JPS6242664B2 - - Google Patents

Info

Publication number
JPS6242664B2
JPS6242664B2 JP54022427A JP2242779A JPS6242664B2 JP S6242664 B2 JPS6242664 B2 JP S6242664B2 JP 54022427 A JP54022427 A JP 54022427A JP 2242779 A JP2242779 A JP 2242779A JP S6242664 B2 JPS6242664 B2 JP S6242664B2
Authority
JP
Japan
Prior art keywords
cylindrical body
solids
cylinder
overflow weir
extending radially
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
JP54022427A
Other languages
Japanese (ja)
Other versions
JPS55114361A (en
Inventor
Yasuo Kuwamoto
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP2242779A priority Critical patent/JPS55114361A/en
Publication of JPS55114361A publication Critical patent/JPS55114361A/en
Publication of JPS6242664B2 publication Critical patent/JPS6242664B2/ja
Granted legal-status Critical Current

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  • Physical Water Treatments (AREA)
  • Centrifugal Separators (AREA)

Description

【発明の詳細な説明】 本発明は遠心濃縮機に関するもので、下水処理
施設等から生ずる汚泥の如き固形物を含む原液を
固形物と清澄水とに分離する際に、固形物の回収
率を向上させることを目的とする。
Detailed Description of the Invention The present invention relates to a centrifugal concentrator, which improves the recovery rate of solids when separating a raw solution containing solids such as sludge generated from sewage treatment facilities into solids and clear water. The purpose is to improve.

従来、このような目的に用いる装置としては、
固形物を遠心濃縮する回転筒体は径が一定の一段
式のものであり固形物の分離は十分でなく清澄水
に一部固形物が逸失するのが現状であつた。
Conventionally, devices used for this purpose include:
The rotating cylinder for centrifugally concentrating solids is a single-stage type with a constant diameter, and the separation of solids is not sufficient, and some of the solids are lost to clear water.

本発明は清澄度を向上させるために固形物を遠
心濃縮する回転筒体を小径の筒体と大径の筒体と
を接続した二段式の回転筒体とし、小径の筒体で
固形物が分離された清澄度がまだ不十分な清澄水
を大径の筒体に流入させて、より大きな遠心力を
与え十分な固形物の回収が得られるようにしたも
のである。
In order to improve the clarity, the present invention uses a two-stage rotary cylinder for centrifugally concentrating solids by connecting a small-diameter cylinder and a large-diameter cylinder. The clarified water, which has been separated and whose clarity is still insufficient, is made to flow into a large-diameter cylindrical body to apply a larger centrifugal force and to obtain sufficient recovery of solids.

以下本発明の実施例を図面に基づいて説明す
る。第1図において、第1の筒体1は軸心回りに
回転自在に設けられており、その一端2には径方
向内側に延びる壁板3が設けられ、他端4には径
方向外側に向う壁板5が設けられている。第2の
筒体6は第1の筒体1よりも大径に形成され、そ
の一端7は前記壁板5に接続されている。また第
1の筒体1の他端4には径方向内側に延びる第1
の越流堰8が設けられ、第2の筒体6の他端9に
は径方向内側に延びかつ前記第1の越流堰8より
も大径の第2の越流堰10が設けられている。1
2は第1の筒体1の底部近くに挿入された原液供
給管であり、13は第1の筒体1の濃縮固形物排
出管であり、14は第2の筒体6の濃縮固形物排
出管である。
Embodiments of the present invention will be described below based on the drawings. In FIG. 1, a first cylindrical body 1 is rotatably provided around its axis, and a wall plate 3 extending radially inward is provided at one end 2, and a wall plate 3 extending radially outward is provided at the other end 4. A facing wall plate 5 is provided. The second cylindrical body 6 is formed to have a larger diameter than the first cylindrical body 1, and one end 7 thereof is connected to the wall plate 5. Further, at the other end 4 of the first cylindrical body 1, a first tube extending inward in the radial direction is provided.
A second overflow weir 8 is provided at the other end 9 of the second cylindrical body 6, and a second overflow weir 10 that extends radially inward and has a larger diameter than the first overflow weir 8 is provided. ing. 1
2 is a stock solution supply pipe inserted near the bottom of the first cylinder 1, 13 is a concentrated solids discharge pipe of the first cylinder 1, and 14 is a concentrated solids discharge pipe of the second cylinder 6. It is a discharge pipe.

そこで原液供給管12から供給された原液は第
1の筒体1によつて遠心力が与えられ固形物Aは
分離して筒体1壁に堆積する。一方固形物が分離
した清澄水Bは固形物の分離が完全なものでな
く、一部固形物が含まれたまゝ越流堰8から流出
して第2の筒体6内に流入する。第3図は遠心力
と固形物の回収率の関係を示すグラフである。そ
こで第1の筒体1で逸失した固形物は第2の筒体
6によつて遠心力は半径の大きさに比例するから
第1の筒体1のときよりも大きな遠心力を受け
て、更に固形物Cが分離され、全体として非常に
高い固形物回収率が得られ清澄水Dの清澄度は向
上する。そして清澄水Dは越流堰10から系外に
流出する。一方固形物A,Cはそれぞれ排出管1
3,14によつて吸引され、筒体1,6外に排出
される。なおこのときの第1の筒体1と第2の筒
体6の容量は各筒体1,6において回収される固
形物の量に比例した大きさであればよい。それ故
第1の筒体1で大部分の固形物が回収されるか
ら、第2の筒体6の容量は第1の筒体1より可成
り小さくてよく、従つて合理的な固形物の回収が
得られる。また排出管14は必ずしも設ける必要
がなく、排出管13によつて第2の筒体6内の固
形物Cを排出することが出来る。
The stock solution supplied from the stock solution supply pipe 12 is subjected to centrifugal force by the first cylinder 1, and the solids A are separated and deposited on the wall of the cylinder 1. On the other hand, the clear water B from which the solids have been separated does not completely separate the solids, and flows out of the overflow weir 8 and into the second cylindrical body 6 while still containing some solids. FIG. 3 is a graph showing the relationship between centrifugal force and solid matter recovery rate. Therefore, the solid matter lost in the first cylinder 1 is subjected to a larger centrifugal force by the second cylinder 6 than in the first cylinder 1, since the centrifugal force is proportional to the size of the radius. Further, the solid matter C is separated, a very high solid matter recovery rate is obtained as a whole, and the clarity of the clear water D is improved. The clear water D then flows out of the system from the overflow weir 10. On the other hand, solids A and C are each discharge pipe 1.
3 and 14, and is discharged outside the cylinders 1 and 6. Note that the capacities of the first cylindrical body 1 and the second cylindrical body 6 at this time may be of a size proportional to the amount of solids collected in each of the cylindrical bodies 1 and 6. Therefore, since most of the solids are recovered in the first cylinder 1, the capacity of the second cylinder 6 can be considerably smaller than that of the first cylinder 1, and therefore a reasonable solids Recovery is obtained. Further, the discharge pipe 14 is not necessarily provided, and the solid matter C in the second cylinder body 6 can be discharged by the discharge pipe 13.

第2図は本発明による他の実施例を示したもの
である。第1図の場合と比較し、第1の筒体1と
第2の筒体6とは天地を逆にして設置したもので
あり、原液供給管13から供給された原液は筒体
16の回転軸16の頂部に取付けた円板17の上
に落ちて遠心力が与えられて第1の筒体1の周壁
に移行し、第1図の場合と同様に固形物が遠心濃
縮される。また第1図、第2図に示したものは軸
心が鉛直方向に設置された竪型であるが、軸心を
水平方向にした横型であつても同様の効果が得ら
れる。
FIG. 2 shows another embodiment according to the invention. Compared to the case shown in FIG. 1, the first cylindrical body 1 and the second cylindrical body 6 are installed upside down, and the undiluted solution supplied from the undiluted solution supply pipe 13 is rotated by the rotation of the cylindrical body 16. The solids fall onto a disk 17 attached to the top of the shaft 16 and are transferred to the peripheral wall of the first cylindrical body 1 due to centrifugal force, whereupon the solids are centrifugally concentrated as in the case of FIG. Further, although what is shown in FIGS. 1 and 2 is a vertical type with the axis set in the vertical direction, the same effect can be obtained even if it is a horizontal type with the axis set in the horizontal direction.

本発明は以上の説明から明らかのように、原液
中に含まれる固形物を遠心分離する回転筒体を小
径の筒体と大径の筒体を接続した2段式にすると
ともに、小径の筒体に原液を供給するようにし
て、小径筒体で回収できず逸失した固形物は大径
の筒体で大きな遠心力を与えて回収するものであ
るから非常に高い固形物の回収率が得られる。
As is clear from the above description, the present invention uses a two-stage rotary cylinder for centrifuging the solids contained in the stock solution, in which a small-diameter cylinder and a large-diameter cylinder are connected. By supplying the undiluted solution to the body, the solids that cannot be recovered by the small-diameter cylinder are collected by applying a large centrifugal force to the large-diameter cylinder, so a very high solids recovery rate can be achieved. It will be done.

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

第1図は本発明の遠心濃縮機の一実施例を示す
縦断面図、第2図は本発明の他の例を示す遠心濃
縮機の縦断面図、第3図は遠心力と固形物の回収
率を示すグラフである。 1……第1の筒体、3,5……壁板、6……第
2の筒体、8……第1の越流堰、10……第2の
越流堰。
Fig. 1 is a longitudinal cross-sectional view showing one embodiment of the centrifugal concentrator of the present invention, Fig. 2 is a longitudinal cross-sectional view of a centrifugal concentrator showing another example of the present invention, and Fig. 3 is a longitudinal cross-sectional view showing centrifugal force and solid matter. It is a graph showing recovery rate. 1... First cylindrical body, 3, 5... Wall plate, 6... Second cylindrical body, 8... First overflow weir, 10... Second overflow weir.

Claims (1)

【特許請求の範囲】[Claims] 1 軸心回りに回転自在な第1の筒体の一端に径
方向内側に延びる壁板を設けると共に他端に径方
向外側に向う壁板を介して前記筒体より大径の第
2の筒体の一端を接続し、前記第1の筒体の他端
に径方向内側に延びる第1の越流堰を設け、前記
第2の筒体の他端に径方向内側に延びかつ前記第
1の越流堰よりも大径の第2の越流堰を設け、前
記第1の筒体の内部に、この第1の筒体内に原液
を供給可能な原液供給管を挿入したことを特徴と
する遠心濃縮機。
1. A first cylindrical body rotatable about its axis is provided with a wall plate extending radially inward at one end, and a second cylindrical body having a larger diameter than the cylindrical body is provided at the other end with a wall plate extending radially outward. a first overflow weir extending radially inward at the other end of the first cylindrical body, and a first overflow weir extending radially inward at the other end of the second cylindrical body A second overflow weir having a larger diameter than the overflow weir is provided, and a concentrate supply pipe capable of supplying the concentrate into the first cylinder is inserted into the first cylinder. centrifugal concentrator.
JP2242779A 1979-02-26 1979-02-26 Centrifugal enricher Granted JPS55114361A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2242779A JPS55114361A (en) 1979-02-26 1979-02-26 Centrifugal enricher

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2242779A JPS55114361A (en) 1979-02-26 1979-02-26 Centrifugal enricher

Publications (2)

Publication Number Publication Date
JPS55114361A JPS55114361A (en) 1980-09-03
JPS6242664B2 true JPS6242664B2 (en) 1987-09-09

Family

ID=12082384

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2242779A Granted JPS55114361A (en) 1979-02-26 1979-02-26 Centrifugal enricher

Country Status (1)

Country Link
JP (1) JPS55114361A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6070125B2 (en) * 2012-12-04 2017-02-01 株式会社Ihi Solid-liquid separation method and apparatus
JP6070124B2 (en) * 2012-12-04 2017-02-01 株式会社Ihi Solid-liquid separation method and apparatus

Also Published As

Publication number Publication date
JPS55114361A (en) 1980-09-03

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