JPS6039426B2 - centrifugal dehydrator - Google Patents
centrifugal dehydratorInfo
- Publication number
- JPS6039426B2 JPS6039426B2 JP101577A JP101577A JPS6039426B2 JP S6039426 B2 JPS6039426 B2 JP S6039426B2 JP 101577 A JP101577 A JP 101577A JP 101577 A JP101577 A JP 101577A JP S6039426 B2 JPS6039426 B2 JP S6039426B2
- Authority
- JP
- Japan
- Prior art keywords
- casing
- screw
- rear end
- main body
- outlet
- 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
Links
Landscapes
- Centrifugal Separators (AREA)
Description
【発明の詳細な説明】
本発明は水処理施設における汚水の脱水等の目的に用い
る遠心脱水機に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a centrifugal dehydrator used for purposes such as dehydration of sewage in water treatment facilities.
従来の横型の遠心脱水機は前端が細く後端が大径となっ
たテーパ部を前半に形成した円筒状ケーシングとこのケ
ーシングの内側に若干の間隙を存して同心に配置したケ
ーシングとほぼ同形の本体の外側に螺旋状の羽根を設け
たスクリューとから成り、これらケーシングとスクリュ
ーとを若干の速度差をもって高速回転させ、スクリュー
の後部中心から流入せしめた汚水をスクリューのテーパ
部の大蓬側の外側へ流入させて遠D力により分離した固
形物はスクリューの送り作用によりケーシングの前端の
固形物出口から排出させ、分離した脱離液はケーシング
の後端に形成した脱離水出口より排出せしめるようにし
たものである。しかし、このような方式の脱水機はよく
検討すると固形物の脱水作用について問題がある。この
問題を分り易くするため遠心作用を除き、そのかわりに
重力沈降により固形物を分離する装置に置きかえて説明
すると第1図のようになる。第1図では1が分離槽でそ
の底部の前半は、前部が高い傾斜部2となり、後半が平
面部3となっている。又、無端チェン4にスクレーパ5
を一定間隔で取付けた固形物掻出機Cを傾斜部2と平面
部3に沿って配置し、沈降した固形物6は槽1の前部の
固形物出口8より排出し、脱離水7は後部の脱離水出口
9より排出するようになっている。この場合、問題にな
るのは一たん平面部3上に沈降した最も濃い固形物が矢
印方向に動〈掻出機Cにより、傾斜部2上を移動する間
に再び水と混合することにより含水率が高まることであ
る。このような問題を解決できるものとして第2図に示
すように槽11の底部に固形物の引抜管12を設け、沈
降した固形物は底部から引抜き、上燈水は上部の上燈水
引抜管13から排出するようにすれば固形物の含水率が
高まることはない。しかして前記した遠心脱水機は第1
図の分離槽1をその前後方向の水平線を軸として回転体
とし、掻出機Cをスクリューとしたものに当たるのであ
る。本発明はこのような問題に鑑みて、第2図のものを
遠心脱水機に応用するものであるが、その詳細を説明す
れば次の通りである。図において、21は横軸であり、
Aはこの横軸21の外側に回敷自在に装置した同Dのケ
ーシングで、その後端部22は4・径となり軸21の外
側に回動自在に鉄合している。A conventional horizontal centrifugal dewatering machine has a cylindrical casing with a tapered part formed in the front half with a narrow front end and a large diameter rear end, and a casing arranged concentrically with a slight gap inside this casing, which is almost the same shape. The casing and screw are rotated at high speed with a slight speed difference, and the sewage that flows in from the center of the rear of the screw is transferred to the large side of the tapered part of the screw. The solids flowed outside and separated by the far-D force are discharged from the solids outlet at the front end of the casing by the feeding action of the screw, and the separated desorbed liquid is discharged from the desorbed water outlet formed at the rear end of the casing. This is how it was done. However, upon careful consideration of this type of dehydrator, there are problems with the dehydration effect on solid materials. In order to make this problem easier to understand, we will remove the centrifugal action and replace it with a device that separates solids by gravity sedimentation, as shown in Figure 1. In FIG. 1, reference numeral 1 denotes a separation tank, and the first half of its bottom is a sloped part 2 with a high front part, and a flat part 3 in the second half. Also, a scraper 5 is attached to the endless chain 4.
A solid material scraper C, which is attached at regular intervals, is arranged along the inclined part 2 and the flat part 3, and the settled solid material 6 is discharged from the solid material outlet 8 at the front of the tank 1, and the desorbed water 7 is It is designed to be discharged from the desorbed water outlet 9 at the rear. In this case, the problem is that once the thickest solids have settled on the flat surface 3, they move in the direction of the arrow. This means that the rate will increase. As a solution to this problem, a solid matter drawing pipe 12 is provided at the bottom of the tank 11 as shown in FIG. If the solids are discharged from the tank, the moisture content of the solids will not increase. However, the centrifugal dehydrator mentioned above is the first
This corresponds to a system in which the separation tank 1 shown in the figure is a rotating body with the horizontal line in the longitudinal direction as an axis, and the scraper C is a screw. In view of these problems, the present invention applies the device shown in FIG. 2 to a centrifugal dehydrator, and the details thereof will be explained as follows. In the figure, 21 is the horizontal axis,
A is a casing of the same type D that is installed on the outside of the horizontal shaft 21 so as to be freely rotatable, and the rear end portion 22 has a diameter of 4 mm and is rotatably fitted on the outside of the shaft 21.
又、小径の前端部23も軸21の外側に回動自在に鉄合
し、中央部24は大径となり、その前後はほぼテーパ状
となっている。BはケーシングA内の前半部に配置され
、軸21に前端部を固定したスクリューで、ケーシング
Aの前半部内面に対して適当な間隙を存して沿うほぼテ
ーパ状で後部が開放された中空の本体25とその外側に
形成した複数の螺旋状の羽根26とから成っている。こ
の羽根26は第4図のようにスクリューBの回転方向を
示す矢印aの方向に向けて前端から後方に螺旋状に形成
したもので、ケーシングAはスクリューBと同方向に若
干遅れて回転することにより、ケーシングAの内面の固
形物30を第4図の矢印のような分力で中心部、即ちス
クリューBの前方の方へ掻寄せる作用を行うものである
。又、ケーシングAの後端部22に近い部分に脱離水出
口27、前端部23には固形物出口28が形成されてい
る。 更に前記軸21は前端を閉鎖した中空で、その後
端には汚水供給管(図示省略)を回転懐手を介して連結
し、軸21の前部におけるスクリューBの内側に汚水出
口29を形成する。本発明は上記の構成であり、適宜の
駆動機構により、ケーシングA及びスクリュWBを若干
の速度差をもって第4図の矢印方向に駆動しつつ軸21
内に汚水を供給し、出口29からスクリューB内に放出
する。Further, the small-diameter front end portion 23 is rotatably fitted to the outside of the shaft 21, and the central portion 24 has a large diameter, and the front and rear portions thereof are substantially tapered. B is a screw that is placed in the front half of the casing A and whose front end is fixed to the shaft 21, and is a hollow screw with an approximately tapered shape and an open rear end that runs along the inner surface of the front half of the casing A with an appropriate gap. It consists of a main body 25 and a plurality of spiral blades 26 formed on the outside thereof. As shown in Fig. 4, this blade 26 is spirally formed from the front end toward the rear in the direction of arrow a indicating the rotation direction of screw B, and casing A rotates in the same direction as screw B with a slight delay. As a result, the solid matter 30 on the inner surface of the casing A is scraped toward the center, that is, toward the front of the screw B by a component force as indicated by the arrow in FIG. Further, a desorbed water outlet 27 is formed in a portion near the rear end portion 22 of the casing A, and a solid matter outlet 28 is formed in the front end portion 23. Further, the shaft 21 is hollow with a closed front end, and a sewage supply pipe (not shown) is connected to the rear end via a rotating pocket, and a sewage outlet 29 is formed inside the screw B at the front of the shaft 21. The present invention has the above-mentioned configuration, and while driving the casing A and the screw WB in the direction of the arrow in FIG. 4 with a slight speed difference using an appropriate drive mechanism, the shaft 21
Sewage is supplied into the screw B and discharged into the screw B through the outlet 29.
この汚水は旋回しつつスクリューBの本体25の内面に
沿って後方に流れ遠心力により固形物3川まケーシング
Aの中央部24の内面に沿った状態となり脱離水31は
脱離水出口27より排出される。中央部24の内面に沿
った固形物301ま羽根26によりケ−シングAの前半
の7ーパ面に沿って移動し、固形物出口から排出される
。尚、ケーシングAとスクリューBの回転はスクリュー
Bによる固形物の引抜速度によって可変される。This waste water flows backward along the inner surface of the main body 25 of the screw B while swirling, and due to centrifugal force, the solids 3 flow along the inner surface of the central part 24 of the casing A, and the desorbed water 31 is discharged from the desorbed water outlet 27. be done. The solids 301 along the inner surface of the central portion 24 are moved along the front half surface of the casing A by the blades 26, and are discharged from the solids outlet. Note that the rotation of the casing A and the screw B is varied depending on the speed at which the solid material is pulled out by the screw B.
即ち、固形物の引抜速度は入口速度C,よりも出口速度
C2が大きい。つまりC4−C2>0になるようにスク
リューBの形状が計算される。丁度ボリュートポンプの
逆回転における状態で羽根26の入口、出口角度がポン
プの中心側、外側の入射角出口角となり、このスクリュ
ーでは外側、中心側と逆になっている。従って.Hth
皿亥(u亭−帆十(C亭−C室)十(Wu喜一V協)}
>○即ちu≧−u妻>0であるから
C≧−C毒+W≧−V鷹>u亭−u室‘こなるような設
計曲線が必要となる。That is, as for the drawing speed of the solid material, the exit speed C2 is higher than the inlet speed C. In other words, the shape of the screw B is calculated so that C4-C2>0. Just when the volute pump is in reverse rotation, the inlet and outlet angles of the vanes 26 become the center side and the outer side of the pump, the incident angle and the outlet angle, and in this screw, the outer side and the center side are opposite. Therefore. Hth
Plate (U-tei-Hoju (C-tei-C room) Ju (Wu Kiichi V-kyo))
>○, that is, u≧-u wife>0, so a design curve such that C≧-C poison+W≧-V hawk>u-tei-u-room is required.
本発明は上記のようにケーシングAやスクIJューBの
形状を特殊なものとすることにより遠心力で分離された
固形物を水中を通すことなく排出できる。In the present invention, by making the casing A and the screw IJ B into special shapes as described above, solids separated by centrifugal force can be discharged without passing through water.
即ち、第2図の沈殿方式を遠心方式に応用したことにな
り、しかも汚水は中空の機軸内を通って本体の内側前部
の最も径の小さい部分に開□している汚水出口から本体
内に排出されるので、汚水は本体の全長に亘つて十分な
遠心分離作用を受けることになる。従って、従来の遠心
脱水機よりも遥かに脱水効果のよいものが得られる特徴
を有するものである。In other words, the sedimentation method shown in Figure 2 has been applied to the centrifugal method, and the wastewater passes through the hollow machine shaft and enters the main body from the wastewater outlet that opens at the smallest diameter part at the front inside of the main body. Therefore, the waste water is subjected to sufficient centrifugal separation over the entire length of the main body. Therefore, it has the feature of providing a much better dehydration effect than conventional centrifugal dehydrators.
第1図、第2図は沈降式分離槽の各例を示す縦断側面図
、第3図は本発明遠心脱水機の縦断側面図、第4図は同
上の正面図である。
A…ケーシング、B…スクリュー、21…横軸、22…
後端部、23…前端部、24…中央部、25・・・本体
、26・・・羽根、27・・・脱離水出口、28・・・
固形物出口、29・・・汚水出口。
第1図第2図
第3図
第4図1 and 2 are longitudinal sectional side views showing examples of sedimentation type separation tanks, FIG. 3 is a longitudinal sectional side view of the centrifugal dehydrator of the present invention, and FIG. 4 is a front view of the same. A...Casing, B...Screw, 21...Horizontal shaft, 22...
Rear end, 23...front end, 24...center, 25...main body, 26...blade, 27...separated water outlet, 28...
Solids outlet, 29...sewage outlet. Figure 1 Figure 2 Figure 3 Figure 4
Claims (1)
該ケーシング内において該ケーシングと同心で該ケーシ
ングと若干の速度差をもつて同方向に回転するスクリユ
ーとから成り、該ケーシングは後端部及び前端部が小径
で中央部に向かいテーパ状となり、中央部を大径とし、
且つ後端部に脱離水出口、前端に固形物出口を設け、該
スクリユはケーシングの前半都内面に適当な間隙を存し
て沿うほぼテーパ状で後部が開放された中空の本体とそ
の外側において、前端部から後部に向つて形成され、ケ
ーシングの前半内面と本体外面間に溜った固形物をケー
シングの固形物出口に掻出す向きの螺旋状とした複数の
羽根を設け、前記横軸は前端を閉鎖した中空とし、その
後端は回転継手を介して汚水供給管に連通させ、前部に
は前記スクリユーの本体の内側前部に開口する汚水出口
を設けたことを特徴とする遠心脱水機。1. A casing that can be rotated at high speed around a horizontal axis,
It consists of a screw that is concentric with the casing and rotates in the same direction as the casing with a slight speed difference within the casing. The part has a large diameter,
In addition, a desorbed water outlet is provided at the rear end, and a solid matter outlet is provided at the front end, and the screw has an approximately tapered hollow main body with an open rear end that runs along the inner surface of the first half of the casing with an appropriate gap, and a hollow main body with an open rear end. , a plurality of spiral blades are formed from the front end toward the rear and are oriented to scrape out solid matter accumulated between the inner surface of the first half of the casing and the outer surface of the main body to the solid matter outlet of the casing, and the horizontal shaft is located at the front end. A centrifugal dehydrator characterized in that the rear end is closed and hollow, the rear end is connected to a waste water supply pipe via a rotary joint, and the front part is provided with a waste water outlet that opens at the front inside of the main body of the screw.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP101577A JPS6039426B2 (en) | 1977-01-08 | 1977-01-08 | centrifugal dehydrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP101577A JPS6039426B2 (en) | 1977-01-08 | 1977-01-08 | centrifugal dehydrator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5385572A JPS5385572A (en) | 1978-07-28 |
| JPS6039426B2 true JPS6039426B2 (en) | 1985-09-05 |
Family
ID=11489738
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP101577A Expired JPS6039426B2 (en) | 1977-01-08 | 1977-01-08 | centrifugal dehydrator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6039426B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61161156A (en) * | 1985-01-11 | 1986-07-21 | Iseki Kaihatsu Koki:Kk | Centrifugal separator |
| WO2017193267A1 (en) * | 2016-05-09 | 2017-11-16 | 占天义 | Stirring-type grinding separator and grinding device |
-
1977
- 1977-01-08 JP JP101577A patent/JPS6039426B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5385572A (en) | 1978-07-28 |
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