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JP7097733B2 - Stirrer - Google Patents
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JP7097733B2 - Stirrer - Google Patents

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JP7097733B2
JP7097733B2 JP2018068963A JP2018068963A JP7097733B2 JP 7097733 B2 JP7097733 B2 JP 7097733B2 JP 2018068963 A JP2018068963 A JP 2018068963A JP 2018068963 A JP2018068963 A JP 2018068963A JP 7097733 B2 JP7097733 B2 JP 7097733B2
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flow path
opening
chamber portion
separation chamber
path chamber
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JP2019177358A (en
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浩史 上野
智生 石間
真治 市川
好一 加藤
健一 吾郷
孝宏 根本
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AQAS CORPORATION
SATAKE MULTIMIX CORPORATION
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SATAKE MULTIMIX CORPORATION
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  • Mixers Of The Rotary Stirring Type (AREA)
  • Activated Sludge Processes (AREA)

Description

本発明は撹拌装置、特に、微生物や触媒を担持した担体を有する排水などの液体を撹拌しながら処理する微生物反応装置や排水処理装置などの撹拌装置に関するものである。 The present invention relates to a stirrer, particularly a stirrer such as a microbial reaction device or a wastewater treatment device that treats a liquid such as wastewater having a carrier carrying a microorganism or a catalyst while stirring.

排水を処理するために、排水に微生物や触媒を担持した担体を撹拌して、排水を浄化する方法がある。 In order to treat the wastewater, there is a method of purifying the wastewater by stirring a carrier carrying a microorganism or a catalyst on the wastewater.

図19及び図20は従来の微生物反応装置などの撹拌装置を示し、1は、撹拌装置、2は、該撹拌装置1の処理槽を示し、該処理槽2は、例えば、槽径(直径)が1~10m、高さが、槽径に対して、0.5~5倍の高さの縦型の円筒状よりなる。 19 and 20 show a stirring device such as a conventional microbial reaction device, 1 is a stirring device, 2 is a processing tank of the stirring device 1, and the processing tank 2 is, for example, a tank diameter (diameter). The height is 1 to 10 m, and the height is 0.5 to 5 times the diameter of the tank, which is a vertical cylindrical shape.

3は、回転翼を示し、該回転翼3は、例えば、翼径が槽径に対して0.3~0.6倍の長さであり、前記処理槽2の上部から垂設された回転軸3aの下端に半径方向に放射状に固定される。 Reference numeral 3 is a rotary blade, wherein the rotary blade 3 has, for example, a blade diameter of 0.3 to 0.6 times the tank diameter, and is vertically installed from the upper part of the treatment tank 2. It is fixed radially to the lower end of the shaft 3a in a radial direction.

前記回転翼3は、例えば、4枚のフラットパドル翼などの矩形板状の翼板からなり、モータ等の駆動手段(図示せず)により前記回転軸3aを介して、前記処理槽2内に所望の高さまで容れられた液体内の上部、例えば、液面の近傍において回転するように設けられている。 The rotary blade 3 is composed of, for example, a rectangular plate-shaped blade plate such as four flat paddle blades, and is placed in the processing tank 2 via a rotary shaft 3a by a driving means (not shown) such as a motor. It is provided to rotate in the upper part of the liquid contained to a desired height, for example, in the vicinity of the liquid surface.

4は、静翼を示し、該静翼4は、例えば、4枚の複数の直線状の帯状板からなり、前記回転翼3の下方の前記処理槽2の底部2aの中心に放射状に等角度に離間して固定される。 Reference numeral 4 denotes a stationary blade, wherein the stationary blade 4 is composed of, for example, four plurality of linear strips, and is radially equiangular with the center of the bottom portion 2a of the processing tank 2 below the rotary blade 3. It is fixed apart from the wing.

また、前記各帯状板は、例えば、図20に示すように、該帯状板の交差部に相当する前記帯状体の中心部は互に間隙5を有すると共に、該各帯状板は、例えば、前記回転翼3の回転方向の前方で、前記底部2aの中心を通る半径線Rから間隔dを開けて並行に固定されている。 Further, in each of the strips, for example, as shown in FIG. 20, the central portions of the strips corresponding to the intersections of the strips have a gap 5 with each other, and the strips are, for example, the said. It is fixed in parallel in front of the rotary blade 3 in the rotation direction with a distance d from the radius line R passing through the center of the bottom portion 2a.

6は、流入管を示し、該流入管6は、例えば、前記処理槽2の側壁の下部に設けられ、処理すべき処理水などの液体を前記処理槽2内に容れるように設けられている。なお、該流入管6は、前記処理槽2の上部に設けてもよい。 Reference numeral 6 is an inflow pipe, which is provided, for example, in the lower part of the side wall of the treatment tank 2 so as to contain a liquid such as treated water to be treated in the treatment tank 2. .. The inflow pipe 6 may be provided in the upper part of the processing tank 2.

7は、担体分離室を示し、該担体分離室7は、例えば、上下方向に延びる箱体よりなり、前記処理槽2の側壁の外側に設けられ、下端において、前記処理槽2の側壁の下端に設けられた開口部8に連通し、上部において、排水を排出する排出口9が設けられている。 Reference numeral 7 denotes a carrier separation chamber, and the carrier separation chamber 7 is made of, for example, a box body extending in the vertical direction, is provided on the outside of the side wall of the treatment tank 2, and at the lower end, the lower end of the side wall of the treatment tank 2. A discharge port 9 is provided at the upper part so as to communicate with the opening 8 provided in the above.

前記従来の撹拌装置においては、微生物や触媒などを担持した担体を有する処理水などの液体を、前記処理槽2内に所望の高さまで流入させて、前記回転翼3を回転させることにより、前記処理槽2内の処理水は、図19に示すように、前記回転翼3により、半径方向外方に吐出されて、前記処理槽2の側壁内面に当接し、そして、該側壁内面に沿って旋回しながら下方の槽底部に向かう緩やかな下降流Pを形成し、その後、前記処理槽2の底部の中心部において、前記静翼4により、上昇流Qを引き起こし、これにより、前記回転翼3と前記静翼4との間で循環流が形成され、前記処理槽2内で例えば、低せん断かつ低動力により担体のダメージを防ぎ、液体の混合・均一分散化を図ることができるようになる。 In the conventional stirring device, a liquid such as treated water having a carrier carrying a microorganism, a catalyst, or the like is allowed to flow into the treatment tank 2 to a desired height, and the rotary blade 3 is rotated to rotate the rotary blade 3. As shown in FIG. 19, the treated water in the treatment tank 2 is discharged outward in the radial direction by the rotary blade 3, abuts on the inner surface of the side wall of the treatment tank 2, and is along the inner surface of the side wall. While swirling, a gentle downward flow P toward the bottom of the lower tank is formed, and then, in the central portion of the bottom of the treatment tank 2, the stationary blade 4 causes an upward flow Q, whereby the rotary blade 3 is formed. A circulating flow is formed between the blade and the stationary blade 4, and the carrier can be prevented from being damaged by, for example, low shear and low power in the processing tank 2, and the liquid can be mixed and uniformly dispersed. ..

また、生物処理等された処理水は、前記開口部8を通じて、前記担体分離室7に流入し、そして、処理水に含まれる担体は前記担体分離室7内で、下方に沈下し、前記開口部8から処理槽2内に戻され、担体のない処理水のみが、上部の前記排出口9から、外部に排出されるようになる。 Further, the treated water treated with organisms flows into the carrier separation chamber 7 through the opening 8, and the carrier contained in the treated water sinks downward in the carrier separation chamber 7 and the opening. It is returned to the treatment tank 2 from the part 8, and only the treated water without a carrier is discharged to the outside from the discharge port 9 at the upper part.

特開2000-246269号公報Japanese Unexamined Patent Publication No. 2000-246269

しかしながら、前記従来の担体分離室7では、該担体分離室7内に入り込んだ担体が、処理槽2内に戻りにくく、また、担体のない処理水のみを効率よく排出口9から外部に排出することができなかった。 However, in the conventional carrier separation chamber 7, the carrier that has entered the carrier separation chamber 7 is difficult to return to the treatment tank 2, and only the treated water without the carrier is efficiently discharged from the discharge port 9 to the outside. I couldn't.

本発明は、簡単な構成で、担体等の処理槽外部への排出を防ぎ、担体のない処理水のみを効率よく外部に排出できる撹拌装置を提供することを目的とする。 An object of the present invention is to provide a stirring device having a simple structure, preventing discharge of a carrier or the like to the outside of a treatment tank, and efficiently discharging only treated water without a carrier to the outside.

前記の目的を達成すべく、本発明の撹拌装置は、担体を有する液体が容れられる処理槽と、該処理槽内に設けられた回転翼と、前記処理槽の底部に固定された放射状に延びる静翼と、担体分離室とよりなり、該担体分離室は、前記処理槽内に連通するよう形成した上部開口部及び下部開口部とを有する流路室部と、前記流路室部の下部に連通するよう形成した排水用開口部と上部に設けた排出口とを有する分離室部とよりなることを特徴とする。 In order to achieve the above object, the stirring device of the present invention has a processing tank containing a liquid having a carrier, a rotary blade provided in the processing tank, and radially extending fixed to the bottom of the processing tank. The carrier separation chamber is composed of a stationary blade and a carrier separation chamber, and the carrier separation chamber has a flow path chamber portion having an upper opening and a lower opening formed so as to communicate with each other in the treatment tank, and a lower portion of the flow path chamber portion. It is characterized by comprising a separation chamber portion having a drainage opening formed so as to communicate with the above and a discharge port provided at the upper part.

また、前記下部開口部の、前記回転翼の回転方向の後方側には、該回転方向の前方側に向かって、前記処理槽内の中心方向側に傾斜したカバー板が設けられていることを特徴とする。 Further, on the rear side of the lower opening in the rotation direction of the rotary blade, a cover plate inclined toward the center direction in the processing tank is provided toward the front side in the rotation direction. It is a feature.

また、前記下部開口部は、該下部開口部の開口面積が、前記上部開口部の開口面積よりも大きく形成されていることを特徴とする。 Further, the lower opening is characterized in that the opening area of the lower opening is formed to be larger than the opening area of the upper opening.

また、前記流路室部は、上部の流路室部の流路断面積が、下部の流路室部の流路断面積よりも、小さく形成されていることを特徴とする。 Further, the flow path chamber portion is characterized in that the flow path cross-sectional area of the upper flow path chamber portion is formed smaller than the flow path cross-sectional area of the lower flow path chamber portion.

また、前記担体分離室は、第1の仕切板を有する箱体により形成され、前記流路室部と前記分離室部とは、該箱体の天井板から、下方の所望の位置まで延びる前記第1の仕切板により仕切られてそれぞれ形成されることを特徴とする。 Further, the carrier separation chamber is formed by a box body having a first partition plate, and the flow path chamber portion and the separation chamber portion extend from the ceiling plate of the box body to a desired position below. It is characterized in that it is partitioned by a first partition plate and each is formed.

また、前記流路室部は、上部の上部流路室部と下部の下部流路室部とにより形成され、前記上部の上部流路室部は、前記流路室部の天井板から、下方の所望の位置まで延びる第2の仕切板が設けられ、該第2の仕切板により、上部の上部流路室部の流路断面積が、下部の下部流路室部の流路断面積よりも、小さく形成されていることを特徴とする。 Further, the flow path chamber is formed by an upper upper flow path chamber and a lower lower flow path chamber, and the upper upper flow path chamber is below the ceiling plate of the flow path chamber. A second partition plate extending to a desired position is provided, and the second partition plate allows the flow path cross-sectional area of the upper upper flow path chamber portion to be larger than the flow path cross-sectional area of the lower lower flow path chamber portion. Is also characterized by being formed small.

また、前記第1の仕切板の下部には、前記下部開口部側に向かう下方に傾斜した傾斜面を有する整流部を設けたことを特徴とする。 Further, the lower portion of the first partition plate is provided with a straightening vane having a downwardly inclined inclined surface toward the lower opening side.

また、前記分離室部内に、前記第1の仕切板に対向する、底面から所望の高さまで延びる衝立板を更に設けたことを特徴とする。 Further, the separation chamber portion is further provided with a strut plate extending from the bottom surface to a desired height, which faces the first partition plate.

本発明は、簡単な構成で、担体等の処理槽外部への排出を防ぎ、担体のない処理水のみを効率よく外部に排出できる撹拌装置を提供することができる。 INDUSTRIAL APPLICABILITY The present invention can provide a stirring device having a simple structure, which prevents discharge of a carrier or the like to the outside of a treatment tank and can efficiently discharge only treated water without a carrier to the outside.

本発明の実施例1の撹拌装置の縦断側面図である。It is a vertical sectional side view of the stirring apparatus of Example 1 of this invention. 本発明の実施例1の撹拌装置の横断平面図である。It is a cross-sectional plan view of the stirring apparatus of Example 1 of this invention. 本発明の担体分離室の縦断側面図である。It is a vertical sectional side view of the carrier separation chamber of this invention. 本発明の、処理槽内から見た担体分離室の正面図である。It is a front view of the carrier separation chamber seen from the inside of a processing tank of this invention. 本発明の担体分離室の説明用斜視図である。It is an explanatory perspective view of the carrier separation chamber of this invention. 本発明の、カバー体を分離した担体分離室の説明用斜視図である。It is explanatory perspective view of the carrier separation chamber which separated the cover body of this invention. 本発明の担体分離室の他の実施例の縦断側面図である。It is a longitudinal side view of another Example of the carrier separation chamber of this invention. 本発明の担体分離室の説明用縦断側面図である。It is a vertical sectional side view for explanation of the carrier separation chamber of this invention. 本発明の担体分離室の説明用模式図である。It is a schematic diagram for explanation of the carrier separation chamber of this invention. 本発明の担体分離室の説明用模式図である。It is a schematic diagram for explanation of the carrier separation chamber of this invention. 本発明の担体分離室の説明用模式図である。It is a schematic diagram for explanation of the carrier separation chamber of this invention. 本発明の第2実施例の担体分離室の説明用斜視図である。It is explanatory perspective view of the carrier separation chamber of 2nd Example of this invention. 本発明の第2実施例の、処理槽内から見た担体分離室の説明用正面図である。It is an explanatory front view of the carrier separation chamber seen from the inside of the processing tank of the 2nd Example of this invention. 本発明の第3実施例の担体分離室の説明用縦断側面図である。It is a vertical sectional side view for explanation of the carrier separation chamber of the 3rd Example of this invention. 本発明の第3実施例の担体分離室の他の実施例の説明用斜視図である。It is a perspective view for explanation of another Example of the carrier separation chamber of the 3rd Example of this invention. 本発明の第3実施例の担体分離室の他の実施例の説明用縦断側面図である。It is a vertical sectional side view for explanation of another Example of the carrier separation chamber of the 3rd Example of this invention. 本発明の、処理槽内から見た担体分離室の他の例の正面図である。It is a front view of another example of the carrier separation chamber seen from the inside of a processing tank of this invention. 本発明の、処理槽内から見た担体分離室の更に他の例の正面図である。It is a front view of still another example of the carrier separation chamber seen from the inside of a processing tank of this invention. 従来の撹拌装置の縦断側面図である。It is a vertical sectional side view of the conventional stirring apparatus. 従来の撹拌装置の横断平面図である。It is a cross-sectional plan view of a conventional agitator.

本発明を実施するための形態の実施例を以下に示す。なお、前記従来例と同じ部分には、同じ符号を付け、説明を省略する。 Examples of embodiments for carrying out the present invention are shown below. The same parts as those in the conventional example are designated by the same reference numerals, and the description thereof will be omitted.

本発明の実施例1を図1~図11によって説明する。 Example 1 of the present invention will be described with reference to FIGS. 1 to 11.

(1.担体分離室の説明) (1. Explanation of carrier separation chamber)

本発明の撹拌装置10は、前記従来の撹拌装置1において、前記担体分離室7を用いる代わりに、前記処理槽2の側壁の外側に、担体分離室11を設ける。 In the conventional stirring device 1, the stirring device 10 of the present invention provides the carrier separation chamber 11 on the outside of the side wall of the processing tank 2 instead of using the carrier separation chamber 7.

該担体分離室11は、図1及び図2に示すように、流路室部12と分離室部13との前後又は左右に並列する2室よりなる。また、前記流路室部12は、上下方向に延びて形成され、前記処理槽2内からの処理水が入流するよう、前記処理槽2内に連通するよう形成した上部開口部14と、該流路室部12内に流入した処理水が、前記処理槽2内に流出するよう、前記処理槽2内に連通するよう形成した、前記上部開口部14よりも下方に設けた下部開口部15とを有する。また、前記分離室部13は、上下方向に延びて形成され、前記流路室部12内の処理水の一部が流入するよう、該流路室部12内の下部に連通するように形成された排水用開口部16を下部に有すると共に、上部に排出口17を有する。 As shown in FIGS. 1 and 2, the carrier separation chamber 11 is composed of two chambers in which the flow path chamber portion 12 and the separation chamber portion 13 are arranged in parallel in the front-rear direction or left and right. Further, the flow path chamber portion 12 is formed so as to extend in the vertical direction and communicate with the treatment tank 2 so that the treatment water from the treatment tank 2 can flow into the treatment tank 2 and the upper opening portion 14. A lower opening 15 provided below the upper opening 14 formed so as to allow the treated water flowing into the flow path chamber 12 to communicate with the treatment tank 2 so as to flow out into the treatment tank 2. And have. Further, the separation chamber portion 13 is formed so as to extend in the vertical direction and communicate with the lower portion in the flow path chamber portion 12 so that a part of the treated water in the flow path chamber portion 12 flows into the separation chamber portion 13. It has a drainage opening 16 at the bottom and a discharge port 17 at the top.

なお、前記上部開口部14から前記流路室部12内に流入した、前記処理槽2からの処理水が、前記排水用開口部16よりも、前記下部開口部15から流出しやすくするために、前記分離室部13の排水用開口部16の上端開口縁は、前記下部開口部15の上端開口縁と同じ高さ、あるいは、若干下方にあることが好ましい。 In order to make it easier for the treated water from the treatment tank 2 that has flowed into the flow path chamber 12 from the upper opening 14 to flow out from the lower opening 15 than the drainage opening 16. It is preferable that the upper end opening edge of the drainage opening 16 of the separation chamber 13 is at the same height as or slightly below the upper end opening edge of the lower opening 15.

(2.カバー体の説明) (2. Explanation of the cover body)

また、前記下部開口部15の、前記回転翼3の回転方向の後方側の縁部15aに、回転方向の前方側に向かって、処理槽2の中心方向側に傾斜して延びるカバー板18aを有するカバー体18を設け、前記処理槽2内の側壁の内周面を旋回する処理水が、前記下部開口部15から前記流路室部12内に入流することを防止するようにしてもよい。 Further, on the edge portion 15a of the lower opening portion 15 on the rear side in the rotation direction of the rotary blade 3, a cover plate 18a extending inclining toward the center direction side of the processing tank 2 toward the front side in the rotation direction is provided. The cover body 18 may be provided to prevent the treated water swirling around the inner peripheral surface of the side wall in the treatment tank 2 from flowing into the flow path chamber portion 12 from the lower opening 15. ..

(3.担体分離室の一例の説明) (3. Explanation of an example of the carrier separation chamber)

前記担体分離室11は、例えば、図3~図6に示すように、その面が互いに平行に対向して配置された垂直方向に延びる左右の側壁11a、11bと、前記処理槽2の側壁の外周面に固定された前面板11cと、該前面板11cの面に対向して配置された背面板11dと、底面板11eと、水平状に延びる天井板11fとの箱体に形成され、前記前面板11cの上端には、前記処理槽2内に連通した前記上部開口部14が形成されると共に、前記前面板11cの下端に、前記処理槽2内に連通した前記下部開口部15が形成される。 As shown in FIGS. 3 to 6, the carrier separation chamber 11 has left and right side walls 11a and 11b whose surfaces are arranged so as to face each other in parallel and extend in the vertical direction, and the side walls of the treatment tank 2. The front plate 11c fixed to the outer peripheral surface, the back plate 11d arranged to face the surface of the front plate 11c, the bottom plate 11e, and the horizontally extending ceiling plate 11f are formed in a box body. The upper opening 14 communicating with the inside of the processing tank 2 is formed at the upper end of the front plate 11c, and the lower opening 15 communicating with the inside of the processing tank 2 is formed at the lower end of the front plate 11c. Will be done.

なお、前記下部開口部15の開口面積は、前記上部開口部14の開口面積より大きく形成することが望ましい。 It is desirable that the opening area of the lower opening 15 is formed larger than the opening area of the upper opening 14.

なお、前記担体分離室11は、前記処理槽2の下方に設けられ、例えば、図1に示すように、前記処理槽の底部からの高さ(L1)が、例えば、槽径に対して0.1~0.5倍の高さに設けられる。 The carrier separation chamber 11 is provided below the treatment tank 2, and the height (L1) from the bottom of the treatment tank is, for example, 0 with respect to the tank diameter, as shown in FIG. It is installed at a height of 1 to 0.5 times.

また、前記箱体状の担体分離室11は、例えば、図3及び図4に示すように、縦方向の長さ(L2)が槽径に対して0.3~0.6倍の長さ、横方向(左右方向)の長さ(L3)が槽径に対して0.1~0.3倍の長さ、奥行きの長さ(L4)が槽径に対して0.2~0.4倍の長さである。 Further, as shown in FIGS. 3 and 4, for example, the box-shaped carrier separation chamber 11 has a length (L2) in the vertical direction of 0.3 to 0.6 times the tank diameter. The lateral length (L3) is 0.1 to 0.3 times the tank diameter, and the depth length (L4) is 0.2 to 0 to the tank diameter. It is four times as long.

また、前記箱体内において、前記前面板11cと前記背面板11dとの間に、前記箱体内を、前面側と背面側とに仕切る、例えば、両側辺が前記左右の側壁11a、11bに接続され、前記天井板11fから下方の所望の位置まで延びる、垂直状の矩形状の第1の仕切板19が設けられる。 Further, in the inside of the box, the inside of the box is divided into a front side and a back side between the front plate 11c and the back plate 11d, for example, both sides are connected to the left and right side walls 11a and 11b. , A vertical rectangular first partition plate 19 extending from the ceiling plate 11f to a desired position below is provided.

なお、前記第1の仕切板19は、図3に示すように、前記前面板11cから、所望の距離(L5)、例えば、槽径に対して0.05~0.2倍の距離、離間して設けられる。 As shown in FIG. 3, the first partition plate 19 is separated from the front plate 11c by a desired distance (L5), for example, a distance of 0.05 to 0.2 times the tank diameter. Is provided.

該第1の仕切板19は、天井板11fから、例えば、前記下部開口部15の上端縁と略同じ位置の高さまで延び、該第1の仕切板19の下端と前記底面板11eとの間には、排水用開口部16が形成されるようになる。 The first partition plate 19 extends from the ceiling plate 11f to, for example, a height substantially the same as the upper end edge of the lower opening 15, and is between the lower end of the first partition plate 19 and the bottom plate 11e. The drainage opening 16 will be formed in.

そして、前記第1の仕切板19により、前記箱体内において、該第1の仕切板19の一方の面側の一方の部屋と、他方の面側の他方の部屋との2室が形成され、それぞれ、前記流路室部12と分離室部13とが形成されるようになる。 Then, the first partition plate 19 forms two rooms in the box body, one room on one side of the first partition plate 19 and the other room on the other side. The flow path chamber portion 12 and the separation chamber portion 13 are formed, respectively.

即ち、前記箱体は、例えば、前記第1の仕切板19により、前後の2室に仕切られ、前面側が前記流路室部12となり、背面側が、前記分離室部13となる。 That is, the box body is divided into two front and rear chambers by, for example, the first partition plate 19, the front side becomes the flow path chamber portion 12, and the back side becomes the separation chamber portion 13.

なお、前記前面板11cは、前記処理槽2の側壁自体により構成されてもよい。 The front plate 11c may be formed of the side wall itself of the processing tank 2.

また、前記上部開口部14は、例えば、矩形状の開口に形成され、横方向(左右方向)が、前記左側の側壁11aから右側の側壁11bに至り、縦方向(上下方向)が、前記天井板11fから、下方に所望の長さ(L6)、例えば、槽径に対して0.01~0.1倍の長さで形成される。 Further, the upper opening 14 is formed in, for example, a rectangular opening, from the left side wall 11a to the right side wall 11b in the horizontal direction (left-right direction), and in the vertical direction (vertical direction) the ceiling. It is formed downward from the plate 11f with a desired length (L6), for example, 0.01 to 0.1 times the length of the tank diameter.

また、前記下部開口部15は、例えば、矩形状の開口に形成され、横方向(左右方向)が、前記左側の側壁11aから右側の側壁11bに至り、縦方向が、前記底面板11eから、上方に所望の長さ(L7)、例えば、槽径に対して0.05~0.2倍の長さに形成される。なお、前記下部開口部15の開口の縦方向の長さ(L7)は、前記上部開口部14の開口の縦方向の長さ(L6)よりも大きく形成するのが好ましく、これにより、より前記流路室部12内の処理水が、前記下部開口部15を通じて、前記処理槽2内に排出されやすくなる。 Further, the lower opening 15 is formed in, for example, a rectangular opening, and the lateral direction (left-right direction) reaches from the left side wall 11a to the right side wall 11b, and the vertical direction is from the bottom plate 11e. It is formed upward to a desired length (L7), for example, 0.05 to 0.2 times the tank diameter. It is preferable that the length (L7) of the opening of the lower opening 15 is larger than the length (L6) of the opening of the upper opening 14 in the vertical direction. The treated water in the flow path chamber portion 12 is easily discharged into the treatment tank 2 through the lower opening portion 15.

なお、前記底面板11eは、例えば、図3に示すように、凹状に湾曲させる以外に、図7に示すように、直線状に傾斜させるようにしてもよい。 The bottom plate 11e may be inclined linearly as shown in FIG. 7, in addition to being curved in a concave shape as shown in FIG. 3, for example.

また、前記底面板11eを、前記下部開口部15の縁部から水平状に延び、そこから、直線状に上方に傾斜させて、前記背面板11dに接続するようにしてもよい。 Further, the bottom plate 11e may extend horizontally from the edge of the lower opening 15 and be inclined upward in a straight line from there to be connected to the back plate 11d.

また、図4に示すように、前記下部開口部15を、前記上部開口部14の真下に設ける以外に、例えば、図17に示すように、前記上部開口部14を、回転翼3の回転方向の後方側に形成し、前記下部開口部15を、回転翼3の回転方向の前方側に形成して、前記下部開口部15を、前記上部開口部14に対して、回転翼3の回転方向に対して前方側の、斜め下方に設けるようにしてもよい。 Further, as shown in FIG. 4, in addition to providing the lower opening 15 directly below the upper opening 14, for example, as shown in FIG. 17, the upper opening 14 is provided in the rotation direction of the rotary blade 3. The lower opening 15 is formed on the rear side of the rotary blade 3 on the front side in the rotation direction of the rotary blade 3, and the lower opening 15 is formed on the rotation direction of the rotary blade 3 with respect to the upper opening 14. It may be provided diagonally downward on the front side with respect to the vehicle.

また、図18に示すように、前記流路室部12を、下方に向かうに従って、回転翼3の回転方向に対して前方側に向くように、斜め下方に傾斜させてもよい。 Further, as shown in FIG. 18, the flow path chamber portion 12 may be inclined diagonally downward so as to face forward with respect to the rotation direction of the rotary blade 3 toward the downward direction.

これらにより、前記処理槽2から前記流路室部12内に流入した液体の流速を高めることができ、前記液体内の担体が前記下部開口15から前記処理槽2内に戻りやすくなる。 As a result, the flow velocity of the liquid flowing from the processing tank 2 into the flow path chamber portion 12 can be increased, and the carrier in the liquid can easily return to the treatment tank 2 from the lower opening 15.

(4.カバー体の一例の説明) (4. Explanation of an example of the cover body)

また、前記カバー体18は、例えば、図5及び図6に示すように、前記下部開口部15の、回転翼3の回転方向の後方側の縁部15aに設けた、回転方向の前方側に向かって、前記処理槽2の中心方向側に傾斜して延びる、前記下部開口部15を略覆う大きさの、矩形状のカバー板18aと、該カバー板18aの上辺と前記下部開口部15の上辺縁とを連結した略三角形状の上板18bと、前記カバー板18aの下辺と前記下部開口部15の下辺縁とを連結した略三角形状の下板18cとよりなる、回転方向の前方側に、略正方形状の開口部18dが形成された断面三角形状の筒状で形成される。 Further, as shown in FIGS. 5 and 6, for example, the cover body 18 is provided on the rear side edge portion 15a of the rotary blade 3 in the rotational direction of the lower opening portion 15, and is provided on the front side in the rotational direction. A rectangular cover plate 18a having a size that substantially covers the lower opening 15 extending toward the center of the processing tank 2, and an upper side of the cover plate 18a and the lower opening 15 The front side in the rotation direction, which comprises a substantially triangular upper plate 18b connecting the upper edge and a substantially triangular lower plate 18c connecting the lower side of the cover plate 18a and the lower edge of the lower opening 15. In addition, it is formed in the shape of a cylinder having a triangular cross section in which a substantially square opening 18d is formed.

そして、前記流路室部12からの処理水が、前記下部開口部15を通じて、前記カバー体18内に流入し、該カバー体18の開口部18dから、前記処理槽2内に排出されるようになる。 Then, the treated water from the flow path chamber portion 12 flows into the cover body 18 through the lower opening portion 15 and is discharged into the processing tank 2 from the opening portion 18d of the cover body 18. become.

なお、前記下板18cを省略して、前記カバー体18の下部も開口するようにしてもよい。 The lower plate 18c may be omitted, and the lower portion of the cover body 18 may also be opened.

該カバー体18により、前記下部開口部15から前記流路室部12内に前記処理槽2内の処理水が逆流しないようになると共に、前記流路室部12内の処理水が、処理槽内に流出しやすいようになる。 The cover body 18 prevents the treated water in the treatment tank 2 from flowing back from the lower opening 15 into the flow path chamber portion 12, and the treated water in the flow path chamber portion 12 flows into the treatment tank. It becomes easy to leak inside.

(5.排水処理方法と効果の説明) (5. Explanation of wastewater treatment method and effect)

次に、前記実施例1の撹拌装置による処理方法と効果を説明する。 Next, the treatment method and the effect by the stirring device of the first embodiment will be described.

前記流入管6より、微生物や触媒などを担持した担体を有する処理水などの液体を、前記処理槽2内に所望の高さまで流入させて、前記液体を前記処理槽2内に貯めるようにする。 A liquid such as treated water having a carrier carrying a microorganism or a catalyst is allowed to flow into the treatment tank 2 to a desired height from the inflow pipe 6 so that the liquid is stored in the treatment tank 2. ..

前記回転翼3を回転させることにより、図1に示す前記処理槽2内において、担体を有する処理水は、図19に示す従来の装置と同様に、前記回転翼3により、半径方向外側に吐出されて処理槽2の側壁内面に当接して下方に流れて、前記処理槽2の側壁内面を旋回しながら緩やかに処理槽2の底部2aに向かう下降流Pが形成され、その後、該処理槽2の中心部の底部において、前記静翼4により、上昇流Qを引き起こし、これにより、前記回転翼3と前記静翼4との間において、循環流が形成され、前記処理槽2内で処理水の混合・均一分散化を図ることができるようになる。 By rotating the rotary blade 3, the treated water having a carrier in the processing tank 2 shown in FIG. 1 is discharged outward in the radial direction by the rotary blade 3 as in the conventional apparatus shown in FIG. Then, it abuts on the inner surface of the side wall of the treatment tank 2 and flows downward to slowly form a downward flow P toward the bottom 2a of the treatment tank 2 while swirling the inner surface of the side wall of the treatment tank 2. At the bottom of the central portion of 2, the stationary blade 4 causes an ascending current Q, whereby a circulating flow is formed between the rotary blade 3 and the stationary blade 4 and processed in the processing tank 2. It will be possible to mix and uniformly disperse water.

また、前記旋回する下降流Pの一部は、図8に示すように、前記上部開口部14から前記流路室部12内に流入し、前記流路部室12内で前記下降流Pの流れに沿った比較的流れの強い下降流Rを形成して、該流路室部12内を下降して、前記下部開口部15から処理槽2内に戻り、この際、前記流路室部12内を流れる、前記処理水よりも比重が重い担体は、前記下降流Rと共に、そのまま前記下部開口部15から前記カバー体18を介して前記処理槽2内に戻されるようなる。 Further, as shown in FIG. 8, a part of the swirling downward flow P flows into the flow path chamber 12 from the upper opening 14, and the flow of the downward flow P in the flow path chamber 12. A relatively strong downward flow R is formed along the flow path R, descends in the flow path chamber portion 12, and returns to the processing tank 2 from the lower opening portion 15, at this time, the flow path chamber portion 12. The carrier that flows inside and has a heavier specific gravity than the treated water is returned to the treatment tank 2 from the lower opening 15 as it is through the cover body 18 together with the descending flow R.

そして、前記排水用開口部16には、図8に示すように、担体のない処理水のみが流入するようになり、前記分離室部13内には、前記排出口17に向かう、前記下降流Rに比べて弱い流れの上昇する排出流Sが形成され、前記排出口17からは、担体の無い処理水のみを槽外に排出することができるようになる。 Then, as shown in FIG. 8, only the treated water without a carrier flows into the drainage opening 16, and the downward flow toward the discharge port 17 enters the separation chamber 13. A discharge flow S having a weaker flow than R is formed, and only the treated water without a carrier can be discharged to the outside of the tank from the discharge port 17.

また、一部の担体が前記分離室部13に流入しても、前記処理水よりも比重が重い担体は、下方に沈降し、前記排水用開口部16を通じて、前記流路室部12内に戻り、前記下部開口部15から前記処理槽2内に戻されるようになる。 Further, even if a part of the carrier flows into the separation chamber portion 13, the carrier having a specific gravity heavier than that of the treated water settles downward and enters the flow path chamber portion 12 through the drainage opening 16. It returns and is returned to the inside of the processing tank 2 from the lower opening 15.

また、前記カバー体18により、前記下部開口部15から、前記処理槽2内の旋回流が入り込まないようになるので、前記流路室部12内の下降流Rを妨げることがなく、担体の処理槽2内への流出がスムーズに行われるようになる。 Further, since the cover body 18 prevents the swirling flow in the processing tank 2 from entering from the lower opening 15, the carrier does not interfere with the downward flow R in the flow path chamber 12. The outflow into the processing tank 2 can be smoothly performed.

(6.仕切板の他の実施例の説明) (6. Explanation of other embodiments of the partition plate)

なお、前記垂直状に形成した第1の仕切板19においては、図9に示すように、前記分離室部13内の下部において、回転流が生じ、前記流路室部12内の担体が巻き込まれて、前記分離室部13内に入り込んでしまう場合がある。 In the vertically formed first partition plate 19, as shown in FIG. 9, a rotary flow is generated in the lower portion of the separation chamber portion 13, and the carrier in the flow path chamber portion 12 is involved. Then, it may enter the separation chamber portion 13.

そこで、図10に示すように、前記第1の仕切板19の下部に、上方から下方に向かうに従って、前記下部開口部15に向かって傾斜した傾斜面20aを有する、例えば、断面三角形状の三角柱状の整流部20を設ける。 Therefore, as shown in FIG. 10, the lower portion of the first partition plate 19 has an inclined surface 20a inclined toward the lower opening 15 from the upper side to the lower side, for example, a triangle having a triangular cross section. A columnar rectifying unit 20 is provided.

該整流部20の傾斜面20aにより、前記流路室部12内を通る処理水が、前記下部開口部15側に向かって流れるようになると共に、前記整流部20の下面の下部において回転流が形成され、前記分離室部13内に、担体が巻き込まれることが少なくなるようになる。 The inclined surface 20a of the rectifying portion 20 allows the treated water passing through the flow path chamber portion 12 to flow toward the lower opening portion 15, and a rotating flow is generated in the lower portion of the lower surface of the rectifying portion 20. It is formed so that the carrier is less likely to be involved in the separation chamber portion 13.

なお、前記断面三角形状の整流部20は、図10に示すように、前記傾斜面20aの下端から、前記仕切板19に向かう下面20bが、上方に向かうように形成され、該下面20bと前記第1の仕切板19とのなす角が鈍角状に形成され、この場合には、前記下面20bの下に、回転流が形成され、その回転流の一部が、前記分離室部13内に形成されるため、前記流路室部12内の担体が、前記分離室部13内に巻き込まれる恐れがある。 As shown in FIG. 10, the rectifying portion 20 having a triangular cross section is formed so that the lower surface 20b facing the partition plate 19 from the lower end of the inclined surface 20a faces upward, and the lower surface 20b and the above surface are formed. The angle formed by the first partition plate 19 is formed in an obtuse angle, and in this case, a rotary flow is formed under the lower surface 20b, and a part of the rotary flow is formed in the separation chamber portion 13. Since it is formed, the carrier in the flow path chamber portion 12 may be caught in the separation chamber portion 13.

そこで、図11に示すように、前記下面20bを、下方に向かって傾斜する傾斜面とし、該下面20bと前記第1の仕切板19とのなす角を鋭角又は直角とした断面三角形状の三角柱状の整流部20を設けることにより、下面に形成される回転流を流路室部側に発生させ、前記流路室部内の担体が、前記分離室部内に巻き込まれないようにしてもよい。 Therefore, as shown in FIG. 11, the lower surface 20b is an inclined surface that inclines downward, and the angle formed by the lower surface 20b and the first partition plate 19 is an acute angle or a right-angled triangular cross section. By providing the columnar rectifying portion 20, a rotating flow formed on the lower surface may be generated on the flow path chamber portion side so that the carrier in the flow path chamber portion is not caught in the separation chamber portion.

(7.担体分離室の他の実施例の説明) (7. Explanation of Other Examples of Carrier Separation Chamber)

本発明の第2の実施例の担体分離室21においては、前記第1の実施例において、前記担体分離室11の前記流路室部12を、下部の流路室部の流路断面積が、上部の流路室部の流路断面積に比べて大きくなるように形成し、そして、前記上部開口部14を前記上部の流路室部に形成し、前記下部開口部15を前記下部の流路室部に形成するようにする。 In the carrier separation chamber 21 of the second embodiment of the present invention, in the first embodiment, the flow path chamber portion 12 of the carrier separation chamber 11 has a flow path cross-sectional area of the lower flow path chamber portion. , The upper opening 14 is formed in the upper channel chamber, and the lower opening 15 is formed in the lower opening 15 so as to be larger than the cross-sectional area of the channel in the upper channel chamber. It is formed in the flow path chamber.

(8.流路室部の他の実施例の一例の説明) (8. Explanation of an example of another embodiment of the flow path chamber)

前記担体分離室21の流路室部12は、例えば、上部の上部流路室部12aと、その下部の下部流路室部12bにより形成され、該上部流路室部12aは、例えば、図12及び図13に示すように、前記第1の実施例の担体分離室11の前記流路室部12内に、上部の流路を狭めるための第2の仕切板22が設けられ、該第2の仕切板22と前記第1の仕切板19と前記右側の側壁11bと前記前面板11cとにより囲まれた部分により構成され、また、前記下部流路室部12bは、前記上部流路室部12aの下部の前記流路室部12により構成される。 The flow path chamber portion 12 of the carrier separation chamber 21 is formed by, for example, an upper upper flow path chamber portion 12a and a lower lower flow path chamber portion 12b thereof, and the upper flow path chamber portion 12a is, for example, the figure. As shown in 12 and FIG. 13, a second partition plate 22 for narrowing the upper flow path is provided in the flow path chamber portion 12 of the carrier separation chamber 11 of the first embodiment, and the second partition plate 22 is provided. The partition plate 22 of 2 is composed of a portion surrounded by the partition plate 22, the first partition plate 19, the right side wall 11b, and the front plate 11c, and the lower flow path chamber portion 12b is the upper flow path chamber. It is composed of the flow path chamber portion 12 below the portion 12a.

そして、図12(b)に示すように、前記下部流路室部12bの流路断面積Aは、前記上部流路室部12aの流路断面積Bに対して大きく形成されるようになる。 Then, as shown in FIG. 12B, the flow path cross-sectional area A of the lower flow path chamber portion 12b is formed larger than the flow path cross-sectional area B of the upper flow path chamber portion 12a. ..

そして、前記上部開口部14は、前記流路を狭められた上部流路室部12aの上部に形成され、前記下部開口部15は、前記下部流路室部12に形成されるようなる。 Then, the upper opening portion 14 is formed in the upper part of the upper flow path chamber portion 12a in which the flow path is narrowed, and the lower opening portion 15 is formed in the lower flow path chamber portion 12.

該第2の仕切板22は、例えば、前記左側の側壁11aと前記右側の側壁11bとの間、例えば、中間部分に、前記流路室部12内の上部を左側と右側に仕切る、例えば、前後辺が前記前側板11cと前記仕切板19に接続され、前記天井板11fから前記仕切板19の下端(又は、前記下部開口部の上部縁)まで延びる、垂直状の矩形状に形成される。 The second partition plate 22 partitions, for example, between the left side wall 11a and the right side wall 11b, for example, in the middle portion, and the upper part in the flow path chamber portion 12 to the left side and the right side, for example. The front and rear sides are connected to the front side plate 11c and the partition plate 19, and are formed in a vertical rectangular shape extending from the ceiling plate 11f to the lower end of the partition plate 19 (or the upper edge of the lower opening). ..

また、前記上部開口部14は、前記第2の仕切板22と前記右側の側壁11bとの間の、前記前面板11cの上端に形成される。 Further, the upper opening 14 is formed at the upper end of the front plate 11c between the second partition plate 22 and the right side wall 11b.

なお、前記第1の仕切板19は、前記上部流路室部12aの構成に不要な部分、例えば、前記左側の側壁11aから前記第2の仕切板22までの部分を省略してもよい。 The first partition plate 19 may omit a portion unnecessary for the configuration of the upper flow path chamber portion 12a, for example, a portion from the left side wall 11a to the second partition plate 22.

なお、前記上部開口部14は、例えば、矩形状の開口に形成され、横方向(左右方向)が、前記第2の仕切板22から右側の側壁11bに至り、縦方向(上下方向)が、前記天井板11fから、下方に所望の長さで形成される。 The upper opening 14 is formed, for example, in a rectangular opening, and the lateral direction (horizontal direction) reaches from the second partition plate 22 to the right side wall 11b, and the vertical direction (vertical direction) is. It is formed downward from the ceiling plate 11f to a desired length.

なお、前記上部開口部14の縦方向(上下方向)の長さは、例えば、前記L6と同様、槽径に対して0.01~0.1倍の長さ、下部開口部15の縦方向(上下方向)の長さは、例えば、前記L7と同様、槽径に対して0.05~0.2倍の長さである。 The length of the upper opening 14 in the vertical direction (vertical direction) is, for example, 0.01 to 0.1 times the diameter of the tank, as in the case of L6, in the vertical direction of the lower opening 15. The (vertical direction) length is, for example, 0.05 to 0.2 times the tank diameter, as in the case of L7.

(9.排水処理方法と効果) (9. Wastewater treatment method and effect)

本発明の第2の実施例においては、前記流路室部12に流入した処理水は、前記上部流路室部12aから、前記下方流路室部12bに流入する際に、流速が遅くなり、担体が前記下部開口部15から排出されやすくなり、これにより、前記排水用開口部16を通じて、前記分離室部13に入り込まなくなる。 In the second embodiment of the present invention, the flow velocity of the treated water flowing into the flow path chamber portion 12 becomes slow when flowing from the upper flow path chamber portion 12a into the lower flow path chamber portion 12b. The carrier is easily discharged from the lower opening 15, whereby the carrier does not enter the separation chamber 13 through the drain opening 16.

なお、例えば、前記第2実施例の担体分離室21において、図14に示すように、前記分離室部13に、前記第1の仕切板19の面に対向する、底面板11eから所望の上方まで延びる、垂直状の矩形板状の衝立板23を設けるようにしてもよい。 For example, in the carrier separation chamber 21 of the second embodiment, as shown in FIG. 14, the separation chamber portion 13 faces the surface of the first partition plate 19 and is desired above the bottom plate 11e. A vertical rectangular plate-shaped strut plate 23 may be provided.

なお、前記衝立板23は、例えば、その両側において、前記担体分離室21の左右の側壁11a、11bに接続され、前記第1の仕切板と所望の距離(L8)、例えば、槽径に対して0.01~0.05倍の距離、離間して設けられる。 The strut plate 23 is connected to the left and right side walls 11a and 11b of the carrier separation chamber 21 on both sides thereof, and is connected to the first partition plate at a desired distance (L8), for example, with respect to the tank diameter. It is provided at a distance of 0.01 to 0.05 times.

なお、前記排出口17は、例えば、前記衝立板23と前記背面板11dの間の天井板11fに設けるようにする。 The discharge port 17 is provided, for example, on the ceiling plate 11f between the counter plate 23 and the back plate 11d.

このように、前記分離室部13内に衝立板23を設けることにより、より担体が、前記分離室部13内に流入することを防ぐことができるようになる。 By providing the abutment plate 23 in the separation chamber portion 13 in this way, it becomes possible to further prevent the carrier from flowing into the separation chamber portion 13.

なお、図15及び図16は、前記担体分離室13において、前記衝立板23の上端辺と、前記背面板11dとを塞ぎ板24により塞いだ例を示す。 15 and 16 show an example in which the upper end side of the counter plate 23 and the back plate 11d are closed by the closing plate 24 in the carrier separation chamber 13.

この実施例においても、図16に示すように、担体分離をすることができるようになる。 Also in this embodiment, as shown in FIG. 16, carrier separation can be performed.

本発明の撹拌装置は、嫌気処理や、好気処理、脱窒・硝化処理などでも活用することができ、用途も電子産業、食品、畜産、農業、オフィス、下水など、産業排水や生活排水において利用可能である。 The stirring device of the present invention can also be used for anaerobic treatment, aerobic treatment, denitrification / nitrification treatment, etc., and is also used in industrial wastewater and domestic wastewater such as electronic industry, food, livestock, agriculture, office, and sewage. It is available.

1 撹拌装置
2 処理槽
2a 底部
3 回転翼
3a 回転軸
4 静翼
5 間隙
6 流入管
7 担体分離室
8 開口部
9 排出口
10 撹拌装置
11 担体分離室
11a 左側の側壁
11b 右側の側壁
11c 前面板
11d 背面板
11e 底面板
11f 天井板
12 流路室部
12a 上部流路室部
12b 下部流路室部
13 分離室部
14 上部開口部
15 下部開口部
15a 縁部
16 排水用開口部
17 排出口
18 カバー体
18a カバー板
18b 上板
18c 下板
18d 開口部
19 第1の仕切板
20 整流部
20a 傾斜面
20b 下面
21 担体分離室
22 第2の仕切板
23 衝立板
24 塞ぎ板
1 Stirrer 2 Processing tank 2a Bottom 3 Rotating blade 3a Rotating shaft 4 Static blade 5 Gap 6 Inflow pipe 7 Carrier separation chamber 8 Opening 9 Outlet 10 Stirring device 11 Carrier separation chamber 11a Left side wall 11b Right side wall 11c Front plate 11d Back plate 11e Bottom plate 11f Ceiling plate 12 Flow path chamber 12a Upper flow path chamber 12b Lower flow chamber 13 Separation chamber 14 Upper opening 15 Lower opening 15a Edge 16 Drainage opening 17 Discharge port 18 Cover body 18a Cover plate 18b Upper plate 18c Lower plate 18d Opening 19 First partition plate 20 Rectifying unit 20a Inclined surface 20b Lower surface 21 Carrier separation chamber 22 Second partition plate 23 Standing plate 24 Closing plate

Claims (13)

担体を有する液体が容れられる処理槽と、
該処理槽内に設けられた回転翼と、
前記処理槽の底部に固定された放射状に延びる静翼と、
担体分離室とよりなり、
該担体分離室は、前記処理槽内に連通するよう形成した上部開口部及び下部開口部とを有する流路室部と、前記流路室部の下部に連通するよう形成した排水用開口部と上部に設けた排出口とを有する分離室部とよりなり、
前記下部開口部の、前記回転翼の回転方向の後方側には、該回転方向の前方側に向かって、前記処理槽内の中心方向側に傾斜したカバー板が設けられていることを特徴とする撹拌装置。
A treatment tank that can hold a liquid with a carrier,
The rotor blades provided in the processing tank and
Radially extending stationary wings fixed to the bottom of the treatment tank,
Consisting with a carrier separation chamber,
The carrier separation chamber includes a flow path chamber portion having an upper opening and a lower opening formed to communicate with the inside of the treatment tank, and a drainage opening formed to communicate with the lower portion of the flow path chamber portion. It consists of a separation chamber having a discharge port provided at the top .
The lower opening is provided with a cover plate inclined toward the center in the processing tank toward the front side in the rotation direction on the rear side of the rotary blade in the rotation direction. Stirrer.
前記下部開口部は、該下部開口部の開口面積が、前記上部開口部の開口面積よりも大きく形成されていることを特徴とする請求項1に記載の撹拌装置。The stirring device according to claim 1, wherein the lower opening is formed so that the opening area of the lower opening is larger than the opening area of the upper opening. 前記流路室部は、上部の流路室部の流路断面積が、下部の流路室部の流路断面積よりも、小さく形成されていることを特徴とする請求項1または2に記載の撹拌装置。According to claim 1 or 2, the flow path chamber portion is formed so that the flow path cross-sectional area of the upper flow path chamber portion is smaller than the flow path cross-sectional area of the lower flow path chamber portion. The stirrer according to the description. 担体を有する液体が容れられる処理槽と、A treatment tank that can hold a liquid with a carrier,
該処理槽内に設けられた回転翼と、The rotor blades provided in the processing tank and
前記処理槽の底部に固定された放射状に延びる静翼と、Radially extending stationary wings fixed to the bottom of the treatment tank,
担体分離室とよりなり、Consisting with a carrier separation chamber,
該担体分離室は、前記処理槽内に連通するよう形成した上部開口部及び下部開口部とを有する流路室部と、前記流路室部の下部に連通するよう形成した排水用開口部と上部に設けた排出口とを有する分離室部とよりなり、The carrier separation chamber includes a flow path chamber portion having an upper opening and a lower opening formed to communicate with the inside of the treatment tank, and a drainage opening formed to communicate with the lower portion of the flow path chamber portion. It consists of a separation chamber having a discharge port provided at the top.
前記下部開口部は、該下部開口部の開口面積が、前記上部開口部の開口面積よりも大きく形成されていることを特徴とする撹拌装置。The lower opening is a stirring device characterized in that the opening area of the lower opening is formed to be larger than the opening area of the upper opening.
前記下部開口部の、前記回転翼の回転方向の後方側には、該回転方向の前方側に向かって、前記処理槽内の中心方向側に傾斜したカバー板が設けられていることを特徴とする請求項4に記載の撹拌装置。The lower opening is provided with a cover plate inclined toward the center in the processing tank toward the front side in the rotation direction on the rear side of the rotary blade in the rotation direction. The stirring device according to claim 4. 前記流路室部は、上部の流路室部の流路断面積が、下部の流路室部の流路断面積よりも、小さく形成されていることを特徴とする請求項4または5に記載の撹拌装置。According to claim 4 or 5, the flow path chamber portion is formed so that the flow path cross-sectional area of the upper flow path chamber portion is smaller than the flow path cross-sectional area of the lower flow path chamber portion. The stirrer according to the description. 担体を有する液体が容れられる処理槽と、A treatment tank that can hold a liquid with a carrier,
該処理槽内に設けられた回転翼と、The rotor blades provided in the processing tank and
前記処理槽の底部に固定された放射状に延びる静翼と、Radially extending stationary wings fixed to the bottom of the treatment tank,
担体分離室とよりなり、Consisting with a carrier separation chamber,
該担体分離室は、前記処理槽内に連通するよう形成した上部開口部及び下部開口部とを有する流路室部と、前記流路室部の下部に連通するよう形成した排水用開口部と上部に設けた排出口とを有する分離室部とよりなり、The carrier separation chamber includes a flow path chamber portion having an upper opening and a lower opening formed to communicate with the inside of the treatment tank, and a drainage opening formed to communicate with the lower portion of the flow path chamber portion. It consists of a separation chamber having a discharge port provided at the top.
前記流路室部は、上部の流路室部の流路断面積が、下部の流路室部の流路断面積よりも、小さく形成されていることを特徴とする撹拌装置。The flow path chamber portion is a stirring device characterized in that the flow path cross-sectional area of the upper flow path chamber portion is formed smaller than the flow path cross-sectional area of the lower flow path chamber portion.
前記下部開口部の、前記回転翼の回転方向の後方側には、該回転方向の前方側に向かって、前記処理槽内の中心方向側に傾斜したカバー板が設けられていることを特徴とする請求項7に記載の撹拌装置。The lower opening is provided with a cover plate inclined toward the center in the processing tank toward the front side in the rotation direction on the rear side of the rotary blade in the rotation direction. The stirring device according to claim 7. 前記下部開口部は、該下部開口部の開口面積が、前記上部開口部の開口面積よりも大きく形成されていることを特徴とする請求項7または8に記載の撹拌装置。The stirring device according to claim 7 or 8, wherein the lower opening is formed so that the opening area of the lower opening is larger than the opening area of the upper opening. 前記担体分離室は、第1の仕切板を有する箱体により形成され、The carrier separation chamber is formed by a box having a first partition plate.
前記流路室部と前記分離室部とは、該箱体の天井板から、下方の所望の位置まで延びる前記第1の仕切板により仕切られてそれぞれ形成されることを特徴とする請求項1乃至9のいずれか1に記載の撹拌装置。Claim 1 is characterized in that the flow path chamber portion and the separation chamber portion are separated from the ceiling plate of the box body by the first partition plate extending downward to a desired position. The stirring device according to any one of 9 to 9.
前記流路室部は、上部の上部流路室部と下部の下部流路室部とにより形成され、The flow path chamber is formed by an upper upper flow path chamber and a lower lower flow path chamber.
前記上部の上部流路室部は、前記流路室部の天井板から、下方の所望の位置まで延びる第2の仕切板が設けられ、The upper upper flow path chamber portion is provided with a second partition plate extending from the ceiling plate of the flow path chamber portion to a desired position below.
該第2の仕切板により、上部の上部流路室部の流路断面積が、下部の下部流路室部の流路断面積よりも、小さく形成されていることを特徴とする請求項10に記載の撹拌装置。10. The second partition plate is characterized in that the flow path cross-sectional area of the upper upper flow path chamber portion is formed smaller than the flow path cross-sectional area of the lower lower flow path chamber portion. The agitator according to.
前記第1の仕切板の下部には、前記下部開口部側に向かう下方に傾斜した傾斜面を有する整流部を設けたことを特徴とする請求項10または11に記載の撹拌装置。The stirring device according to claim 10 or 11, wherein a rectifying portion having a downwardly inclined inclined surface toward the lower opening side is provided in the lower portion of the first partition plate. 前記分離室部内に、前記第1の仕切板に対向する、底面から所望の高さまで延びる衝立板を更に設けたことを特徴とする請求項10、11または12に記載の撹拌装置。The stirring device according to claim 10, 11 or 12, further comprising a strut plate extending from the bottom surface to a desired height in the separation chamber portion, which faces the first partition plate.
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Citations (3)

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Publication number Priority date Publication date Assignee Title
JP2000246269A (en) 1999-02-26 2000-09-12 Nec Environment Eng Ltd Wastewater treatment equipment
JP2003019489A (en) 2001-07-10 2003-01-21 Nec Ameniplantex Ltd Waste water treatment equipment
JP2012030155A (en) 2010-07-29 2012-02-16 Satake Chemical Equipment Mfg Ltd Wastewater treatment apparatus and wastewater treatment method

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JPS5372762U (en) * 1976-11-19 1978-06-17
JPH08103781A (en) * 1994-10-06 1996-04-23 Nitto Seimo Kk Polluted water treatment method and device therefor using spherical material of small diameter on which bacteria are deposited

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000246269A (en) 1999-02-26 2000-09-12 Nec Environment Eng Ltd Wastewater treatment equipment
JP2003019489A (en) 2001-07-10 2003-01-21 Nec Ameniplantex Ltd Waste water treatment equipment
JP2012030155A (en) 2010-07-29 2012-02-16 Satake Chemical Equipment Mfg Ltd Wastewater treatment apparatus and wastewater treatment method

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