JPS6247586B2 - - Google Patents

Info

Publication number
JPS6247586B2
JPS6247586B2 JP53133553A JP13355378A JPS6247586B2 JP S6247586 B2 JPS6247586 B2 JP S6247586B2 JP 53133553 A JP53133553 A JP 53133553A JP 13355378 A JP13355378 A JP 13355378A JP S6247586 B2 JPS6247586 B2 JP S6247586B2
Authority
JP
Japan
Prior art keywords
discharge
raw water
drum
classifier
opening
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
JP53133553A
Other languages
Japanese (ja)
Other versions
JPS5534188A (en
Inventor
Osami Okada
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.)
Ebara Koki KK
Original Assignee
Ebara Koki KK
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 Ebara Koki KK filed Critical Ebara Koki KK
Priority to JP13355378A priority Critical patent/JPS5534188A/en
Publication of JPS5534188A publication Critical patent/JPS5534188A/en
Publication of JPS6247586B2 publication Critical patent/JPS6247586B2/ja
Granted legal-status Critical Current

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  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Description

【発明の詳細な説明】 本発明は、砂などの固形物を含む濁状、その他
の懸濁液から固形物を連続的に分離するための分
級機、特にドラム式のロータリー分級機に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a classifier for continuously separating solids from turbid or other suspensions containing solids such as sand, particularly a drum-type rotary classifier. be.

一般に、ロータリー分級機においては、砂など
の固形物を含有している濁水中より固形分を分離
する方法として重力による沈降堆積を原理として
おり、原水の流入速度と分級可能な原水濃度との
間には密接な関係があるので、機体構造の自由な
設計を妨げられ高い能率が得られなかつた。
In general, rotary classifiers use sedimentation and sedimentation by gravity as a method of separating solids from turbid water containing solids such as sand, and the difference between the raw water inflow velocity and the raw water concentration that can be classified is Because of the close relationship between the two, it was difficult to freely design the airframe structure, making it impossible to achieve high efficiency.

殊に従来では改良されたロータリー分級機とし
て特開昭49−124671等の一連のものが提案されて
いるが、この従来公知のロータリー分級機の構造
は第1図に示すように内側にラセン状の送り羽根
2を固定した回転ドラム1と、該ドラム1内にド
ラムと同心に支柱31をもつて固設された投入シ
ユート3との二重筒からなり、ドラム後壁4には
円錐状の排出シユート5を備え、この排出シユー
ト5上に放射状に固設された複数個の脱水羽根6
と排出口リング7等を夫々図示の関係位置に固設
し、排出樋11に臨ましめられ、要すれば排出シ
ユート5と投入シユート3との間にバツフルリン
グ8を固設したもので、前記ドラム1のドラム前
壁9は円環状で分級機の汚水の排出口を形成する
と共に、ドラム1内の水位を規定している。そし
て原水流入樋10は円筒となる前記投入シユート
3に開口され原水が投入シユート3を経てから外
筒のドラム1に供給される。
In particular, a series of improved rotary classifiers have been proposed in Japanese Patent Application Laid-Open No. 49-124671, but the structure of this conventionally known rotary classifier has a helical shape on the inside as shown in Figure 1. It consists of a double cylinder consisting of a rotating drum 1 to which a feeding blade 2 is fixed, and a charging chute 3 fixedly installed in the drum 1 with a support 31 concentrically with the drum. A plurality of dewatering blades 6 are provided with a discharge chute 5 and are fixedly arranged radially on the discharge chute 5.
and a discharge port ring 7, etc., are fixedly installed in the relative positions shown in the figure, and are forced to face the discharge gutter 11, and if necessary, a full ring 8 is fixedly installed between the discharge chute 5 and the input chute 3. The drum front wall 9 of the drum 1 is annular and forms an outlet for the waste water of the classifier, and also defines the water level within the drum 1. The raw water inflow gutter 10 is opened to the cylindrical input chute 3, and the raw water is supplied to the outer drum 1 after passing through the input chute 3.

即ち、原水中の固形分はドラム底部にたまつた
水中で次第に沈降し、送り羽根2によつて順次排
出側に送られ、排出端に至つてドラム上方に掻き
上げられ、排出シユート5の上に落下し、更に脱
水羽根6で案内され水分を分離されながら排出シ
ユート5の斜面を滑つて排出口リング7から排出
樋11へ落ちて排出され、一方分級点以下の細粉
を含む汚水はドラム前壁9の開口部より流出され
るものである。
That is, the solid content in the raw water gradually settles in the water that has accumulated at the bottom of the drum, is sent to the discharge side by the feed blade 2, is scraped up to the top of the drum when it reaches the discharge end, and is swept up to the top of the discharge chute 5. The water is further guided by dewatering blades 6 to separate water, slide down the slope of the discharge chute 5, fall from the discharge port ring 7 to the discharge gutter 11, and be discharged. It flows out from the opening in the front wall 9.

従つてこのような分級機の処理操作では内筒と
なる投入シユート3の後端はできるだけ固形物排
出端に近い場所にしなければならず、投入シユー
ト3の全長は長いものになり、実質的に一端から
他端にまで至るばかりか流速をつけるために先太
りのテーパ付円周とするのが普通であるが、機体
全体の大きさに制約されてこのテーパをあまり大
きくすることはできない。その結果、投入シユー
ト内の原水流速は比較的遅いので図示のA部にお
いて望ましくない沈降がはじまる。この部分には
羽根はないから、一旦沈降したものは回転によつ
ても運び去られることはなく、かりにラセン羽根
をつけたとしても底部で移動を繰り返して送出効
果は少ない。一方投入シユート3を離れてドラム
下部の原水溜に落下するとき、はげしく落下する
時は原水溜中に乱流をひきおこし、折角沈降中の
固形分を再び舞い上がらせて分離効率を極めて悪
化させる。
Therefore, in the processing operation of such a classifier, the rear end of the input chute 3, which serves as the inner cylinder, must be placed as close to the solid material discharge end as possible, and the total length of the input chute 3 becomes long, and in practice It is common to have a tapered circumference with a thicker end to increase the flow velocity from one end to the other, but this taper cannot be made too large due to the size of the entire fuselage. As a result, the flow rate of the raw water in the input chute is relatively slow, so that undesirable sedimentation begins in section A shown in the figure. Since there are no blades in this part, once it has settled down, it will not be carried away by rotation, and even if spiral blades were attached to it, it would repeatedly move at the bottom and the sending effect would be low. On the other hand, when it leaves the input chute 3 and falls into the raw water reservoir at the bottom of the drum, when it falls violently, it causes turbulence in the raw water reservoir, and the solids that have been settling are thrown up again, extremely deteriorating the separation efficiency.

従つてこの形式の分級機においては、A部の堆
積を避けるためには投入シユートの流速は早いほ
ど良く落下時の流速は遅いほど良いという二律背
反の設計条件となり、設計は非常に困難である上
にどうしてもA部に望まざる堆積を生じ、止むを
得ず原水の流入量、濃度等にきびしい制限をつけ
て使用するような煩雑な運転管理を強いられる場
合が多かつた。
Therefore, in this type of classifier, in order to avoid the accumulation of part A, the faster the flow rate in the input chute, the better, and the slower the flow rate at the time of falling, the contradictory design conditions are created, which makes the design extremely difficult. Undesirable deposits inevitably occur in the A section, and in many cases, complicated operational management is forced, such as using raw water with strict restrictions on the amount of raw water flowing in, its concentration, etc.

本発明は、これら従来の諸欠点を適確に除去し
ようとするもので新しい構想により従来の分級機
の設計困難であつた点を克服し、設計の自由度を
大巾に大として高能率の分級機を製作簡単で安価
な形態として提供することを目的としたものであ
る。
The present invention aims to accurately eliminate these conventional drawbacks, and uses a new concept to overcome the difficulties in designing conventional classifiers, greatly increasing the degree of freedom in design, and achieving high efficiency. The purpose is to provide a classifier that is easy to manufacture and inexpensive.

また本発明の他の目的は処理液や使用条件に制
約されることが少なく適用範囲を著しく拡大し、
運転管理をも簡易化できるロータリー分級機とす
ることにある。
Another object of the present invention is to significantly expand the scope of application without being restricted by processing solutions or conditions of use.
The objective is to create a rotary classifier that can simplify operation management.

本発明は、分離液流出口と固形物排出口とを両
端に開口したドラムを回転可能に備え、このドラ
ム内面に固形物を排出口へ向つて移送するための
ラセン状送り羽根を持ち、前記排出口部に一端が
開口端となつている中空の固形物排出用錐状部を
固設してなるロータリー分級機において、前記排
出用錐状部を両端が開口端である角錐筒で構成
し、その開口端の一方を原水流入用開口部とな
し、この開口部に臨ましめて角錐筒の内部に衝突
板を設け、さらに前記開口部から流入され前記衝
突板に当つて流入される原水の流水減速部材を設
けると共に前記角錐筒の排出側外周に間隙をあけ
て環状部材を重合配備したことを特徴とするもの
である。
The present invention is provided with a rotatable drum having a separated liquid outlet and a solids discharge port opened at both ends, and a helical sending blade for transferring the solids toward the discharge port on the inner surface of the drum. A rotary classifier comprising a hollow cone-shaped part for discharging solids, which has an open end at one end, is fixed to the discharge port, and the cone-shaped discharge part is constituted by a pyramidal tube having open ends at both ends. , one of the opening ends is used as an opening for inflowing raw water, a collision plate is provided inside the pyramid cylinder facing this opening, and the raw water flowing through the opening hits the collision plate and flows in. The present invention is characterized in that a deceleration member is provided and annular members are arranged overlappingly on the outer periphery of the discharge side of the pyramidal cylinder with a gap therebetween.

本発明を実施例につき第2図乃至第5図を参照
して説明すると、分離液流出口19と固形物排出
口18とを両端に開口したドラム1を回転可能に
備え、この回転するドラム1の内側にラセン状の
送り羽根2を固設し、該ドラム1の一端の前記固
形物排出口18側に多角錐状の排出シユート5が
設けられる。該排出シユート5はその両端部を開
口端とし、フランジ13′を有する投入口筒13
を一方の開口端に形成してドラム1外に導出配備
してある。そしてドラム1内への原水供給のため
原水流入樋10はドラム1の固形物排出側に設置
し、前記投入口筒13内に挿入配備され排出シユ
ート5内に開口臨ませてあり、また投入口筒13
中には原水の排出側への洩れを防ぐ洩れ止壁1
3″が付設されて投入口筒13を閉じ排出シユー
ト5の開口端を閉塞し、且つ原水流入樋10の流
入原水の流入正面に臨ませて衝突板14を排出シ
ユート5内の中央部に固設する。
Embodiments of the present invention will be described with reference to FIGS. 2 to 5. The drum 1 is rotatably equipped with a separated liquid outlet 19 and a solid matter outlet 18 at both ends. A spiral feeding blade 2 is fixedly installed inside the drum 1, and a polygonal pyramid-shaped discharge chute 5 is provided at one end of the drum 1 on the solid material discharge port 18 side. The discharge chute 5 has open ends at both ends thereof, and an input tube 13 having a flange 13'.
is formed at one open end and led out from the drum 1. In order to supply raw water into the drum 1, a raw water inflow gutter 10 is installed on the solid matter discharge side of the drum 1, inserted into the input port cylinder 13, and opened into the discharge chute 5, and has an input port. Cylinder 13
Inside is a leak-stop wall 1 that prevents raw water from leaking to the discharge side.
3'' is attached to close the inlet pipe 13 and close the open end of the discharge chute 5, and to fix the collision plate 14 to the center of the discharge chute 5 so as to face the inflow front of the raw water flowing into the raw water inlet trough 10. Set up

また前記排出シユート5の内周側にリング状の
バツフル板15が水流を妨げる方向に固設されて
いると共に、外周側に放射状に複数の脱水羽根6
を区切部材として必要に応じ設けてある。前記バ
ツフル板15は平板或いは多孔板を用いたり、或
いは棒又は板を規則的、不規則的に並列させたも
のを用いることができるが、いずれにしても水流
を妨害してそのエネルギーを奪い水流をおだやか
にする装置であれば良く、前記衝突板14に組合
せて設けられる。必要あれば排出シユート5の斜
面内側に沿い複数段に設け、或いは複数種類の部
材を混用設置しても良い。また衝突板14として
も凹凸板、多孔板や分配板などが選んで用いられ
る。
Further, a ring-shaped baffle plate 15 is fixedly installed on the inner circumferential side of the discharge chute 5 in a direction to obstruct the water flow, and a plurality of dewatering blades 6 are radially arranged on the outer circumferential side.
are provided as partition members as necessary. The baffle plate 15 can be a flat plate or a perforated plate, or can be made by regularly or irregularly arranging rods or plates, but in any case, it obstructs the water flow and takes away its energy. Any device may be used as long as it calms the impact, and it is provided in combination with the collision plate 14. If necessary, they may be provided in multiple stages along the inside of the slope of the discharge chute 5, or a plurality of types of members may be installed in a mixed manner. Further, as the collision plate 14, a concavo-convex plate, a perforated plate, a distribution plate, etc. can be selected and used.

なお前記バツフル板15とは別のバツフル板1
6を単数又は複数、バツフル板15より汚水排出
側に適宜の間隔をおいた場所に設置し、ドラム1
内に貯留される原水の水面17はこのバツフル板
16の面内にもあるようにするのも効果的であ
る。これは原水流路の際に水面に若干の波立ちを
与えることも考えられるので、別のバツフル板1
6を設けて波立ちの多い水面をバツフル板15,
16の間に閉じこめるようにすることで合理的な
配置構成となる。
Note that there is a separate board 1 other than the board 15.
Drum 1 or drums 6 are installed at appropriate intervals on the sewage discharge side from the full plate 15.
It is also effective to arrange that the water surface 17 of the raw water stored inside is also within the plane of this baffle plate 16. This may cause some ripples on the water surface during the raw water flow path, so another Batsuful board 1
6 is installed to cover the rippled water surface with a full board 15,
By confining it between 16 and 16, a rational arrangement can be achieved.

また角錐筒からなる排出シユート5は、その反
対方向に傾斜する環状部材の排出口リング7を間
隙をあけて相対して二重筒となるように設けてあ
りこの環状部材である排出口リング7の錐状部の
排出シユート5から落下してくる固形物をドラム
回転によつても四方に飛散させないで所定の排出
樋11に誘導落下させるために必要なもので、錐
状部に脱水羽根がなくても有効に用いられ固形物
排出口18で排出樋11に開口された状態にドラ
ム5に配備されている。
Further, the discharge chute 5 made of a pyramidal cylinder has a discharge port ring 7 which is an annular member inclined in the opposite direction and is provided so as to face each other with a gap to form a double cylinder. This is necessary in order to guide the solids falling from the discharge chute 5 of the cone-shaped part into a predetermined discharge gutter 11 without scattering them in all directions even when the drum rotates. Even if there is no solid material discharge port 18, it can be effectively used and is provided in the drum 5 with the solid matter discharge port 18 opening into the discharge gutter 11.

図中14′,15′,16′は前記衝突板14、
バツフル板15、バツフル板16に対するそれぞ
れの支脚、20はドラム回転用の駆動装置、21
はチエン、22はタイヤ、23は支持ローラ、2
4は軸受、25は排水樋、26は原水受槽であ
る。
In the figure, 14', 15', 16' are the collision plates 14,
Respective support legs for the buttful plate 15 and the buttful plate 16; 20 is a drive device for rotating the drum; 21
is a chain, 22 is a tire, 23 is a support roller, 2
4 is a bearing, 25 is a drainage gutter, and 26 is a raw water receiving tank.

なお前記原水流入樋10からの原水を受ける排
出シユート5の内部は原水の投入シユートも兼ね
ていて、その底面の角度が堆積物を自動的に落下
せしめ得るような急傾斜となつていて、投入シユ
ートを離れる時の水流がドラム下部の原水溜に与
える撹乱の影響ができるだけ少なくなつているの
で設計の自由度を得ると共に機械全体の効率を向
上させることが容易に可能となつている。
The interior of the discharge chute 5 that receives the raw water from the raw water inflow gutter 10 also serves as a raw water input chute, and its bottom surface is steeply sloped to allow sediment to fall automatically. Since the influence of disturbance caused by the water flow leaving the chute on the raw water reservoir at the bottom of the drum is minimized, it is easily possible to obtain design freedom and improve the efficiency of the entire machine.

また前記排出シユート5は、もし流下速度等の
関係、或いは摩耗等の関係で一体が望ましくない
場合にはシユート両斜面を用いるのに代えて外側
面と内側面の表裏を夫々別体とし、夫々に最適の
傾斜角を与えるように、二重構造に製作すること
も可能である。
In addition, if the discharge chute 5 is undesirable due to flow rate, wear, etc., instead of using both slopes of the chute, the front and back surfaces of the outer and inner surfaces may be made separate, respectively. It is also possible to fabricate a double structure to provide the optimum angle of inclination.

しかして原水を原水流入樋10より供給すれ
ば、流入速度が小さい場合はそのまま角錐筒の排
出シユート5の内側を流れ、もし流入速度が大き
い場合は一旦衝突板14及びバツフル板15に衝
突し、速度エネルギーの大部分を失つて排出シユ
ート5の内側に流下する。この排出シユート5の
内側傾斜は大きいから流下速度は増加して投入
時、原水中の固形分の沈降が起りにくい。
If raw water is supplied from the raw water inflow gutter 10, if the inflow velocity is low, it will flow directly inside the pyramidal cylinder discharge chute 5, and if the inflow velocity is high, it will collide once with the collision plate 14 and the buttful plate 15. It flows down inside the discharge chute 5, losing most of its velocity energy. Since the inner slope of this discharge chute 5 is large, the flow rate is increased, and solid content in the raw water is less likely to settle during charging.

即ち排出シユート5を流下する原水は衝突板1
4によつて多分に乱流状態であるので沈降は起り
にくく、かりに起つても排出シユート5における
斜面の傾斜角は沈降物の堆積、滞溜を許さないか
ら沈降物は直ちにバツフル板15を通過して本来
の堆積場所であるドラム1内の送り羽根2,2の
間に落ちつくこととなつて、固形物排出口18側
へ移送される。
That is, the raw water flowing down the discharge chute 5 passes through the collision plate 1
4, the flow is highly turbulent, so sedimentation is difficult to occur, and even if it occurs, the slope angle of the discharge chute 5 does not allow sediment to accumulate or accumulate, so the sediment immediately passes through the baffle plate 15. Then, the solids settle between the feeding blades 2, 2 in the drum 1, which is the original deposition place, and are transferred to the solids discharge port 18 side.

また前記排出シユート5を流下した乱流の原水
は、バツフル板15,16等の原水流入減速部材
により、一層細かな乱流となつて原水溜の中に流
入するので沈降作用を行なつている原水を掻きま
わす影響は最小限に止まる。かくしてドラム1の
固形物排出側において、上方に運び上げられた固
形物は直接排出シユート5の表面上を転落し、排
出口リング7及び排出樋11から導出される。即
ち、排出口リング7は排出シユート5から落下し
てくる固形物をドラム回転によつても四方に飛散
させないで所定の排出樋11に誘導落下させる。
一方固形物を沈降分離した分離液はドラム1の一
端の分離液流出口19から導出され、排出樋25
を経て処分させる。
Further, the turbulent raw water flowing down the discharge chute 5 becomes a finer turbulent flow by the raw water inflow slowing members such as the baffle plates 15 and 16 and flows into the raw water reservoir, thereby performing a settling action. The impact of stirring up raw water is kept to a minimum. On the solids discharge side of the drum 1, the solids thus carried upwards fall directly onto the surface of the discharge chute 5 and are led out of the discharge ring 7 and the discharge trough 11. That is, the discharge port ring 7 guides the solid matter falling from the discharge chute 5 into a predetermined discharge gutter 11 without scattering it in all directions even when the drum rotates.
On the other hand, the separated liquid obtained by sedimentation and separation of the solid matter is led out from the separated liquid outlet 19 at one end of the drum 1, and is discharged from the discharge gutter 25.
be disposed of after

本発明により、従来では投入シユート上の原水
の流入速度と排出速度は不可分の関係にあつた
が、両者を全く無関係に自由に設計できるために
使用条件の範囲が大巾に広がり機械の適用範囲を
著しく広げ得ると共に、使用原水に最適な機械が
容易に設計できるので、機械の効率が大巾に高め
られ、能率的な分級作業が可能となり、しかもそ
の構造は極めて簡単で製作、保守保安が著しく容
易となり、使用材料は従来型に比し節減し、軽量
化がはかられ運転動力も軽減できて省エネルギー
並びに省資源にも貢献するほか、排出シユートか
ら落下してくる固形物を環状部材で受けてドラム
回転によつても四方に飛散させないで排出樋に誘
導し固形物のドラム外への導出が適確でドラム内
への脱落混入がなく且つ排出シユートの内外両面
を原水流入と固形物排出とに無駄なく活用して固
形物排出と原水流入とを区分けして集中して適確
に行ないうるし排出シユートも分割配備できるの
で構成がコンパクトで簡単であり製作に便利で、
運転にきびしい制約を受けることなく運転、管理
も容易化できる利益がある。
With the present invention, the inflow speed of raw water on the input chute and the discharge speed were inseparable from each other in the past, but since the two can be designed freely and completely unrelated, the range of usage conditions has been widened and the scope of application of the machine has been expanded. Not only can it be expanded significantly, it is also easy to design a machine that is optimal for the raw water used, so the efficiency of the machine is greatly increased and efficient classification work is possible.Moreover, its structure is extremely simple, making manufacturing, maintenance, and safety extremely easy. It is easier to use, uses less material than the conventional type, is lighter, reduces operating power, and contributes to energy and resource conservation. Even when the drum rotates, the solids are guided to the discharge gutter without being scattered in all directions, and the solids are properly guided out of the drum, preventing them from falling into the drum. The solid material discharge and raw water inflow can be separated, concentrated, and carried out accurately without any waste, and the lacquer discharge chute can also be deployed separately, making the configuration compact and simple, and convenient for manufacturing.
There is an advantage that operation and management can be facilitated without severe restrictions on operation.

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

第1図は従来例のロータリー分級機の縦断面
図、第2図は本発明の実施例の縦断面図、第3図
は使用状態を示す正面図、第4図はその背面図、
第5図はその側面図である。 1……ドラム、2……送り羽根、3……投入シ
ユート、4……ドラム後壁、5……排出シユー
ト、6……脱水羽根、7……排出口リング、8…
…バツフルリング、9……ドラム前壁、10……
原水流入樋、11……排出樋、13……投入口
筒、13′……フランジ、13″……洩れ止壁、1
4……衝突板、14′,15′,16′……支脚、
15,16……バツフル板、17……原水面、1
8……固形物排出口、19……分離液流出口、2
0……駆動装置、21……チエン、22……タイ
ヤ、23……支持ローラ、24……軸受、25…
…排水樋、26……原水受槽、31……支柱。
Fig. 1 is a vertical cross-sectional view of a conventional rotary classifier, Fig. 2 is a longitudinal cross-sectional view of an embodiment of the present invention, Fig. 3 is a front view showing the state of use, and Fig. 4 is a rear view thereof.
FIG. 5 is a side view thereof. DESCRIPTION OF SYMBOLS 1...Drum, 2...Feeding blade, 3...Input chute, 4...Drum rear wall, 5...Discharge chute, 6...Dewatering blade, 7...Discharge port ring, 8...
...Batsuful ring, 9...Drum front wall, 10...
Raw water inflow gutter, 11...Discharge gutter, 13...Inlet tube, 13'...Flange, 13''...Leak stop wall, 1
4... Collision plate, 14', 15', 16'... Support leg,
15, 16... Batsuful board, 17... Raw water surface, 1
8... Solid matter outlet, 19... Separated liquid outlet, 2
0... Drive device, 21... Chain, 22... Tire, 23... Support roller, 24... Bearing, 25...
...Drainage gutter, 26...Raw water receiving tank, 31...Strut.

Claims (1)

【特許請求の範囲】 1 分離液流出口と固形物排出口とを両端に開口
したドラムを回転可能に備え、このドラム内面に
固形物を排出口へ向つて移送するためのラセン状
送り羽根を持ち、前記排出口部に中空で一端が開
口端である固形物排出用錐状部を固設してなるロ
ータリー分級機において、前記排出用錐状部を両
端が開口端である角錐筒で構成し、その開口端の
一方を原水流入用開口部となし、この開口部に臨
ましめて角錐筒の内部に衝突板を設け、さらに前
記開口部から流入され前記衝突板に当つて流入さ
れる原水の流水減速部材を設けると共に前記角錐
筒の排出側外周に間隙をあけて環状部材を重合配
備したことを特徴とするロータリー分級機。 2 前記角錐筒が、洩れ止壁を有する投入口筒を
備えたものである特許請求の範囲第1項記載の分
級機。 3 前記流水減速部材が、多孔板である特許請求
の範囲第1項又は第2項記載の分級機。 4 前記流水減速部材が、錐状部内壁で分離液排
出側に適宜間隔をおいて複数設けられるものであ
つて、その少なくとも一つがドラム内に貯留され
る原水面下に下端が位置して配備されるものであ
る特許請求の範囲第1〜3項のいずれか一つの項
記載の分級機。
[Scope of Claims] 1. A rotatable drum having a separated liquid outlet and a solids discharge port opened at both ends, and a helical feed blade for transferring the solids toward the discharge port on the inner surface of the drum. In a rotary classifier, the solid material discharge cone-shaped part is hollow and has an open end at one end and is fixed to the discharge port, and the discharge cone-shaped part is composed of a pyramidal tube having open ends at both ends. One of the opening ends is used as an opening for inflowing raw water, and a collision plate is provided inside the pyramidal cylinder facing this opening, and further the raw water flows through the opening and hits the collision plate. A rotary classifier characterized in that a flowing water deceleration member is provided and annular members are arranged overlappingly on the outer periphery of the discharge side of the pyramidal cylinder with a gap therebetween. 2. The classifier according to claim 1, wherein the pyramidal cylinder is provided with an inlet cylinder having a leak-stopping wall. 3. The classifier according to claim 1 or 2, wherein the flowing water reducing member is a perforated plate. 4. A plurality of the flowing water reducing members are provided at appropriate intervals on the inner wall of the conical part on the separated liquid discharge side, and at least one of them is arranged with its lower end located below the surface of the raw water stored in the drum. A classifier according to any one of claims 1 to 3, wherein the classifier is a classifier according to any one of claims 1-3.
JP13355378A 1978-10-30 1978-10-30 Rotary classifier Granted JPS5534188A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13355378A JPS5534188A (en) 1978-10-30 1978-10-30 Rotary classifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13355378A JPS5534188A (en) 1978-10-30 1978-10-30 Rotary classifier

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP10783678A Division JPS5534180A (en) 1978-09-02 1978-09-02 Rotary classifier

Publications (2)

Publication Number Publication Date
JPS5534188A JPS5534188A (en) 1980-03-10
JPS6247586B2 true JPS6247586B2 (en) 1987-10-08

Family

ID=15107496

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13355378A Granted JPS5534188A (en) 1978-10-30 1978-10-30 Rotary classifier

Country Status (1)

Country Link
JP (1) JPS5534188A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5910850U (en) * 1982-07-12 1984-01-23 株式会社気工社 Conical chute of classifier

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5534180A (en) * 1978-09-02 1980-03-10 Ebara Koki Kk Rotary classifier

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5534180A (en) * 1978-09-02 1980-03-10 Ebara Koki Kk Rotary classifier

Also Published As

Publication number Publication date
JPS5534188A (en) 1980-03-10

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