liquid separation continuously and efficiently.
しかし、この連続遠心分離機は、比重差による沈降分
離のため、固形物に付着している母液を洗浄液にて洗い
落とす、いわゆる固形物洗浄については、その洗浄効果
が他の濾過式の遠心分離機に比べて劣っているという欠
点があった。However, this continuous centrifuge removes the mother liquor adhering to the solid matter with a washing liquid because of sedimentation separation due to the difference in specific gravity.For so-called solid matter washing, the washing effect is that of another filtration type centrifuge. It had the disadvantage that it was inferior to.
ところで、連続遠心分離機における固形物の洗浄方法と
しては、脱液ゾーンまで運ばれてきた固形物に対して、
スクリューの回転中心部にある洗浄液孔より洗浄液を振
りかけることにより行っていた。By the way, as a method for washing solids in a continuous centrifuge, for solids that have been transported to the dewatering zone,
The cleaning liquid was sprinkled through the cleaning liquid hole at the center of rotation of the screw.
しかし、この方法には、次のような欠点があった。 However, this method has the following drawbacks.
洗浄液をすべての固形物に対してまんべんなく、か
つ均等に振りかけることができなかった。The washing solution was not evenly and evenly sprinkled on all solids.
個々の固形物について見ると、洗浄液によって固形
物の一部分は洗われるが、その固形物の全表面を洗浄液
が回って洗うことが困難であった。Looking at individual solids, a part of the solids was washed by the washing liquid, but it was difficult for the washing liquid to spin and wash the entire surface of the solids.
それでも、固形物粒子の粗いものは、洗浄液が粒子間
を通過しやすいため、粒子表面との接触がある程度なさ
れ、一応の洗浄効果が得られるが、均一で安定した洗浄
効果が得にくく、また細かい粒子においては、洗浄液が
粒子間を通る際の抵抗が大きく、そのため大部分の洗浄
液が固形層の表面を流れて、ほとんど洗浄効果を得るこ
とができなかった。Even so, when the solid particles are coarse, the cleaning liquid easily passes between the particles, so that the particles come into contact with the surface of the particles to some extent and a temporary cleaning effect is obtained, but it is difficult to obtain a uniform and stable cleaning effect, and fine particles are fine. With respect to the particles, the resistance of the cleaning liquid passing between the particles was large, and therefore most of the cleaning liquid flowed on the surface of the solid layer, and the cleaning effect could hardly be obtained.
このため、一般的に採られる固形物洗浄方法として、
一旦連続遠心分離機で分離排出された固形物を洗浄液タ
ンクで洗浄液と共に攪拌して再スラリー化し、再び連続
遠心分離機に供給して固液分離を行い、それによって均
一で安定した洗浄効果が得られるようにしていた。For this reason, as a commonly-used solid cleaning method,
The solid matter that was once separated and discharged by the continuous centrifuge is stirred with the washing solution in the washing solution tank to re-slurry it, and then supplied to the continuous centrifuge again for solid-liquid separation, thereby obtaining a uniform and stable washing effect. I was allowed to.
本発明は、洗浄液タンクで固形物洗浄を行うのでな
く、連続遠心分離機内で洗浄液タンクに相当する洗浄液
のプール部を作り、そのプール部に分離脱液された固形
物を連続的に浸漬させ、洗浄液タンクでの固形物洗浄と
同様な洗浄効果を与えるようにしたもの(以下プール式
固形物洗浄という)であり、ボールとスクリューを有
し、固形物洗浄のための洗浄液供給機構を備えた連続遠
心分離機において、固形物より母液を分離するための第
一円錐ボールと、固形物を洗浄するための第二円錐ボー
ルとを有し、第二円錐ボールの基端部の内径を第一円錐
ボールの先端部の内径よりも大きく形成するとともに第
二円錐ボールの先端部の内径を第一円錐ボールの先端部
の内径よりも小さく形成して第二円錐ボールの内周面と
第一円錐ボールの先端部の端面とで洗浄プールを形成
し、洗浄プールに供給された洗浄液を第一円錐ボール側
に越流させ、母液と共に排出するようにしたことを特徴
とする。The present invention does not wash the solids in the washing liquid tank, but creates a pool portion of the washing liquid corresponding to the washing liquid tank in the continuous centrifuge, and continuously immersing the separated and drained solids in the pool portion, It is designed to give a cleaning effect similar to that of cleaning solids in a cleaning liquid tank (hereinafter referred to as pool type solids cleaning), has a ball and a screw, and is equipped with a cleaning liquid supply mechanism for cleaning solids. In the centrifuge, the first cone ball for separating the mother liquor from the solid matter, and the second cone ball for washing the solid matter, the inner diameter of the base end of the second cone ball is the first cone The inner diameter of the tip of the second conical ball is made larger than the inner diameter of the tip of the second conical ball, and the inner diameter of the tip of the second conical ball is made smaller than the inner diameter of the tip of the first conical ball. Tip of Forming a cleaning pool between the end faces, was supplied to the washing pool washings were Yue flow to the first conical ball side, characterized in that so as to discharge with the mother liquor.
以下、本発明の連続遠心分離機を図示の実施例に基づ
いて説明する。Hereinafter, the continuous centrifuge of the present invention will be described based on the illustrated embodiments.
図において1は円筒ボール、2はこの円筒ボール1の
先端内周部に形成される第一円錐ボール、3は前記円筒
ボール1の先端に、しかも第一円錐ボール2よりも前方
に突出する如く形成される第二円錐ボールで、この円筒
ボール1、第一、第二円筒ボール2,3により所要形状の
ボール4を形成するとともに、このボール4内にボール
4と同心で、わずかな差をもって回転する円筒スクリュ
ー5と、この円筒スクリュー5の先端側に突設させた円
筒スクリュー6とよりなるスクリュー7を嵌入し、かつ
ボール4及びスクリュー7はギヤーユニット8を介して
プーリ9及び10にて高速回転するようになっている。In the drawing, 1 is a cylindrical ball, 2 is a first conical ball formed on the inner peripheral portion of the tip of the cylindrical ball 1, and 3 is at the tip of the cylindrical ball 1 and projects further forward than the first conical ball 2. With the second conical ball formed, the cylindrical ball 1, the first and second cylindrical balls 2 and 3 form a ball 4 of a required shape, and the ball 4 is concentric with the ball 4 and has a slight difference. A screw 7 composed of a rotating cylindrical screw 5 and a cylindrical screw 6 projecting from the distal end side of the cylindrical screw 5 is inserted, and the balls 4 and the screws 7 are attached to pulleys 9 and 10 via a gear unit 8. It is designed to rotate at high speed.
また、前記スクリュー7の円筒スクリュー5内には駆
動側と反対側より洗浄パイプ19及びこの洗浄パイプ内に
嵌挿された給液パイプ12が挿入される。A washing pipe 19 and a liquid supply pipe 12 fitted in the washing pipe are inserted into the cylindrical screw 5 of the screw 7 from the side opposite to the driving side.
しかして、同心的に配設されたボール4とスクリュー
7とがわずかな差をもって、しかも高速回転するが、こ
の高速回転時、スラリーは給液口11より給液パイプ12を
通り、スクリュー7の給液室13に供給され、さらに給液
吐出口14よりボール4の内に円筒スクリューとの間に形
成された母液プール15に供給されて高い遠心力を受け
る。Then, the balls 4 and the screw 7 arranged concentrically rotate at a high speed with a slight difference, and at the time of this high speed rotation, the slurry passes from the liquid supply port 11 through the liquid supply pipe 12 and passes through the screw 7 The liquid is supplied to the liquid supply chamber 13 and further supplied from the liquid supply outlet 14 to the mother liquor pool 15 formed between the ball 4 and the cylindrical screw to receive a high centrifugal force.
これにより、液より比重の重い固形物dは、ボール4
の内壁に押し付けられ、その内側にリング状の液層を形
成する。As a result, the solid matter d having a higher specific gravity than the liquid is
It is pressed against the inner wall of and forms a ring-shaped liquid layer inside it.
分離された固形物dは、スクリュー7により第一円錐
ボール2の先端部に搬送され、堰板16によって規制され
る液面eよりさらに内径側の脱液ゾーン17で母液を振り
切り、分離脱液される。The separated solid d is conveyed to the tip of the first conical ball 2 by the screw 7, and the mother liquor is shaken off in the liquid removal zone 17 on the inner diameter side of the liquid level e regulated by the weir plate 16 to separate and drain the liquid. To be done.
一方、分離された母液は堰板16よりオーバーフローし
て機外へ排出される。On the other hand, the separated mother liquor overflows from the dam plate 16 and is discharged to the outside of the machine.
固形物dを洗浄するための洗浄液は洗浄口18より洗浄
パイプ19を通じてスクリュー7の洗浄液室20に供給さ
れ、1個、又は2個以上の洗浄液吐出穴21により、第二
円錐ボール3の基端部の内径を第一円錐ボール2の先端
部の内径よりも大きく形成するとともに第二円錐ボール
3の先端部の内径を第一円錐ボール2の先端部の内径よ
りも小さく形成することにより第二円錐ボール3の内周
面と第一円錐ボール2の先端部の端面とで形成した洗浄
プール22に供給される。The cleaning liquid for cleaning the solids d is supplied from the cleaning port 18 to the cleaning liquid chamber 20 of the screw 7 through the cleaning pipe 19, and one or more cleaning liquid discharge holes 21 are provided to the base end of the second conical ball 3. By forming the inner diameter of the portion larger than the inner diameter of the tip portion of the first conical ball 2 and the inner diameter of the tip portion of the second conical ball 3 smaller than the inner diameter of the tip portion of the first conical ball 2, It is supplied to the cleaning pool 22 formed by the inner peripheral surface of the conical ball 3 and the end surface of the tip of the first conical ball 2.
脱液ゾーン17で分離脱液された固形物dは洗浄液で占
められている洗浄プール22に流入して洗浄液に浸漬し、
スクリュー7の固形物搬送の際の攪拌作用と相まって固
形物粒子表面に付着している母液が希釈洗浄される。The solid matter d separated and deliquored in the deliquoring zone 17 flows into the washing pool 22 occupied by the washing liquid and is immersed in the washing liquid,
The mother liquor adhering to the surface of the solid particles is diluted and washed together with the stirring action of the screw 7 during the transportation of the solid material.
引き続き固形物dはスクリュー7によって第二円錐ボ
ール3の先端部側に搬送され、第一円錐ボール2の先端
部によって規制される液面fよりさらに内径側の洗浄脱
液ゾーン23で洗浄液を振り切り、第二円錐ボール3の固
形物吐出口24より機外へ排出される。Subsequently, the solid matter d is conveyed to the tip side of the second conical ball 3 by the screw 7, and the washing liquid is shaken off in the washing and dewatering zone 23 on the inner diameter side of the liquid level f regulated by the tip of the first conical ball 2. The solid particles are discharged from the solid cone discharge port 24 of the second conical ball 3 to the outside of the machine.
一方、分離された洗浄液は、脱液ゾーン17を通り、母
液プール15へ越流し、そのためスクリュー7によって搬
送されてくる固形物と接触して予備的に固形物を洗浄す
る。On the other hand, the separated cleaning liquid passes through the dewatering zone 17 and overflows into the mother liquor pool 15, so that the cleaning liquid comes into contact with the solid matter conveyed by the screw 7 to preliminarily wash the solid matter.
第2図は、連続遠心分離機の固形物の洗浄原理を示す
説明図である。FIG. 2 is an explanatory view showing the principle of washing solids in a continuous centrifuge.
次に本発明のプール型の連続遠心分離機と従来型(洗
浄液吐出孔から適切な箇所より洗浄液を直接固形物に振
りかけて洗浄を行う方式)の連続遠心分離機との固形物
の洗浄効果の比較を第1表に示す。Next, the effect of washing the solid matter between the pool type continuous centrifuge of the present invention and the conventional type (a method in which the washing liquid is directly sprinkled onto the solid matter from the washing liquid discharge hole to wash the solid matter) The comparison is shown in Table 1.
処理条件として処理物が固形物濃度50重量%の樹脂ビ
ーズスラリー760l/Hrにて各々の連続遠心分離機に供給
し、固形物洗浄液として、純水を280l/Hrにて供給した
ものである。As treatment conditions, the treated material was supplied to each continuous centrifuge in a resin bead slurry 760 l / Hr having a solid concentration of 50% by weight, and pure water was supplied at 280 l / Hr as a solid washing liquid.
第1表からも明らかなように、従来型より本発明のプ
ール型の連続遠心分離機の方が固形物の洗浄効果が数段
優れており、そのメリットとして固形物の製品純度が上
がり、また洗浄液タンクが不要になり、特に固形物の乾
燥工程において塩素イオンによる腐食が大幅に押さえら
れることにより、経済的効果が著しく上がることにな
る。 As is clear from Table 1, the pool-type continuous centrifuge of the present invention is several times superior to the conventional type in the washing effect of solids, and as a merit, the product purity of solids is increased. The cleaning liquid tank becomes unnecessary, and corrosion due to chlorine ions is greatly suppressed particularly in the drying process of solids, so that the economical effect is remarkably improved.
本発明によれば、第一円錐ボールにおいて母液と分離
した固形物を第二円錐ボール3の洗浄プール内で洗浄す
ることができ、さらに、洗浄プールに供給された洗浄液
を第一円錐ボール側に越流させ、固形物を母液プール内
で予備的に洗浄することができる。このため、固形物の
洗浄効果が優れ、固形物の製品純度を向上することがで
きるとともに、洗浄液タンクが不要となり、設備費が低
減できる等の利点を有する。According to the present invention, the solid matter separated from the mother liquor in the first conical ball can be washed in the cleaning pool of the second conical ball 3, and further the cleaning liquid supplied to the cleaning pool can be transferred to the first conical ball side. Overflow and solids can be preliminarily washed in the mother liquor pool. Therefore, there are advantages that the cleaning effect of the solid matter is excellent, the product purity of the solid matter can be improved, the cleaning liquid tank becomes unnecessary, and the facility cost can be reduced.
第1図は本発明の一実施例を示す要部全体断面図、第2
図は第1図のプール型固形物洗浄部の拡大断面図であ
る。 1は円筒ボール、2は第一円錐ボール、3は第二円筒ボ
ール、4はボール、7はスクリュー、15は母液プール、
16は堰板、22は洗浄プール、dは固形物、eは液面、f
は液面。FIG. 1 is an overall sectional view of an essential part showing an embodiment of the present invention, FIG.
The figure is an enlarged cross-sectional view of the pool type solid matter cleaning unit of FIG. 1 is a cylindrical ball, 2 is a first conical ball, 3 is a second cylindrical ball, 4 is a ball, 7 is a screw, 15 is a mother liquor pool,
16 is a barrier plate, 22 is a washing pool, d is a solid matter, e is a liquid surface, f
Is the liquid level.
Claims (1)
ための洗浄液供給機構を備えた連続遠心分離機におい
て、固形物より母液を分離するための第一円錐ボール
(2)と、固形物を洗浄するための第二円錐ボール
(3)とを有し、第二円錐ボール(3)の基端部の内径
を第一円錐ボール(2)の先端部の内径よりも大きく形
成するとともに第二円錐ボール(3)の先端部の内径を
第一円錐ボール(2)の先端部の内径よりも小さく形成
して第二円錐ボール(3)の内周面と第一円錐ボール
(2)の先端部の端面とで洗浄プール(22)を形成し、
洗浄プール(22)に供給された洗浄液を第一円錐ボール
(2)側に越流させ、母液と共に排出するようにしたこ
とを特徴とする連続遠心分離機。A first conical ball (2) for separating a mother liquor from a solid in a continuous centrifuge having a cleaning liquid supply mechanism for washing a solid, which has a ball and a screw, and a solid. And a second conical ball (3) for cleaning the second conical ball (3), the inner diameter of the base end of the second conical ball (3) is formed larger than the inner diameter of the tip of the first conical ball (2), and The inner diameter of the tip of the two conical balls (3) is made smaller than the inner diameter of the tip of the first conical balls (2) so that the inner peripheral surface of the second conical balls (3) and the first conical balls (2) are A cleaning pool (22) is formed with the end face of the tip,
A continuous centrifuge characterized in that the washing liquid supplied to the washing pool (22) is allowed to flow toward the first conical ball (2) side and is discharged together with the mother liquor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62091616A JPH0822395B2 (en) | 1987-04-14 | 1987-04-14 | Continuous centrifuge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62091616A JPH0822395B2 (en) | 1987-04-14 | 1987-04-14 | Continuous centrifuge |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63256152A JPS63256152A (en) | 1988-10-24 |
| JPH0822395B2 true JPH0822395B2 (en) | 1996-03-06 |
Family
ID=14031504
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62091616A Expired - Fee Related JPH0822395B2 (en) | 1987-04-14 | 1987-04-14 | Continuous centrifuge |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0822395B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4132593A1 (en) * | 1991-09-30 | 1993-04-01 | Linde Kca Dresden Gmbh | REACTOR FOR COUNTERFLOW TREATMENT OF SOLID AND LIQUID |
| JP4518531B2 (en) * | 2001-09-27 | 2010-08-04 | 孝治 大塚 | Rinse decanter |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58124244U (en) * | 1982-02-19 | 1983-08-24 | 三菱重工業株式会社 | Multi-stage separation/washing centrifuge |
-
1987
- 1987-04-14 JP JP62091616A patent/JPH0822395B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63256152A (en) | 1988-10-24 |
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