JPS5969113A - Thickener - Google Patents

Thickener

Info

Publication number
JPS5969113A
JPS5969113A JP17828582A JP17828582A JPS5969113A JP S5969113 A JPS5969113 A JP S5969113A JP 17828582 A JP17828582 A JP 17828582A JP 17828582 A JP17828582 A JP 17828582A JP S5969113 A JPS5969113 A JP S5969113A
Authority
JP
Japan
Prior art keywords
tank
rakes
center
thickener
rake
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
Application number
JP17828582A
Other languages
Japanese (ja)
Inventor
Takeshi Onodera
健 小野寺
Akizou Nagasashi
永指 彰三
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP17828582A priority Critical patent/JPS5969113A/en
Publication of JPS5969113A publication Critical patent/JPS5969113A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a thickener having improved functions for scraping and transferring deposits and thickening the same in a scraper which transfers the deposits by means of rotary rakes to the discharging port side at the thickener center by the constitution wherein the width of the rotary rake is calculated by the specific equation. CONSTITUTION:This thickener 10 is provided with a scraper which transfers deposits to the discharging port 11 side at the thickener center by means of plural rotary rakes 30 consisting of plural blades 3A disposed at an equal pitch P and a specified scraping angle (r) and disposed radially from the center of the thickener 10. The rakes 30 are constituted at the width of the rakes 30 by the approximate value calculated from the equation where the inside diameter of the thickener 10 is designated as D, the outside diameter of the port 11 as Du, the number of the rakes 30 as (n), the coefft. of allowance as (epsilon), the ratio between the inter-blade distance (d) of the object disposition with respect to the center of the thickener and the above-described D as (x), and the width of the rakes 30 as A. Then the scraping power is maximized by each blade 3A and the driving power required for turning the rake 30 is minimized.

Description

【発明の詳細な説明】 本発明は、槽底に沈降する沈積物を槽中心の排出ポート
側に掻取って移行させ4る掻寄機を備えた汚泥濃縮用等
の濃縮槽に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a thickening tank for sludge thickening, etc., which is equipped with a scraper that scrapes and transfers sediments settling at the bottom of the tank to the discharge port side in the center of the tank. .

汚泥濃縮槽について従来例を説明すると、第1図、第2
図に示すように、傾斜した槽底(10a) 。
Conventional examples of sludge thickening tanks are explained in Figures 1 and 2.
As shown in the figure, a sloped tank bottom (10a).

槽中心の排出z−ト(111,センターポストC121
,および周! (IOh)上部に設けた排水溝側等を有
する汚泥濃縮槽(101内に、センターポストにベアリ
ング(1α)を介し回転自在に装架されたセンタートラ
ス(11と、センタートラスから放射状に突設された複
数のレーキトラス(21と1等ピッチかつ定掻寄角に配
置された複数のブレード(3α)よりなり前記レーキト
ラス(21の下側に配設された複数(2〜4本)の回転
レーキ(31と、減速機付の駆動電動機(4)等よりな
る汚泥掻寄機が配設され、駆動電動機(4)によりセン
タートラス(1)、レーキトラス(2)を介して各回転
レーキ(3)が槽中心を回転中心にして槽底(IOIZ
)上に沿って矢示のように旋回され、回転レーキ(3)
を構成する各ブレード(3a、)が槽底(10(Z)上
の沈積物を掻取り排出ポー)(ill側に向って移行さ
せ、排出ポート旧)内に移行された沈積物は図示省略し
たスクリューコンベヤー等によって槽外に取出されると
ともに、汚泥分離後の水は排水溝(13)内にオーバー
フローさせて排出するようになっている。
Discharge z-tot in the center of the tank (111, center post C121
, and Zhou! (IOh) Inside the sludge thickening tank (101), which has a drainage ditch installed at the top, there is a center truss (11) rotatably mounted on the center post via a bearing (1α), and a center truss (11) that protrudes radially from the center truss. A plurality of rotary rakes (2 to 4) arranged under the rake truss (21) and a plurality of blades (3α) arranged at equal pitch and at a constant raking angle. (31), a sludge scraper consisting of a drive motor (4) with a speed reducer, etc. The bottom of the tank (IOIZ) is rotated around the center of the tank.
) is rotated along the top as shown by the arrow, and the rotating rake (3)
The blades (3a,) forming the tank scrape off the sediment on the tank bottom (10 (Z) and move it toward the ill side, and the sediment transferred into the discharge port (old) is not shown). The sludge is taken out of the tank by a screw conveyor or the like, and the water after the sludge separation is discharged by overflowing into a drainage ditch (13).

また、汚泥掻寄機における前記の回転レーキ(3)は、
第2図に示すように汚泥濃縮槽αQの周壁(1oh)近
傍の点P と排出ポート(illの外周に接する点P、
Pとを結ぶ2本の直線11.lによって設定された回転
レーキ幅αに形成され1回転レーキ(31を構成する各
ブレード(3α)は前記直線l、l内において等ピッチ
Pにかつ定掻寄角γによって配設されているとともに、
第1図に示すように槽底(10a)に対して一定のブレ
ード高さBに構成された構造よりなっている。
Furthermore, the rotary rake (3) in the sludge scraper is
As shown in Fig. 2, a point P near the peripheral wall (1oh) of the sludge thickening tank αQ, a point P touching the outer circumference of the discharge port
Two straight lines connecting P11. The blades (3α) constituting the one-rotation rake (31) are formed to have a rotational rake width α set by l, and are arranged at equal pitches P and at a constant rake angle γ within the straight lines l and l. ,
As shown in FIG. 1, the structure is such that the blade height B is constant with respect to the tank bottom (10a).

しかし、従来の前記掻取機を備えた濃縮槽においては、
前記回転レーキ(3)の各ブレード(3α)における沈
積物の掻取りおよび移行能力が槽底(Noα)各部にお
ける沈積物の状態に十分に対応されたものとは言えず、
特に第1図に示すように排出ポート0Il側付近のブレ
ード(3α)による沈積物の掻取および移行能力に不足
を生じて、槽中心側に図示のような沈積物の盛上りを生
じ、沈積物の排出機能および母線機能が著しく低減され
る難点がある・本発明は、従来の掻寄機を備えた濃縮槽
におけ゛る前記したような難点を解消するために開発さ
れたものであって1等ピッチかっ定掻寄角にて配置され
た複数のブレードよりなり槽中心から放射状に配置され
た複数の回転レーキな有し、該回転レーキによって沈積
物を槽中心の排出ポート側に移行させる掻寄機において
、濃縮槽内径?:D、排出ホード外径をDW、  回転
レーキ数をル、アロアンス係数をε、槽中心に対し対象
配置のプレート間距離dと前記りとの比をX、回転レー
キ幅をAとするとき。
However, in the conventional concentration tank equipped with the scraper,
It cannot be said that the ability of each blade (3α) of the rotary rake (3) to scrape and transfer the sediment sufficiently corresponds to the state of the sediment in each part of the tank bottom (Noα).
In particular, as shown in Figure 1, the ability of the blade (3α) near the discharge port 0Il side to scrape and transfer sediment is insufficient, causing a bulge of sediment as shown in the figure on the center side of the tank, causing sedimentation. There is a drawback that the material discharge function and the busbar function are significantly reduced.The present invention was developed to solve the above-mentioned drawbacks of the conventional concentration tank equipped with a scraper. It has a plurality of rotating rakes arranged radially from the center of the tank, which are composed of a plurality of blades arranged at a constant pitch and a constant scraping angle, and the rotating rakes move the sediment to the discharge port side of the center of the tank. What is the inner diameter of the thickening tank in the scraping machine? :D, the outer diameter of the discharge hoard is DW, the number of rotating rake is L, the allowance coefficient is ε, the ratio of the distance d between the plates of the target arrangement to the center of the tank and the above is X, and the width of the rotating rake is A.

の上記式により算出された近似値による回転レーキ幅に
て構成された回転レーキな具備した掻寄機を備えた点に
特徴を有し、その目的とする処は。
The present invention is characterized in that it is equipped with a raking machine equipped with a rotary rake whose width is an approximate value calculated by the above formula.

回転レーキな構成する各ブレードの掻取りおよび移行能
力を槽底各部における沈積物の実態に対応した構成にす
ることにより、沈積物の掻取り移行排出ならびに濃縮機
能を高めた濃縮槽を供する点にある。
By configuring the scraping and transfer capabilities of each blade of the rotating rake to correspond to the actual condition of sediment at each part of the tank bottom, we provide a thickening tank with enhanced functions of scraping, transferring, discharging, and concentrating sediment. be.

本発明は、前記の構成になっており、濃縮槽内に装備さ
れた掻寄機における各回転レーキ幅を前記構成にするこ
とにより、同回転レーキを構成している各ブレードのそ
れぞれが、槽底各部における沈積物の実態に対応した最
適な沈積物の掻取りならびに移行能力を有するものとな
るので、濃縮槽内全域において前記回転レーキによる沈
積物の掻取りならびに移行機能が極めて効果的に発揮さ
れ、濃縮槽における沈積物の排出および濃縮機能が著し
く向上されるとともに、消費動力乞大幅に節減できる。
The present invention has the above-described configuration, and by setting the width of each rotating rake in the scraper installed in the thickening tank to the above-described configuration, each of the blades constituting the same rotating rake can Since it has the optimum sediment scraping and transfer ability corresponding to the actual condition of sediment in each part of the bottom, the sediment scraping and transfer function by the rotary rake is extremely effective throughout the entire area inside the thickening tank. As a result, the function of discharging and concentrating sediment in the concentration tank is significantly improved, and power consumption can be reduced significantly.

以下5本発明の実施例を図示について説明する◎汚泥濃
縮槽について本発明の一実施例を説明すると、本実施例
は、第1図に示したセンタートラス(1)、複数のレー
キトラス(2)、同レーキトラス(2)の下側に配設さ
れ複数個のブレード(3α)より構成された放射方向の
複数の回転レーキ(31、および駆動電動機(4)等よ
りなる濃縮槽(10)内の汚泥掻寄機において、前記回
転レーキ(3)ヲ後記のように構成することによって、
その回転レーキの構成要件となる各ブレードが、槽底各
部における沈積物即ち沈積汚泥の実態に対応した最適な
沈積物の掻取りおよび移行能力を有するものにした構成
に特徴を有するものであって、本実施例の回転レーキは
次のように構成される。
Below, five embodiments of the present invention will be explained with reference to illustrations.◎An embodiment of the present invention regarding a sludge thickening tank will be explained.This embodiment is based on a center truss (1) and a plurality of rake trusses (2) shown in Fig. 1. , a plurality of radially rotating rakes (31) disposed below the rake truss (2) and composed of a plurality of blades (3α), and a drive motor (4), etc. in the thickening tank (10). In the sludge scraper, by configuring the rotary rake (3) as described below,
The rotating rake is characterized by a configuration in which each blade, which is a component of the rotating rake, has an optimal ability to scrape and transfer sediment in response to the actual state of sediment, that is, sedimented sludge, in each part of the tank bottom. The rotary rake of this embodiment is constructed as follows.

即ち、第6.4図に示す本実施例においては、第6図に
示すよ5に、回転レーキ00)の主体となる各ブレード
(3A)が1等ピッチPにより複数(図示例では7個)
配置されるとともに、各ブレード(3A)の掻寄角γは
、槽底(10α)上の沈積物即ち沈積汚泥における摩擦
係数fとの関連において。
That is, in the present embodiment shown in Fig. 6.4, each blade (3A) which is the main body of the rotary rake 00 is arranged at a plurality of blades (7 in the illustrated example) at a constant pitch P, as shown in Fig. 6. )
and the scraping angle γ of each blade (3A) in relation to the coefficient of friction f in the sludge on the tank bottom (10α).

taイ覗可しf   −−−fi+ の関係を有し、上記(1)式によって算出された掻寄角
γに設定することにより、各ブレード(3A)における
掻取り能力が最大限に発揮されるようになり1回転レー
キ(7)の旋回に要する動力′!11′最小にすること
ができ、前記摩擦係数fつまり濃縮対象の汚泥に基づき
各ブレード(3A)の掻寄角を同じγに設定する。
By setting the scraping angle γ calculated by the above formula (1), the scraping ability of each blade (3A) can be maximized. The power required to turn the rake (7) once! 11' can be minimized, and the scraping angle of each blade (3A) is set to the same γ based on the friction coefficient f, that is, the sludge to be concentrated.

また、槽底(10α)上に立設状態に配置されている各
ブレード(3A)の高さB(第1図参照)については。
Also, regarding the height B (see Fig. 1) of each blade (3A) placed upright on the tank bottom (10α).

W:固定物負荷に9/m2h(濃縮槽設定のベースとな
る)N:回転レーキの回転数γ、p、h(通常、先端側
の外周速度18077L/h以内) γ5:濃縮対象の汚泥比重lay / m 3Sf:汚
泥排出濃度、kg/ゆ ε:アロワンス係数(通常1.2〜1,3)D二演縮槽
内径m DllL:排出ポート外径m n、二回伝レーキ数 とすると。
W: Fixed material load 9/m2h (base of concentration tank settings) N: Rotating rake rotation speed γ, p, h (usually within 18077 L/h of peripheral speed on the tip side) γ5: Specific gravity of sludge to be concentrated lay/m 3Sf: sludge discharge concentration, kg/yu ε: allowance coefficient (usually 1.2 to 1.3) D2 compression tank inner diameter m DllL: discharge port outer diameter m n, 2 transfer rake number.

にて表わすことができ、上記(21式によってブレード
高さくBlを適切値に設定できるとともに、上記+21
式から明らかなようにブレード高さBは、濃縮槽および
掻寄機の基本的な設計邦項と濃縮対象の汚泥に基づいて
容易に設定できる。
The above formula (21) allows the blade height Bl to be set to an appropriate value, and the above +21
As is clear from the equation, the blade height B can be easily set based on the basic design specifications of the thickening tank and scraper and the sludge to be concentrated.

しかし”乙前記のように構成された汚泥掻畜機の回転レ
ーキにおいて、槽底(10α)上の各部における沈積汚
泥を掻取って郡行するために最も影響し重要0項となる
各ブレード(3A)の長さは、第6図に示すように回転
レーキの幅Aによって表わすことができ5本実施例にお
ける前記回転レーキ幅Aは、さらに、槽中心に対し対象
配置になっているプレード間距離d(第3図参照)とし
、同dと前記りとの比をXとすると。
However, in the rotary rake of the sludge scraper configured as described above, each blade ( 3A) can be expressed by the width A of the rotating rake as shown in FIG. Let the distance be d (see Figure 3), and the ratio of the distance d to the above distance be X.

にて表わすことができ、上記(3)式により算出して求
められた曲線71+71 によって第4図に示すように
回転レーキ幅を設定し、第6図に示すように等ピッチP
および定掻寄角γにて配置されている各ブレード(3A
)を前記曲線11.1!□ に達する長さにすると、該
各ブレード(3A)は、槽底(10a、 )上の各部に
おける沈積汚泥の実態て対応しまた最適な掻取り能力1
よらびに移行能力を有する理想的な構成にすることがで
きる。
The rotating rake width is set as shown in Fig. 4 using the curve 71+71 calculated using the above equation (3), and the equal pitch P is set as shown in Fig. 6.
and each blade (3A
) to the curve 11.1! When the length reaches □, each blade (3A) corresponds to the actual condition of the sedimented sludge at each part on the tank bottom (10a, ) and has an optimum scraping capacity 1.
This makes it possible to create an ideal configuration that has the ability to read and migrate.

しかし、実際には、上記(3)式で算出された回転レー
キ幅は1図示のように複雑な曲線となり実用的でないた
め、第4図に示すように点P0と22間を結ぶ直線12
と平行な直線13が上記(31式にて得られた曲、%>
 711 と交わる点Y P3とし、前記点P□と23
間を直線lηLで結びかつ点P3 とP2 間を直線e
nで結び、前記直線1mと13r、、にて回転レーキ幅
Aを画定すると、該回転レーキ幅は、上記(3)式てよ
って算出されたものに極(近似したものとなり、その近
似値による回転レーキ幅Aにすることによって、その回
転レーキの各ブレード6Aを前記のような理想的なもの
にほぼ同様に設定することができる。なお、前記の点P
3(最尤点)は、第5図に示す各DtL/D曲線におい
て。
However, in reality, the rotating rake width calculated using the above formula (3) becomes a complicated curve as shown in Figure 1, which is not practical.
The straight line 13 parallel to the above (song obtained by formula 31, %>
Let the point Y P3 intersect with 711, and the points P□ and 23
A straight line lηL connects the two points, and a straight line e connects the points P3 and P2.
n, and define the rotating rake width A by the straight lines 1m and 13r, . . By setting the rotating rake width to A, each blade 6A of the rotating rake can be set almost in the same ideal manner as described above.
3 (maximum likelihood point) in each DtL/D curve shown in FIG.

のように定めることができる。It can be defined as follows.

図示した実施例は、前記したような構成よりなっている
ので、特に前記(31式によって算出された回転レーキ
幅の前記近似値により、同回転レーキ幅を定め、それを
構成する各ブレードが槽底各部における沈積汚泥の実態
に対応した最適なその掻取りならびに移行能力を有する
構成にすることができ、濃縮槽内全域において前記回転
レーキによる沈積物の掻取りおよび移行機能が極めて効
果的に発揮され、従来のような槽中心側に生ずる沈積物
の盛上りがな(なり、濃縮槽における沈積物の排出なら
びに濃縮機能が著しく向上される。よって、掻寄機の用
型動力も著しく節減することができろ。
Since the illustrated embodiment has the above-mentioned configuration, the width of the rotating rake is determined by the approximate value of the rotating rake width calculated by the formula (31), and each blade constituting it is The structure can be configured to have the optimum scraping and transfer ability corresponding to the actual condition of the sedimented sludge in each part of the bottom, and the function of scraping and transferring the sediment by the rotary rake is extremely effective throughout the entire area inside the thickening tank. This eliminates the build-up of sediment that occurs at the center of the tank as in the past, and the function of draining and concentrating sediment in the thickening tank is significantly improved.Therefore, the power required for the scraping machine is also significantly reduced. Be able to do that.

なお、前記実施例では汚泥濃縮槽について説明したが、
本発明は各種プラントの濃縮槽に適用可能である。
In addition, although the sludge thickening tank was explained in the above example,
The present invention is applicable to concentration tanks of various plants.

以上本発明を実施例について説明したが、勿論本発明は
このような実施例にだけ局限されるものではなく5本発
明の精神を逸脱しない範囲内で種々の設計の改変を施し
うるものである。
Although the present invention has been described above with reference to embodiments, it goes without saying that the present invention is not limited to these embodiments, and that various design modifications can be made without departing from the spirit of the present invention. .

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

第1図は従来の掻寄機を備えた濃縮槽を示す縦断面図、
第2図は第1図における掻寄機の回転レーキ部分の構造
を示す平面図、第6図は本発明の一実施例を示す回転レ
ーキ部分の\\平面図、第4図は第6図に示す回転レー
キの構成説明図、第5図は回転レーキ幅の近似値設定の
ための特性曲線図である。 1:センタートラス 2ニレ−キトラス 6Aニブレー
ド 4:駆動電動機 10:濃縮槽10α:槽底 11
:排出ポート 12:センターポスト 13:排水溝 
30=回転レーキ A:回転レーキ幅 P:ピッチ γ
:掻寄角復代理人 升埋士岡本重文 外2名 第2(2) 築3図 搗4目 第5図 φ品 yガ y述 、 イ糸( イ七シ方イa     cl ニーに≧91’f)−D
α
Figure 1 is a vertical cross-sectional view showing a concentration tank equipped with a conventional scraper;
Fig. 2 is a plan view showing the structure of the rotary rake portion of the scraper in Fig. 1, Fig. 6 is a plan view of the rotary rake portion showing an embodiment of the present invention, and Fig. 4 is Fig. 6 FIG. 5 is a characteristic curve diagram for setting an approximate value of the rotating rake width. 1: Center truss 2 Elm-kit truss 6A Niblade 4: Drive motor 10: Concentrator tank 10α: Tank bottom 11
: Discharge port 12: Center post 13: Drain groove
30 = Rotating rake A: Rotating rake width P: Pitch γ
:Kakiyori-kaku sub-agent, Masu burying person, Okamoto important cultural heritage, 2 people, 2nd (2), 3rd figure, 4th figure, 5th figure 'f)-D
α

Claims (1)

【特許請求の範囲】 等ピッチかつ定掻寄角にて配置された複数のブレードよ
りなり槽中心から放射状に配置された複数の回転レーキ
を有し、該回転レーキによって沈積物を槽中心の排出ポ
ート側に移行させる掻寄機において、濃縮槽内径をり、
排出ポート外径をDμ。 回転レーキ数を几、アロアンス係数乞ε、槽中心に対し
対象配置のプレート間距離dと前記りとの比をx1回転
レーキ幅YAとするとき。 の上記式により算出された近似値による回転レーキ幅に
て構成された回転レーキを具備した掻寄機に特徴を有す
る濃縮槽。
[Claims] It has a plurality of rotating rakes arranged radially from the center of the tank, which are made up of a plurality of blades arranged at equal pitches and at a constant raking angle, and the rotating rakes discharge sediment from the center of the tank. In the scraping machine that moves to the port side, the inner diameter of the concentration tank is
The outer diameter of the discharge port is Dμ. When the number of rotating rakes is 几, the allowance coefficient is ε, and the ratio of the distance d between the plates of the target arrangement with respect to the tank center is x1 and the rotating rake width YA. A concentration tank characterized by a scraper equipped with a rotating rake having a rotating rake width determined by an approximate value calculated by the above formula.
JP17828582A 1982-10-13 1982-10-13 Thickener Pending JPS5969113A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17828582A JPS5969113A (en) 1982-10-13 1982-10-13 Thickener

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17828582A JPS5969113A (en) 1982-10-13 1982-10-13 Thickener

Publications (1)

Publication Number Publication Date
JPS5969113A true JPS5969113A (en) 1984-04-19

Family

ID=16045790

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17828582A Pending JPS5969113A (en) 1982-10-13 1982-10-13 Thickener

Country Status (1)

Country Link
JP (1) JPS5969113A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100868332B1 (en) 2008-03-31 2008-11-12 (주)효성엔바이로 A sludge gathering apparatus having a waterway crushing part in a circle settling basin
JP2009067394A (en) * 2007-09-10 2009-04-02 Nippon Steel & Sumikin Metal Products Co Ltd Hoop material bending processing method and binding member manufacturing apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009067394A (en) * 2007-09-10 2009-04-02 Nippon Steel & Sumikin Metal Products Co Ltd Hoop material bending processing method and binding member manufacturing apparatus
KR100868332B1 (en) 2008-03-31 2008-11-12 (주)효성엔바이로 A sludge gathering apparatus having a waterway crushing part in a circle settling basin

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