JP7333246B2 - Pretreatment device for portable wastewater treatment evaluation and wastewater treatment evaluation method - Google Patents

Pretreatment device for portable wastewater treatment evaluation and wastewater treatment evaluation method Download PDF

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JP7333246B2
JP7333246B2 JP2019196431A JP2019196431A JP7333246B2 JP 7333246 B2 JP7333246 B2 JP 7333246B2 JP 2019196431 A JP2019196431 A JP 2019196431A JP 2019196431 A JP2019196431 A JP 2019196431A JP 7333246 B2 JP7333246 B2 JP 7333246B2
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勇人 斎藤
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Cosmo Oil Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Description

本発明は、携帯型排水処理評価用前処理装置および排水処理評価方法に関する。 TECHNICAL FIELD The present invention relates to a portable pretreatment device for wastewater treatment evaluation and a wastewater treatment evaluation method.

従来より、各種産業において、有機物を含む工業排水が活性汚泥法により処理されるようになっている(例えば、特許文献1(特開2002-210486号公報)参照)。
活性汚泥法は有機排水を好気的に生物処理する方法であり、例えば、標準活性汚泥法においては、活性汚泥処理槽のBOD-SS負荷(曝気槽内の単位MLSS量(kg)あたり1日に加えられる汚水中のBOD量)が0.2~0.4kgBOD/(kgMLSS・日)程度になるようにプロセス設計されている。
BACKGROUND ART Conventionally, in various industries, industrial wastewater containing organic substances has been treated by an activated sludge method (see, for example, Patent Document 1 (Japanese Unexamined Patent Application Publication No. 2002-210486)).
The activated sludge method is a method of biologically treating organic wastewater aerobically. The process is designed so that the amount of BOD in the wastewater added to the waste water is about 0.2 to 0.4 kgBOD/(kgMLSS/day).

上記活性汚泥法による排水処理方法としては、例えば、各種工場から排出される工業排水を一旦バッファタンクに集合した後、このバッファタンク中の工業排水に対し、油水分離処理、凝集処理(凝集沈殿処理または凝集浮上処理)等の一次処理を行い、次いで活性汚泥処理等の二次処理を行うことにより、工業排水中のフェノール、ベンゼン等の有機物や、窒素、リン等が排出基準以下になるように生物処理を行っている。 As a wastewater treatment method by the activated sludge method, for example, after collecting industrial wastewater discharged from various factories in a buffer tank, the industrial wastewater in this buffer tank is subjected to oil-water separation treatment, coagulation treatment (coagulation sedimentation treatment) Or coagulation flotation treatment), etc.), and then secondary treatment such as activated sludge treatment, so that organic matter such as phenol, benzene, etc., nitrogen, phosphorus, etc. We are doing biological treatment.

特開2002-210486号公報Japanese Patent Application Laid-Open No. 2002-210486

しかしながら、上記活性汚泥法による排水処理は、例えば各種排水の排出源となる製造プロセスの運転条件変更等に伴って、排水中の有機物や、窒素、リン等の量も変動することから、各種排出基準を満たす上で、排水処理設備の運転条件、特に活性汚泥処理装置の運転条件を適宜変更する必要がある。
上記活性汚泥処理装置の運転条件を決定するに際し、排水を直接活性汚泥処理装置に導入することは活性汚泥に与える負荷を必ずしも予測し得ないことから、活性汚泥処理装置を模して作製された据え付け型の評価装置に上記排水を導入して各種排水処理条件を決定することが考えられる。
However, in the wastewater treatment by the activated sludge method, the amount of organic matter, nitrogen, phosphorus, etc. In order to meet the standards, it is necessary to appropriately change the operating conditions of wastewater treatment facilities, especially the operating conditions of activated sludge treatment equipment.
When determining the operating conditions of the activated sludge treatment apparatus, it is not always possible to predict the load on the activated sludge if waste water is introduced directly into the activated sludge treatment apparatus. It is conceivable to introduce the above-described waste water into a stationary evaluation device and determine various waste water treatment conditions.

一方、評価対象となる排水処理プラントが評価装置の設置場所から遠方に位置している場合、上記排水処理プラントから排水や活性汚泥を評価装置の設置場所まで逐一持ち込んだ上で、各種規制値を満たすように試行錯誤的に排水処理条件を決定し、係る排水処理条件を排水処理プラントにフィードバックする必要があり、一旦決定した排水処理条件が必ずしも評価対象となる排水処理施設に適合したものになっていない場合には、再度評価装置を用いて排水処理条件を修正する必要がある。
この場合、評価対象となる排水処理プラントが例えば海外等の遠方に位置する場合には、排水処理プラントの排水処理条件を決定する迄に、排水処理プラントから評価装置の設置箇所まで排水や活性汚泥を移送したり、排水処理施設の操業者側と評価装置による評価側で煩雑な情報交換が必要となるばかりか、排水や活性汚泥自体の持ち出しまたは持ち込みが規制される場合や、排水や活性汚泥を評価装置迄移送するまでに変質する場合も想定されることから、必ずしも適切な評価を行い難かった。
On the other hand, if the wastewater treatment plant to be evaluated is located far from the installation location of the evaluation equipment, the wastewater and activated sludge from the wastewater treatment plant are brought to the installation location of the evaluation equipment one by one, and various regulation values are set. It is necessary to determine the wastewater treatment conditions through trial and error so as to satisfy the requirements and feed back the relevant wastewater treatment conditions to the wastewater treatment plant. If not, it is necessary to correct the wastewater treatment conditions using the evaluation device again.
In this case, if the wastewater treatment plant to be evaluated is located in a distant place such as overseas, wastewater or activated sludge from the wastewater treatment plant to the installation location of the evaluation device may be required before determining the wastewater treatment conditions of the wastewater treatment plant. Not only is it necessary to exchange complicated information between the operator of the wastewater treatment facility and the evaluation side using the evaluation device, but there are restrictions on taking out or bringing in wastewater or activated sludge itself, and wastewater or activated sludge Therefore, it was difficult to perform appropriate evaluation because it is assumed that the quality of the material may deteriorate before it is transported to the evaluation apparatus.

このような状況下、本発明者等は、排水処理施設に小型の活性汚泥処理設備を併設し、実際の排水処理プラントにおける活性汚泥処理装置と同様の条件で処理して処理水を得ることにより、短時間にかつ簡便に排水処理条件を評価し得ることを着想した。 Under such circumstances, the present inventors installed a small activated sludge treatment facility in the wastewater treatment facility and obtained treated water by treating under the same conditions as the activated sludge treatment equipment in the actual wastewater treatment plant. , it was conceived that wastewater treatment conditions can be evaluated easily in a short time.

ところで、上記小型の活性汚泥処理設備は、恒久的な設備である必要はなく一時的な設備であれば足り、また、海外等への運搬の利便性を考慮すると、排水処理施設に持ち運び可能な携帯性を有するものが求められる。
一方、排水処理条件を適切に評価するためには、小型の活性汚泥処理設備とともに、前処理装置として凝集処理(凝集沈殿処理または凝集浮上処理)を行うための小型の凝集槽も求められる。
By the way, the above-mentioned small activated sludge treatment facility does not need to be a permanent facility, and it is sufficient if it is a temporary facility. A device with portability is required.
On the other hand, in order to properly evaluate wastewater treatment conditions, a small coagulation tank for performing coagulation treatment (coagulation sedimentation treatment or coagulation flotation treatment) as a pretreatment device is required along with a small activated sludge treatment facility.

しかしながら、本発明者等が検討したところ、処理対象となる排水が油分やSS(Suspended Solids;浮遊物質)等を含むものである場合、凝集槽に排水を流入して処理しようとすると、槽壁に浮遊物質の付着物が層状に生成することが判明した。実際の排水処理プラントにおいては、凝集槽のスケールが非常に大きいために上記槽壁への付着物の生成やその量は無視し得る程度のものであるが、凝集槽のサイズを携帯可能な程度まで小型化した場合には、槽壁へ生じる付着物の存在が無視し得なくなって、適切な凝集処理を行い難くなる。
この場合、小型の凝集槽設備の運転を停止して槽壁を清掃した後、再度運転する必要が生じることから、迅速かつ的確な排水処理評価を行い難くなる。
However, as a result of investigation by the present inventors, when the wastewater to be treated contains oil, SS (suspended solids), etc., if the wastewater is to be treated by flowing into the flocculation tank, it will float on the tank wall. It was found that deposits of substances were formed in layers. In an actual wastewater treatment plant, the scale of the flocculation tank is so large that the formation and amount of deposits on the walls of the tank are negligible, but the size of the flocculation tank is portable. If the size is reduced to 10, the presence of deposits on the tank wall cannot be ignored, making it difficult to carry out appropriate agglomeration treatment.
In this case, it is necessary to stop the operation of the small-sized flocculation tank equipment, clean the tank walls, and then restart the operation, which makes it difficult to quickly and accurately evaluate wastewater treatment.

従って、本発明によれば、槽壁への付着物層の形成を抑制しつつ簡便かつ迅速に排水処理条件を評価するための携帯型排水処理評価前処理装置および排水処理評価方法を提供することを目的とするものである。 Therefore, according to the present invention, there is provided a portable wastewater treatment evaluation pretreatment device and a wastewater treatment evaluation method for simply and quickly evaluating wastewater treatment conditions while suppressing the formation of deposit layers on tank walls. It is intended for

このような状況下、本発明者等が鋭意検討したところ、携帯型排水処理評価用前処理装置であって、排水が流入する内容量3~12Lの凝集槽と、前記凝集槽の槽内に、外縁部の少なくとも一部に柔軟性樹脂からなる拡幅部が設けられた攪拌羽根と、前記攪拌羽根を凝集槽の上下方向に位置調整可能な上下位置移動手段とを有し、前記攪拌羽根の拡幅部が撹拌羽根の回転時に凝集槽の内壁に接触し得るように配置されている携帯型排水処理評価用前処理装置により上記技術課題を解決し得ることを見出し、本知見に基づいて本発明を完成するに至った。 Under these circumstances, the inventors of the present invention have made intensive studies and found that a portable pretreatment device for evaluating wastewater treatment includes a coagulation tank with an internal capacity of 3 to 12 L into which wastewater flows, and a tank in the coagulation tank. , a stirring blade provided with a widened portion made of a flexible resin on at least a part of the outer edge, and a vertical position moving means capable of adjusting the position of the stirring blade in the vertical direction of the aggregation tank, and the stirring blade We have found that the above technical problems can be solved by a portable pretreatment device for evaluating wastewater treatment, in which the widened portion is arranged so as to be able to contact the inner wall of the flocculation tank when the stirring blade rotates, and the present invention is based on this finding. was completed.

すなわち、本発明は、
(1)携帯型排水処理評価用前処理装置であって、
排水が流入する内容量3~12Lの凝集槽と、
前記凝集槽の槽内に、外縁部の少なくとも一部に柔軟性樹脂からなる拡幅部が設けられた攪拌羽根と、
前記攪拌羽根を凝集槽の上下方向に位置調整可能な上下位置移動手段とを有し、
前記攪拌羽根の拡幅部が撹拌羽根の回転時に凝集槽の内壁に接触し得るように配置されている
ことを特徴とする携帯型排水処理評価用前処理装置、
(2)前記攪拌羽根が攪拌プロペラである上記(1)に記載の携帯型排水処理評価用前処理装置、
(3)前記凝集槽と連通し当該凝集槽で処理された凝集物処理水を貯留する貯留室をさらに有するとともに、当該貯留室に貯留した凝集物処理水を排出する排出管を有し、
当該排出管の取水口が前記貯留室内に引き込まれるとともに前記貯留した凝集物処理水の水面近傍に位置するように上下移動可能に配置されている
上記(1)または(2)に記載の携帯型排水処理評価用前処理装置、および
(4)上記(1)~(3)のいずれかに記載の携帯型排水処理評価用前処理装置を用いて排水処理することを特徴とする排水処理評価方法
を提供するものである。
That is, the present invention
(1) A portable pretreatment device for evaluating wastewater treatment,
A coagulation tank with an internal volume of 3 to 12 L into which waste water flows;
a stirring blade provided with a widened portion made of a flexible resin on at least a part of an outer edge portion in the tank of the aggregation tank;
A vertical position moving means capable of adjusting the position of the stirring blade in the vertical direction of the aggregation tank,
A portable pretreatment device for wastewater treatment evaluation, wherein the widened portion of the stirring blade is arranged so as to be in contact with the inner wall of the flocculation tank when the stirring blade rotates,
(2) The portable pretreatment device for evaluating wastewater treatment according to (1) above, wherein the stirring blade is a stirring propeller;
(3) further comprising a storage chamber communicating with the aggregation tank and storing the aggregate-treated water treated in the aggregation tank, and having a discharge pipe for discharging the aggregate-treated water stored in the storage chamber;
The portable type according to (1) or (2) above, wherein the water intake port of the discharge pipe is pulled into the storage chamber and is arranged so as to be vertically movable so as to be positioned near the surface of the stored aggregate-treated water. and (4) a wastewater treatment evaluation method comprising treating wastewater using the portable pretreatment equipment for wastewater treatment evaluation according to any one of (1) to (3) above. It provides

本発明によれば、凝集槽内に設けられた攪拌羽根が外縁部の少なくとも一部に柔軟性樹脂からなる拡幅部を有し、係る拡幅部が撹拌羽根の回転時に凝集槽の内壁に接触し得るように配置されるとともに、上記攪拌羽根が上下位置移動手段により凝集槽の上下方向に移動可能に配置されていることにより、槽壁に生成した付着物を除去しつつ好適に凝集処理を行うことが可能となる。
このため、本発明によれば、槽壁への付着物層の形成を抑制しつつ簡便かつ迅速に排水処理条件を評価するための携帯型排水処理評価前処理装置および排水処理評価方法を提供することができる。
According to the present invention, the stirring blade provided in the coagulation tank has a widened portion made of a flexible resin on at least a part of the outer edge, and the widened portion contacts the inner wall of the coagulation tank when the stirring blade rotates. In addition, the stirring blade is arranged so as to be movable in the vertical direction of the coagulation tank by the vertical position moving means, so that the coagulation treatment is preferably performed while removing the deposits generated on the tank wall. becomes possible.
Therefore, according to the present invention, there is provided a portable wastewater treatment evaluation pretreatment device and a wastewater treatment evaluation method for simply and quickly evaluating wastewater treatment conditions while suppressing the formation of deposit layers on tank walls. be able to.

本発明に係る携帯型排水処理評価用前処理装置の形態例を説明するための概略図(斜視図)である。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram (perspective view) for explaining an example of the form of a portable pretreatment device for evaluation of wastewater treatment according to the present invention; 本発明に係る携帯型排水処理評価用前処理装置の形態例を説明するための概略図(正面図)である。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram (front view) for explaining an example of the form of a portable pretreatment device for evaluation of wastewater treatment according to the present invention; 本発明に係る携帯用排水処理評価用前処理装置において、撹拌羽根の形態例を示す概略図である。FIG. 2 is a schematic diagram showing an example of the form of the stirring blade in the portable pretreatment device for wastewater treatment evaluation according to the present invention. 本発明に係る携帯用排水処理評価用前処理装置において、撹拌羽根の形態例を示す概略図である。FIG. 2 is a schematic diagram showing an example of the form of a stirring blade in the portable pretreatment device for wastewater treatment evaluation according to the present invention. 本発明に係る携帯用排水処理評価用前処理装置において、撹拌羽根の上下位置移動形態例を示す概略図である。FIG. 2 is a schematic diagram showing an example of vertical position movement of the stirring blade in the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention. 本発明に係る携帯用排水処理評価用前処理装置において、撹拌羽根の上下位置移動形態例を示す概略図である。FIG. 2 is a schematic diagram showing an example of vertical position movement of the stirring blade in the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention. 本発明に係る携帯型排水処理評価用前処理装置の他の形態例を説明するための概略図(斜視図)である。FIG. 3 is a schematic diagram (perspective view) for explaining another embodiment of the portable pretreatment apparatus for evaluation of wastewater treatment according to the present invention. 本発明に係る携帯型排水処理評価用前処理装置を用いた排水処理評価の実施形態例を説明するための概略図である。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram for explaining an embodiment of wastewater treatment evaluation using a portable pretreatment device for wastewater treatment evaluation according to the present invention;

本発明に係る携帯型排水処理評価用前処理装置は、排水が流入する内容量3~12Lの凝集槽と、前記凝集槽の槽内に、外縁部の少なくとも一部に柔軟性樹脂からなる拡幅部が設けられた攪拌羽根と、前記攪拌羽根を凝集槽の上下方向に位置調整可能な上下位置移動手段とを有し、前記攪拌羽根の拡幅部が撹拌羽根の回転時に凝集槽の内壁に接触し得るように配置されていることを特徴とするものである。 A portable pretreatment device for evaluating wastewater treatment according to the present invention includes a flocculation tank with an internal capacity of 3 to 12 L into which wastewater flows, and a widened width made of a flexible resin at least part of the outer edge in the flocculation tank. and a vertical position moving means capable of adjusting the position of the stirring blade in the vertical direction of the coagulation tank, and the widened portion of the stirring blade contacts the inner wall of the coagulation tank when the stirring blade rotates. It is characterized by being arranged so as to be able to

以下、本発明に係る携帯型排水処理評価前処理装置について、適宜図面を参照しつつ説明するものとする。 DESCRIPTION OF THE PREFERRED EMBODIMENTS A portable pretreatment apparatus for wastewater treatment evaluation according to the present invention will be described below with appropriate reference to the drawings.

本発明に係る携帯型排水処理評価用前処理装置において、処理対象となる排水は、通常活性汚泥処理装置で処理される有機物含有排水であれば特に制限されない。
例えば、各種石油留分、潤滑油、有機溶剤、油脂、糖液、発酵液等の有機物を含有する工業排水、生活排水等から選ばれる一種以上であってもよいし、これ等の工業排水および生活排水等から選ばれる一種以上に油水分離処理を施したものであってもよい。
In the portable pretreatment apparatus for evaluating wastewater treatment according to the present invention, wastewater to be treated is not particularly limited as long as it is organic matter-containing wastewater that is usually treated with an activated sludge treatment apparatus.
For example, it may be one or more selected from industrial wastewater containing organic substances such as various petroleum fractions, lubricating oils, organic solvents, oils and fats, sugar solutions, fermentation liquids, etc., domestic wastewater, etc., and these industrial wastewater and One or more kinds selected from domestic wastewater or the like may be subjected to oil-water separation treatment.

図1および図2は、本発明に係る携帯型排水処理評価用前処理装置の形態例を説明するための概略図であり、図1が斜視図、図2が正面図に相当する。 1 and 2 are schematic diagrams for explaining an example of the form of a portable pretreatment apparatus for wastewater treatment evaluation according to the present invention, where FIG. 1 corresponds to a perspective view and FIG. 2 corresponds to a front view.

図1に示すように、本発明に係る携帯型排水処理評価用前処理装置10は、排水が流入する凝集槽11と、攪拌羽根12と、係る攪拌羽根12を凝集槽11の上下方向に上下移動可能に位置調整可能な上下位置移動手段14とを備えている。 As shown in FIG. 1, a portable pretreatment apparatus 10 for evaluation of wastewater treatment according to the present invention includes a flocculation tank 11 into which wastewater flows, a stirring blade 12, and the agitating blade 12 is vertically arranged in the vertical direction of the flocculation tank 11. A vertical position moving means 14 whose position is movably adjustable is provided.

本発明に係る携帯型排水処理評価用前処理装置において、凝集槽は、その内容量が、3~12Lであるものであり、4~10Lであるものが好ましく、5~8Lであるものがより好ましい。
凝集槽の内容量が上記範囲内にあることにより、携帯性を有しつつも、実機(実際の排水処理プラントにおける凝集槽)と同様の条件下における凝集処理を省スペースで簡便に行うことができる。
In the portable wastewater treatment evaluation pretreatment device according to the present invention, the content of the coagulation tank is 3 to 12 L, preferably 4 to 10 L, more preferably 5 to 8 L. preferable.
Since the content of the coagulation tank is within the above range, it is possible to easily perform coagulation treatment in a space-saving manner under the same conditions as the actual equipment (coagulation tank in an actual wastewater treatment plant) while maintaining portability. can.

本発明に係る携帯型排水処理評価用前処理装置において、凝集槽の形態は特に制限されないが、通常その形態は、排水を流入して凝集処理する槽の内部形状が概略円筒形状を有することが好ましい。
凝集槽の内部形状が円筒形状である場合、そのサイズは、内径150~250mm、高さ100~500mm程度であることが好ましい。
凝集槽内のサイズが上記範囲内にあることにより、携帯性を有しつつも、実機と同様の条件下における活性汚泥処理を省スペースで簡便に行うことができる。
In the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention, the form of the flocculation tank is not particularly limited, but the form is usually such that the internal shape of the tank into which the wastewater flows and is flocculated has a substantially cylindrical shape. preferable.
When the internal shape of the aggregation tank is cylindrical, the size is preferably about 150 to 250 mm in inner diameter and 100 to 500 mm in height.
Since the size of the inside of the coagulation tank is within the above range, the activated sludge treatment can be easily performed in a space-saving manner under the same conditions as in the actual machine while maintaining portability.

凝集槽は、通常、処理対象となる排水の流入口および凝集処理後の排水の流出口を有している。
図1および図2に例示する凝集槽11においては、図に示す流入口Dinより排水が流入し、槽内で凝集処理された排水が流出口Doutより流出する。
The coagulation tank usually has an inlet for waste water to be treated and an outlet for waste water after coagulation treatment.
In the flocculation tank 11 illustrated in FIGS. 1 and 2, waste water flows in from the inlet Din shown in the figures, and waste water that has been flocculated in the tank flows out from the outlet Dout.

図1および図2に例示するように、本発明に係る携帯型排水処理評価用前処理装置において、凝集槽11は、概略円筒形状を有する槽の底部にテーパー状の仕切り板P3を設けることにより、垂直方向上部から下部に向かって内径が狭まるテーパー状の(逆円錐状の)底部Bを有していてもよい。 As exemplified in FIGS. 1 and 2, in the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention, the flocculation tank 11 has a substantially cylindrical shape and is provided with a tapered partition plate P3 at the bottom of the tank. , and may have a tapered (inverted conical) bottom portion B with an inner diameter that narrows from top to bottom in the vertical direction.

凝集槽がテーパー状の底部を有することにより、凝集槽内で凝集、沈降した凝集物を凝集槽の最下部から容易に抜き出すことができる。 Since the flocculation tank has a tapered bottom, the flocculation that has flocculated and sedimented in the flocculation tank can be easily extracted from the lowest part of the flocculation tank.

本発明に係る携帯型排水処理評価用前処理装置において、凝集槽の側壁部や底部等は、所定の強度等を要するものであればその材質や厚み等は特に制限されず、透明または半透明な樹脂板等により構成されることが好ましく、透明または半透明な樹脂板等により構成されることにより、内部の観察が容易になるとともに軽量化を容易に図ることができる。 In the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention, the side walls, bottom, etc. of the flocculation tank are not particularly limited in terms of material, thickness, etc., as long as they require a predetermined strength, etc., and are transparent or translucent. By using a transparent or translucent resin plate or the like, it is possible to easily observe the inside and to easily reduce the weight.

本発明に係る携帯型排水処理評価用前処理装置は、攪拌羽根を有しており、係る攪拌羽根は、通常、(図1や図2に例示するように)支持棒に支持された状態で凝集槽内に配置される。
本発明に係る携帯型排水処理評価用前処理装置は、上記攪拌羽根を回転させることにより、凝集槽内において処理対象となる排水と凝集剤(例えば、硫酸アルミニウム等の無機系の凝集剤や高分子凝集剤から選ばれる一種以上)とを好適に混合することができる。
The portable pretreatment device for wastewater treatment evaluation according to the present invention has a stirring blade, and the stirring blade is usually supported by a support rod (as illustrated in FIGS. 1 and 2). Placed in a flocculation tank.
The portable pretreatment device for wastewater treatment evaluation according to the present invention rotates the stirring blades so that wastewater to be treated and a flocculant (for example, an inorganic flocculant such as aluminum sulfate or a high one or more selected from molecular flocculants) can be suitably mixed.

本発明に係る携帯型排水処理評価用前処理装置において、上記攪拌羽根には、外縁部の少なくとも一部に柔軟性樹脂からなる拡幅部が設けられている。 In the portable pretreatment device for wastewater treatment evaluation according to the present invention, the stirring blade is provided with a widened portion made of a flexible resin on at least a part of the outer edge portion.

本発明に係る携帯型排水処理評価用前処理装置において、上記撹拌羽根12の形状は特に制限されず、図3(a)および図3(b)に示すように、プロペラ状のもの(撹拌プロペラ)であってもよいし、図4に示すように、板状のものであってもよい。
本発明に係る携帯型排水処理評価用前処理装置において、上記撹拌羽根12の形状が板状である場合、撹拌羽根が配置される沈殿槽3の凝集槽の内部形状に対応した形状を有することが好ましく、例えば図1や図2に例示するように凝集槽11の底部が先細りする逆円錐形状である場合には、(その垂直断面形状が三角形であるために)板状の撹拌羽根は、図4に示すように三角形状のものが好ましい。
In the portable wastewater treatment evaluation pretreatment device according to the present invention, the shape of the stirring blade 12 is not particularly limited, and as shown in FIGS. ), or as shown in FIG. 4, it may be plate-shaped.
In the portable pretreatment device for wastewater treatment evaluation according to the present invention, when the shape of the stirring blade 12 is plate-like, it has a shape corresponding to the internal shape of the coagulation tank of the sedimentation tank 3 in which the stirring blade is arranged. is preferable, for example, when the bottom of the aggregation tank 11 is tapered and has an inverted conical shape as illustrated in FIGS. A triangular shape as shown in FIG. 4 is preferred.

本発明に係る携帯型排水処理評価用前処理装置において、凝集槽内に配置される撹拌羽根は、外縁部の少なくとも一部に柔軟性樹脂からなる拡幅部が設けられ、当該拡幅部が撹拌羽根の回転時に凝集槽の内壁に接触し得るように配置されている。 In the portable pretreatment device for wastewater treatment evaluation according to the present invention, the stirring blade placed in the flocculation tank has a widened portion made of a flexible resin on at least a part of the outer edge portion, and the widened portion is the stirring blade It is arranged so that it can come into contact with the inner wall of the flocculation tank when it rotates.

本発明に係る携帯型排水処理評価用前処理装置において、撹拌羽根の外縁部に設けられる拡幅部の形態は、当該拡幅部が撹拌羽根の回転時に沈殿槽の内壁に接触し得るものであれば特に制限されず、拡幅部の固定方法も、チューブ状の柔軟性樹脂を羽根に差し込み固定する方法であってもよいし、柔軟性樹脂を羽根に貼り付け固定する方法であってもよいし、撹拌羽根の製造時に一体成形してなるものであってもよい。
例えば、図3(a)に例示するように、プロペラ状の羽根の先端部に柔軟性樹脂からなるチューブ状の樹脂を差し込み固定することにより、撹拌羽根12の外縁部を拡幅した拡幅部Rであってもよいし、さらに、図3(b)に示すように、プロペラ状の羽根の先端部に、先端部を適宜切り出し加工した柔軟性樹脂からなるチューブ状の樹脂を差し込み固定することにより、撹拌羽根12の外縁部を拡幅した拡幅部Rであってもよい。
また、例えば、図4に例示するように、板状の攪拌羽根12の側部(配置時に凝集槽の側壁に対向する傾斜部)の先端に、柔軟性樹脂を切り出した短冊状物を貼り付け固定することにより、撹拌羽根の外縁部を拡幅した拡幅部Rであってもよい。
In the portable pretreatment device for wastewater treatment evaluation according to the present invention, the shape of the widened portion provided at the outer edge of the stirring blade is such that the widened portion can contact the inner wall of the sedimentation tank when the stirring blade rotates. It is not particularly limited, and the method of fixing the widened portion may be a method of inserting a tubular flexible resin into the blade and fixing it, or a method of attaching and fixing the flexible resin to the blade. It may be integrally formed when the stirring blade is manufactured.
For example, as illustrated in FIG. 3A, by inserting and fixing a tube-shaped resin made of a flexible resin into the tip of the propeller-shaped blade, the outer edge of the stirring blade 12 is widened at the widened portion R Further, as shown in FIG. 3(b), by inserting and fixing a tube-shaped resin made of a flexible resin whose tip is appropriately cut out into the tip of the propeller blade, It may be a widened portion R obtained by widening the outer edge of the stirring blade 12 .
Alternatively, for example, as shown in FIG. 4, a strip of flexible resin cut out is pasted on the tip of the side portion of the plate-shaped stirring blade 12 (the inclined portion facing the side wall of the aggregation tank when arranged). It may be a widened portion R obtained by widening the outer edge of the stirring blade by fixing it.

本発明に係る携帯型排水処理評価用前処理装置において、撹拌羽根の外縁部に設けられる拡幅部とは、撹拌羽根の回転時に沈殿槽の内壁に接触し得る部分を意味する。通常、撹拌羽根は使用時に凝集槽の壁部に接触しないものが選択され配置されており、本発明に係る携帯型排水処理評価用前処理装置においても、撹拌羽根の本体(基体)部分は、凝集槽の内壁に接触することなく回転し、凝集槽内に流入する排水を撹拌するが、撹拌羽根に設けた拡幅部のみが撹拌羽根の回転時に凝集槽の内壁に接触する。
撹拌羽根は、通常、回転軸を中心にして左右対称の形状を有しているが、本発明に係る携帯型排水処理評価用前処理装置において、撹拌羽根の外縁部に拡幅部が設けられることにより、必ずしも上記対称形状を有さなくてもよい。
In the portable pretreatment device for wastewater treatment evaluation according to the present invention, the widened portion provided at the outer edge of the stirring blade means a portion that can come into contact with the inner wall of the sedimentation tank when the stirring blade rotates. Normally, the stirring blades are selected and arranged so as not to contact the walls of the flocculation tank during use. It rotates without contacting the inner wall of the flocculating tank and agitates the waste water flowing into the flocculating tank, but only the widened portion provided on the stirring blade contacts the inner wall of the flocculating tank when the stirring blade rotates.
The stirring blade usually has a symmetrical shape with respect to the axis of rotation. Therefore, it does not necessarily have the symmetrical shape described above.

本発明に係る携帯型排水処理評価用前処理装置において、撹拌羽根の外縁部に設けられる拡幅部を構成する柔軟性樹脂とは、撹拌羽根が回転して沈殿槽の内壁に接触した際に可撓性を有するものを意味し、特に限定されないが、例えば、ポリエチレン、エチレンプロピレンゴム等のポリオレフィン類、ブタジエンゴムやエチレンプロピレンゴム又はアクリルゴムに(メタ)アクリル系ポリマー鎖等がグラフトされたグラフトゴム、ウレタン系ゴム、熱可塑性ポリウレタン、アクリル系ゴム、アクリル系熱可塑性ポリマー、シロキサン系熱可塑性ポリマー、シリコン樹脂等から選ばれる一種以上が挙げられる。 In the portable pretreatment device for wastewater treatment evaluation according to the present invention, the flexible resin constituting the widened portion provided on the outer edge of the stirring blade is flexible when the stirring blade rotates and comes into contact with the inner wall of the sedimentation tank. It means a material having flexibility, and is not particularly limited. Examples include polyolefins such as polyethylene and ethylene propylene rubber, butadiene rubber, ethylene propylene rubber, or graft rubber obtained by grafting (meth)acrylic polymer chains onto acrylic rubber. , urethane-based rubber, thermoplastic polyurethane, acrylic rubber, acrylic-based thermoplastic polymer, siloxane-based thermoplastic polymer, silicone resin, and the like.

図1および図2に例示するように、攪拌羽根12は、支持棒13に固定された状態で凝集槽11内に配置されるとともに、支持棒13には、撹拌装置(回転装置)16が配置され、支持棒13を介して所望の回転速度で撹拌羽根12を回転させて、凝集槽11内を撹拌することができる。 As illustrated in FIGS. 1 and 2, the stirring blades 12 are arranged in the aggregation tank 11 while being fixed to the support rods 13, and the support rods 13 are provided with a stirring device (rotating device) 16. Then, the inside of the aggregation tank 11 can be stirred by rotating the stirring blade 12 at a desired rotation speed via the support rod 13 .

本発明に係る携帯型排水処理評価用前処理装置は、上記攪拌羽根を凝集槽の上下方向(凝集槽の高さ方向)に位置調整可能な上下位置移動手段を有している。 The portable pretreatment apparatus for wastewater treatment evaluation according to the present invention has vertical position moving means capable of adjusting the position of the stirring blade in the vertical direction of the coagulation tank (the height direction of the coagulation tank).

本発明に係る携帯型排水処理評価用前処理装置において、上記攪拌羽根の上下位置移動手段の構造および形状は、特に制限されない。 In the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention, the structure and shape of the means for moving the stirring blade up and down are not particularly limited.

図5は、図1および図2に例示する携帯型排水処理評価用前処理装置の形態例における上下位置移動手段14において、攪拌羽根12の上下位置移動方法(上下位置の変更方法)を説明するための図である。
図5に示す上下位置移動手段14は、凝集槽11の頂部を横切るように設けられたコの字状の板材からなる架橋部材M1を有し、係る架橋部材M1は、凝集槽11に隣接する側部において、ネジC、Cにより凝集槽の側壁に固定されている。また、図5に示す上下位置移動手段14は、架橋部材M1上に立設された一対のボルトM3、M3と、架橋部材M1上部を横切るように設けられ、支持棒13および一対のボルトM1、M1を貫通させた状態で支持棒13に固定された板状の位置決め部材M2とを有している。
上記位置決め部材M2は、支持棒13が回転自在に回転し得るようにこれを挿通するとともに、ボルトM3、M3に対してナットn、nにより上下位置を任意に決定し得るように固定されている。
FIG. 5 illustrates a vertical position moving method (vertical position changing method) of the stirring blade 12 in the vertical position moving means 14 in the exemplary form of the portable pretreatment apparatus for evaluation of wastewater treatment illustrated in FIGS. It is a diagram for
Vertical position moving means 14 shown in FIG. At the side, it is fixed to the side wall of the flocculation tank by means of screws C, C. The vertical position moving means 14 shown in FIG. 5 is provided so as to cross a pair of bolts M3, M3 erected on the bridging member M1, and the upper part of the bridging member M1. It has a plate-shaped positioning member M2 fixed to the support rod 13 in a state in which M1 is passed therethrough.
The positioning member M2 is inserted through the support rod 13 so as to be rotatable, and is fixed to the bolts M3, M3 by nuts n, n so that the vertical position can be determined arbitrarily. .

図5に例示する携帯型排水処理評価用前処理装置10においては、図5の左図に示す状態で一対のボルトM3、M3に各々設けたナットn、nを緩めた上で、図5の右図に示すように支持棒13を引き上げ、次いで一対のボルトM3、M3に各々設けたナットn、nを締めることにより、攪拌羽根12を凝集槽11の上部方向に位置調整する(上部方向に位置変更する)ことができる。
また、上記とは逆に、図5に例示する携帯型排水処理評価用前処理装置10において、図5の右図に示す状態で一対のボルトM3、M3に各々設けたナットn、nを緩めた上で、図5の左図に示すように支持棒13を引き下げ、次いで一対のボルトM3、M3に各々設けたナットn、nを締めることにより、攪拌羽根12を凝集槽11の下部方向に位置調整する(下部方向に位置変更する)ことができる。
In the portable wastewater treatment evaluation pretreatment device 10 illustrated in FIG. As shown in the right figure, the support rod 13 is pulled up, and then the nuts n, n provided on the pair of bolts M3, M3 are tightened to adjust the position of the stirring blade 12 in the upper direction of the aggregation tank 11 (upward direction). can be repositioned).
On the contrary to the above, in the portable wastewater treatment evaluation pretreatment device 10 illustrated in FIG. 5, the support rod 13 is pulled down, and then the nuts n, n provided on the pair of bolts M3, M3 are tightened, thereby moving the stirring blade 12 toward the bottom of the flocculation tank 11. It can be repositioned (repositioned downward).

図6は、図5に例示した携帯型排水処理評価用前処理装置の形態例とは別の形態例における上下位置移動手段14において、攪拌羽根12の上下移動方法を説明するための図である。 FIG. 6 is a diagram for explaining a vertical movement method of the stirring blade 12 in the vertical position moving means 14 in a form example different from the form example of the portable wastewater treatment evaluation pretreatment apparatus illustrated in FIG. .

図6に示す上下位置移動手段14は、凝集槽11の頂部を横切るように設けられたコの字状の板材からなる架橋部材M1を有する点において、図5に示す上下位置移動手段14と共通し、図6に示す架橋部材M1は、凝集槽11に隣接する側部において、ネジC、Cで凝集槽11の側壁に固定されている点で図5に示す架橋部材M1と共通している。 The vertical position moving means 14 shown in FIG. 6 is common to the vertical position moving means 14 shown in FIG. The bridging member M1 shown in FIG. 6 is common to the bridging member M1 shown in FIG. .

一方、図6に示す上下位置移動手段14は、位置決め部材M2および一対のボルトM3、M3を有さない。また、図6に示す架橋部材M1は、支持棒13が回転自在に回転し得るようにこれを挿通するとともに、図5に示す架橋部材M1に比較して、凝集槽11に隣接する側部の長さが凝集槽の上下方向(凝集槽の高さ方向)に沿って長く設けられており、ネジC,Cを固定するネジ穴も、凝集槽の上下方向(凝集槽の高さ方向)に複数設けられている。 On the other hand, the vertical position moving means 14 shown in FIG. 6 does not have the positioning member M2 and the pair of bolts M3, M3. In addition, the bridging member M1 shown in FIG. 6 is inserted through the support rod 13 so as to be rotatable, and compared to the bridging member M1 shown in FIG. The length is long along the vertical direction of the coagulation tank (height direction of the coagulation tank), and the screw holes for fixing the screws C and C are also oriented in the vertical direction of the coagulation tank (height direction of the coagulation tank). Multiple are provided.

図6に例示する携帯型排水処理評価用前処理装置10においては、図6の左図に示す状態で一対のネジC、Cを緩めた上で、図6の右図に示すように支持棒13とともに架橋部材M1を引き上げ、次いで一対のネジC、Cを締めることにより、攪拌羽根12を凝集槽11の上部方向に位置調整する(上部方向に位置変更する)ことができる。
また、上記とは逆に、図6に例示する携帯型排水処理評価用前処理装置10において、図6の右図に示す状態で一対のネジC,Cを緩めた上で、図6の左図に示すように支持棒13とともに架橋部材M1を引き下げ、次いで一対のネジC、Cを締めることにより、攪拌羽根12を凝集槽11の下部方向に位置調整する(下部方向に位置変更する)ことができる。
In the portable wastewater treatment evaluation pretreatment device 10 illustrated in FIG. By pulling up the bridging member M1 together with 13 and then tightening the pair of screws C, C, the position of the stirring blade 12 can be adjusted in the upward direction of the aggregation tank 11 (changed in the upward direction).
On the contrary to the above, in the portable wastewater treatment evaluation pretreatment device 10 illustrated in FIG. As shown in the figure, the bridging member M1 is pulled down together with the support rod 13, and then the pair of screws C, C are tightened to adjust the position of the stirring blade 12 in the lower direction of the aggregation tank 11 (change the position in the lower direction). can be done.

上述したように、凝集槽を携帯可能な程度に小型化した場合、上記凝集槽の側壁に浮遊性の付着物が層状に形成され、この付着物の生成により槽内での凝集処理が適切に行い難くなるが、本発明に係る携帯型排水処理評価用前処理装置においては、凝集槽内に設けられた攪拌羽根が外縁部の少なくとも一部に柔軟性樹脂からなる拡幅部を有し、係る拡幅部が撹拌羽根の回転時に凝集槽の内壁に接触し得るように配置されるとともに、上記攪拌羽根が上下位置移動手段により凝集槽の上下方向に移動可能に配置されていることにより、槽壁に生成した付着物を除去しつつ好適に凝集処理を行うことが可能となる。
また、本発明によれば、攪拌羽根を凝集槽の上下方向に位置調整可能な上下位置移動手段を有することにより、凝集槽内で使用する凝集剤の量および種類や、処理対象となる排水の量または種類に応じて、攪拌羽根の上下位置(凝集槽の高さ方向における位置)を変更して、最適な攪拌処理を行うことができる。
As described above, when the flocculation tank is made small enough to be portable, floating deposits are formed in layers on the sidewalls of the flocculation tank. Although it is difficult to perform, in the portable pretreatment device for evaluating wastewater treatment according to the present invention, the stirring blade provided in the flocculation tank has a widened portion made of a flexible resin on at least a part of the outer edge portion. The widened portion is arranged so as to come into contact with the inner wall of the coagulation tank when the stirring blade rotates, and the stirring blade is arranged so as to be movable in the vertical direction of the coagulation tank by the vertical position moving means, so that the tank wall It is possible to suitably carry out the aggregating process while removing the deposits generated in the process.
In addition, according to the present invention, by having a vertical position moving means that can adjust the position of the stirring blade in the vertical direction of the coagulation tank, the amount and type of coagulant used in the coagulation tank, and the wastewater to be treated. Depending on the amount or type, the vertical position of the stirring blade (the position in the height direction of the aggregation tank) can be changed to perform the optimum stirring process.

本発明に係る携帯型排水処理評価用前処理装置は、上記凝集槽と連通し当該凝集槽で処理された凝集物処理水を貯留する貯留室および上記貯留室内に引き込まれ取水口が凝集物処理水の水面近傍に位置するように上下移動可能に配置された排出管をさらに有するものであってもよい。 A portable pretreatment device for evaluating wastewater treatment according to the present invention includes a storage chamber that communicates with the flocculation tank and stores flocculated water treated in the flocculation tank, and a water intake that is drawn into the storage chamber and has a flocculation treatment. It may further have a discharge pipe arranged so as to be vertically movable so as to be positioned near the surface of the water.

図7は、本発明に係る携帯型排水処理評価用前処理装置において、上記貯留室および排出管を有する形態例について説明するための概略図(斜視図)である。
図7に示す例において、携帯型排水処理評価用前処理装置10は、凝集槽11とともに、当該凝集槽11と連通し当該凝集槽11で処理された凝集物処理水を貯留する貯留室15をさらに有している。
FIG. 7 is a schematic view (perspective view) for explaining an example of the form of the portable pretreatment apparatus for evaluating wastewater treatment according to the present invention, which has the storage chamber and the discharge pipe.
In the example shown in FIG. 7, the portable wastewater treatment evaluation pretreatment apparatus 10 includes a flocculation tank 11 and a storage chamber 15 that communicates with the flocculation tank 11 and stores flocculated water treated in the flocculation tank 11. have more.

本発明に係る携帯型排水処理評価用前処理装置において、貯留室15の形態は特に制限されないが、通常その形態は概略箱形状である。
本発明に係る携帯型排水処理評価用前処理装置において、貯留室は、その内容量が、
0.5~10Lであるものであるものが好ましく、1.0~8Lであるものがより好ましく、2~5Lであるものがさらに好ましく、1~5Lであるものが一層好ましい。
貯留室の形状が箱型である場合、その外形のサイズは、縦100~200mm、横100~200mm、高さ150~250mm程度であることが好ましい。貯留室のサイズが上記範囲内にあることにより、携帯性を有しつつも、実機(実際の排水処理プラントで使用される凝集槽)と同様の条件下における凝集処理を省スペースで簡便に行うことができる。
本発明に係る携帯型排水処理評価用前処理装置において、貯留室の側壁、天井板、床板
等も、所定の強度等を要するものであればその材質や厚み等は特に制限されず、透明または半透明な樹脂板等により構成されることが好ましく、透明または半透明な樹脂板等により構成されることにより、内部の観察が容易になるとともに軽量化を容易に図ることができる。
In the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention, the shape of the storage chamber 15 is not particularly limited, but the shape is generally box-shaped.
In the portable pretreatment device for wastewater treatment evaluation according to the present invention, the storage chamber has an internal capacity of
0.5 to 10 L is preferred, 1.0 to 8 L is more preferred, 2 to 5 L is even more preferred, and 1 to 5 L is even more preferred.
When the shape of the storage chamber is box-shaped, it is preferable that the size of the outer shape is about 100 to 200 mm in length, 100 to 200 mm in width, and 150 to 250 mm in height. Because the size of the storage chamber is within the above range, while maintaining portability, coagulation treatment can be easily performed in a space-saving manner under the same conditions as the actual machine (coagulation tank used in an actual wastewater treatment plant). be able to.
In the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention, the side wall, ceiling plate, floor plate, etc. of the storage chamber are not particularly limited in terms of material, thickness, etc., as long as they require a predetermined strength. It is preferable to use a semi-transparent resin plate or the like. By using a transparent or semi-transparent resin plate or the like, the inside can be easily observed and the weight can be easily reduced.

図7に示す例において、凝集槽11および貯留室15間には、凝集物処理水(凝集槽で処理した処理水)が相互に流通可能な状態になるように貫通孔Pが設けられている。 In the example shown in FIG. 7, a through hole P is provided between the flocculation tank 11 and the storage chamber 15 so that the flocculation treated water (treated water treated in the flocculation tank) can flow mutually. .

また、図7に示す例においては、貯留室15に貯留した凝集物処理水を排出する排出管Tを有し、当該排出管Tの取水口が貯留室内に引き込まれるとともに貯留した凝集物処理水の水面近傍に位置するように上下移動可能に配置されている。
上記排出管Tの取水口を凝集物処理水の水面近傍に位置するように上下移動する手段は特に制限されず、例えば、図7に示すように、排出管Tが、外管内に内管が同軸二重円筒状に収容された構造を有するとともに、(図示しない)調整つまみによって排出管Tの取水口の位置を上下させて凝集物処理水の水面WS近傍に位置し得るように設計されているものを挙げることができる。
Further, in the example shown in FIG. 7, there is a discharge pipe T for discharging the aggregate-treated water stored in the storage chamber 15, and the water intake of the discharge pipe T is drawn into the storage chamber and the stored aggregate-treated water It is arranged so that it can move up and down so that it is positioned near the surface of the water.
The means for vertically moving the water intake of the discharge pipe T so as to be positioned near the surface of the flocculate-treated water is not particularly limited. For example, as shown in FIG. It has a structure housed in a coaxial double cylinder shape, and is designed so that the position of the water intake of the discharge pipe T can be moved up and down by an adjustment knob (not shown) so that it can be positioned near the water surface WS of the flocculate-treated water. I can list what I have.

図7に例示するように、本発明に係る携帯型排水処理評価用前処理装置が、凝集槽11とともに貯留室15を有し、かかる貯留室15が凝集槽11で処理された凝集物処理水を排出するための排出管Tを内部に有し、当該排出管Tの取水口が凝集物処理水の水面WS近傍に位置するように上下移動可能に配置されていることにより、凝集槽11で槽壁から掻き取られた付着物や凝集槽内で(凝集剤の添加により)生成した凝集物の流出を容易に抑制することができる。
このように付着物や凝集物の含有割合が低い上澄液のみを凝集物処理水として流出口Doutから排出することにより、後続する装置(例えば、携帯型の活性汚泥処理槽)の負荷を容易に低減することができる。
また、図7に例示するように、本発明に係る携帯型排水処理評価用前処理装置が、凝集槽11とともに貯留室15を有し、かかる貯留室15が凝集槽11で処理された凝集物処理水を排出するための排出管Tを内部に有し、当該排出管Tの取水口が凝集物処理水の水面WS近傍に位置するように上下移動可能に配置されていることにより、評価対象となる実機(実際の排水処理プラントで使用される凝集槽)に応じて凝集槽の処理容量を容易に調整することができる。
As exemplified in FIG. 7, the portable pretreatment device for wastewater treatment evaluation according to the present invention has a storage chamber 15 together with a coagulation tank 11, and the storage chamber 15 is a flocculate-treated water treated in the flocculation tank 11. and is vertically movable so that the intake port of the discharge pipe T is located near the water surface WS of the flocculation treated water. It is possible to easily suppress the outflow of deposits scraped from the tank wall and the aggregates generated in the coagulation tank (by adding the coagulant).
By discharging only the supernatant liquid with a low content of deposits and aggregates as aggregate treated water from the outlet Dout in this way, the load of subsequent equipment (for example, a portable activated sludge treatment tank) can be easily reduced. can be reduced to
Further, as illustrated in FIG. 7, the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention has a storage chamber 15 together with a flocculation tank 11, and the storage chamber 15 is a flocculated material treated in the flocculation tank 11. A discharge pipe T for discharging the treated water is provided inside, and the intake port of the discharge pipe T is arranged so that it can move up and down so that it is located near the water surface WS of the flocculate treated water. It is possible to easily adjust the treatment capacity of the coagulation tank according to the actual equipment (coagulation tank used in the actual wastewater treatment plant).

図8は、本発明に係る携帯型排水処理評価用前処理装置を用いた排水処理評価の実施形態例を説明するための図である。
図8は、本発明の一実施形態に係る携帯型排水処理評価用前処理装置10と、携帯型活性汚泥処理槽20とを組み合わせた携帯用排水処理評価装置を示している。
FIG. 8 is a diagram for explaining an embodiment of wastewater treatment evaluation using a portable pretreatment device for wastewater treatment evaluation according to the present invention.
FIG. 8 shows a portable wastewater treatment evaluation apparatus in which a portable wastewater treatment evaluation pretreatment apparatus 10 according to one embodiment of the present invention and a portable activated sludge treatment tank 20 are combined.

携帯型活性汚泥処理槽20としては、携帯型活性汚泥処理槽20の底部から上部方向に酸素含有気体を流入させる流入ノズルNを有するものが好ましく、流入ノズルNから活性汚泥処理槽内に流入する酸素含有気体としては、酸素または空気を挙げることができる。 The portable activated sludge treatment tank 20 preferably has an inflow nozzle N for inflowing the oxygen-containing gas upward from the bottom of the portable activated sludge treatment tank 20, and the gas flows into the activated sludge treatment tank from the inflow nozzle N. Oxygen-containing gas can include oxygen or air.

図8に例示するように、携帯型活性汚泥処理槽20は、活性汚泥処理された活性汚泥処理水を排出する排出管tを有しており、係る排出管tは、上述した貯留室内に配置される排出管Tと同様に、その取水口が携帯型活性汚泥処理槽20内に引き込まれるとともに活性汚泥処理水の水面近傍に位置するように上下移動可能に配置されているものが好ましい。 As illustrated in FIG. 8, the portable activated sludge treatment tank 20 has a discharge pipe t for discharging the activated sludge treated water, and the discharge pipe t is arranged in the storage chamber described above. As with the discharge pipe T, it is preferable that the intake port is drawn into the portable activated sludge treatment tank 20 and is arranged so as to be vertically movable so as to be positioned near the water surface of the activated sludge treated water.

図8に示す例において、排出管tとしては、上記排出管Tと同様のものを挙げることができる。 In the example shown in FIG. 8, the discharge pipe t may be the same as the discharge pipe T described above.

図8に例示するように、本発明に係る携帯型排水処理評価用前処理装置が、携帯型活性汚泥処理槽20で処理された活性汚泥処理水を排出するための排出管tを有し、当該排出管tの取水口が活性汚泥処理水の水面近傍に位置するように上下移動可能に配置されていることにより、携帯型活性汚泥処理槽20により活性汚泥処理された、活性汚泥の含有割が低い上澄液のみを活性汚泥処理水として排出することができる。 As illustrated in FIG. 8, the portable wastewater treatment evaluation pretreatment device according to the present invention has a discharge pipe t for discharging the activated sludge treated water treated in the portable activated sludge treatment tank 20, The content of activated sludge treated by the portable activated sludge treatment tank 20 by arranging the water intake of the discharge pipe t so as to be able to move up and down so that it is positioned near the water surface of the activated sludge treated water Only the supernatant liquid with a low C can be discharged as the activated sludge treated water.

本発明に係る携帯型排水処理評価用前処理装置は、小型の凝集槽を必須とし、さらに小型の活性汚泥処理槽等や、必要に応じて撹拌装置やポンプ、ホース等の導管等の任意の付属品を組み合わせた携帯型排水処理評価処理装置として使用することにより、装置全体の小型化、軽量化を図りつつ、容易に組み立て、分解できるものであるので、例えば旅行用のスーツケース内に収容する等して容易に運搬し、使用することができる。 The portable pretreatment device for wastewater treatment evaluation according to the present invention requires a small flocculation tank, a small activated sludge treatment tank, etc., and optionally a stirring device, a pump, a conduit such as a hose, etc. By using it as a portable wastewater treatment evaluation treatment device combined with accessories, it is possible to reduce the size and weight of the entire device while assembling and disassembling it easily. can be easily transported and used.

本発明に係る携帯型排水処理評価用前処理装置を使用する場合、実機(実際の排水処理プラントで使用される凝集槽)と同様の排水を採用し、実機に対応する条件下で排水処理が行われる。
本発明に係る携帯型排水処理評価用前処理装置において、凝集槽に対する排水の供給量は、5~50mL/分間であることが好ましく、上記凝集槽とともに携帯型の活性汚泥処理槽を用いる場合は、携帯型の活性汚泥処理槽に対する排水の供給量は、5~30mL/分間であることが好ましい。
When using the portable wastewater treatment evaluation pretreatment device according to the present invention, the same wastewater as the actual equipment (coagulation tank used in the actual wastewater treatment plant) is adopted, and wastewater treatment is performed under the conditions corresponding to the actual equipment. done.
In the portable wastewater treatment evaluation pretreatment device according to the present invention, the amount of wastewater supplied to the flocculation tank is preferably 5 to 50 mL / minute, and when a portable activated sludge treatment tank is used together with the flocculation tank The amount of waste water supplied to the portable activated sludge treatment tank is preferably 5 to 30 mL/minute.

上記小型の活性汚泥処理槽から得られる処理水は、公知の方法により、例えば、生物化学的酸素要求量(Biochemical oxygen demand:BOD)、化学的酸素要求量(Chemical Oxygen Demand:COD)、全有機炭素(Total Organic Carbon:TOC)、全窒素濃度、全リン濃度、懸濁物濃度等が測定され、各種規制値を満たし得るか否かが評価される。 The treated water obtained from the small-sized activated sludge treatment tank is measured by a known method, for example, biochemical oxygen demand (BOD), chemical oxygen demand (Chemical Oxygen Demand: COD), total organic Carbon (Total Organic Carbon: TOC), total nitrogen concentration, total phosphorus concentration, suspension concentration, etc. are measured, and it is evaluated whether various regulation values can be satisfied.

上記評価の結果、評価対象となる排水処理プラントが設置された地域における規制値を満たさない項目が検出された場合は、さらに排水処理条件を変更した上で、本発明に係る携帯型排水処理評価用前処理装置を用いた排水処理を行い、再度各種検査項目について評価を行って、全ての規制値を満たすまで繰り返し排水処理を行えばよい。 As a result of the above evaluation, if an item that does not satisfy the regulation value in the area where the wastewater treatment plant to be evaluated is installed is detected, the wastewater treatment conditions are further changed, and the portable wastewater treatment evaluation according to the present invention Wastewater treatment may be performed using a pretreatment device, and then the various inspection items may be evaluated again, and the wastewater treatment may be repeatedly performed until all regulatory values are satisfied.

本発明によれば、槽壁への付着物層の形成を抑制しつつ簡便かつ迅速に排水処理条件を評価するための携帯型排水処理評価前処理装置を提供することができる。 According to the present invention, it is possible to provide a portable wastewater treatment pre-evaluation apparatus for simply and quickly evaluating wastewater treatment conditions while suppressing the formation of deposit layers on tank walls.

次に、本発明に係る排水処理評価方法について説明する。
本発明に係る排水処理評価方法は、本発明に係る携帯型排水処理評価用前処理装置を用いて排水処理することを特徴とするものである。
本発明に係る携帯型排水処理評価用前処理装置を用いて処理水を得るための排水処理の詳細は、上述したとおりである。
本発明に係る携帯型排水処理評価用前処理装置は、上述したように、適宜携帯型の活性汚泥処理槽を併用することができ、得られた処理水は、適宜、一以上の組成評価または物性評価に供される。
得られた処理水の組成評価または物性評価としては、公知の評価項目を挙げることができ、例えば、生物化学的酸素要求量(Biochemical oxygen demand:BOD)、化学的酸素要求量(Chemical Oxygen Demand:COD)、全有機炭素(Total Organic Carbon:TOC)、全窒素濃度、全リン濃度、懸濁物濃度等から選ばれる一種以上を挙げることができる。
これ等の評価項目は、各種評価項目に対応する公知の測定方法により測定すればよい。
Next, the wastewater treatment evaluation method according to the present invention will be described.
A wastewater treatment evaluation method according to the present invention is characterized by treating wastewater using the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention.
The details of wastewater treatment for obtaining treated water using the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention are as described above.
As described above, the portable pretreatment apparatus for evaluating wastewater treatment according to the present invention can be used in combination with a suitable portable activated sludge treatment tank. Provided for physical property evaluation.
As composition evaluation or physical property evaluation of the obtained treated water, known evaluation items can be mentioned, for example, biochemical oxygen demand (Biochemical oxygen demand: BOD), chemical oxygen demand (Chemical Oxygen Demand: COD), Total Organic Carbon (TOC), total nitrogen concentration, total phosphorus concentration, suspension concentration and the like.
These evaluation items may be measured by known measurement methods corresponding to various evaluation items.

上記各種評価項目における評価値(組成値または物性値)が、排水処理プラントの設置地域における規制を満たさない場合には、再度本発明に係る携帯型排水処理評価用前処理装置を用い、排水処理条件を変更した上で排水処理する操作を適宜繰り返すことにより、最適な排水処理条件を決定することができる。 If the evaluation values (composition values or physical property values) in the above various evaluation items do not satisfy the regulations in the area where the wastewater treatment plant is installed, the portable wastewater treatment evaluation pretreatment device according to the present invention is used again to treat the wastewater. By appropriately repeating the operation of wastewater treatment after changing the conditions, the optimum wastewater treatment conditions can be determined.

本発明によれば、本発明に係る携帯型排水処理評価用前処理装置を用いていることから、槽壁への付着物層の形成を抑制しつつ簡便に排水処理条件を評価、決定することができる。 According to the present invention, since the portable pretreatment apparatus for evaluating wastewater treatment according to the present invention is used, it is possible to easily evaluate and determine wastewater treatment conditions while suppressing the formation of deposit layers on the tank walls. can be done.

以下に実施例を示して本発明をさらに具体的に説明するが、本発明はこれに制限されるものではない。 EXAMPLES The present invention will be described in more detail with reference to examples below, but the present invention is not limited thereto.

(実施例1)
図7に示す装置構成を有する携帯型排水処理評価用前処理装置10を構成した。
図7に示すように、本実施例で用いた携帯型排水処理評価用前処理装置10において、流入口Dinより排水が流入する凝集槽11(内容量が5L、内径20cm、縦40cmの内部形状が概略円筒形状であるもの)の槽内に、支持棒13により支持された攪拌羽根12と、攪拌羽根12を凝集槽11の上下方向に位置調整可能な上下位置移動手段14とを配置した。
また、本実施例で用いた携帯型排水処理評価用前処理装置10において、凝集槽11と連通し凝集槽11で処理された凝集物処理水を貯留する貯留室15(内容量が2Lで、内部形状が、縦15cm、横15cm、高さ25cmの外略箱形状のもの)と、取水口が上記貯留室15内に引き込まれるとともに貯留した凝集物処理水の水面W13近傍に位置するように上下移動可能に配置される上記貯留室15に貯留した凝集物処理水を排出する排出管T(内径15mm)とを配置した。
上記凝集槽11および貯留室15は、厚さ4~6mmの透明な樹脂板により構成され、外部から容易に視認し得る状態になっている。
上記凝集槽11内に配置される攪拌羽根(攪拌プロペラ)12(各翼の長さ約6 cm)は、図3(b)に示す形態を有し、同図に示すように、プロペラ状の複数枚の翼のうち、1枚の翼の先端部には先端部を切り出し加工した、内径10mmのチューブ状のシリコン樹脂を差し込み固定することにより(上記チューブ状のシリコン樹脂を差し込んだ後の翼の長さ約24cm)、撹拌羽根12の外縁部を拡幅した拡幅部Rが形成され、当該拡幅部Rが攪拌プロペラ12の回転時に凝集槽11の内壁に接触し得るように配置した。
上記携帯型排水処理評価用装置10において、石油精製設備から排出される排水を、流入口Dinより凝集槽11に速度20ml/分間で流入させるとともに、凝集槽11内において攪拌プロペラ12を1~10rpmで回転させながら、凝集剤として硫酸アルミニウムを加えて当該凝集物を凝集、沈殿させた。係る凝集処理によって得られた凝集物処理水を貫通孔Pを介して貯留室15に流入させるとともに、貯留室15に貯留した凝集物処理水を排出管Tの流出口Doutより速度15ml/分間で流出させた。
(Example 1)
A portable pretreatment apparatus 10 for wastewater treatment evaluation having the apparatus configuration shown in FIG. 7 was constructed.
As shown in FIG. 7, in the portable wastewater treatment evaluation pretreatment device 10 used in the present example, the coagulation tank 11 (with an internal capacity of 5 L, an inner diameter of 20 cm, and a length of 40 cm) into which the wastewater flows from the inlet Din is approximately cylindrical), a stirring blade 12 supported by a support rod 13, and a vertical position moving means 14 capable of adjusting the position of the stirring blade 12 in the vertical direction of the aggregation tank 11 were arranged.
In addition, in the portable wastewater treatment evaluation pretreatment apparatus 10 used in the present example, the storage chamber 15 (with an internal capacity of 2 L, The internal shape is 15 cm long, 15 cm wide, and 25 cm high), and the water intake is drawn into the storage chamber 15 and positioned near the water surface W13 of the stored aggregate-treated water. A discharge pipe T (with an inner diameter of 15 mm) for discharging the aggregate-treated water stored in the storage chamber 15, which is arranged so as to be vertically movable, is arranged.
The coagulation tank 11 and the storage chamber 15 are made of a transparent resin plate having a thickness of 4 to 6 mm and are easily visible from the outside.
The stirring blade (stirring propeller) 12 (each blade length is about 6 cm) arranged in the aggregation tank 11 has a form shown in FIG. By inserting a tube-shaped silicon resin with an inner diameter of 10 mm and fixing the tip of one blade out of the plurality of blades (the blade after inserting the above-mentioned tube-shaped silicone resin) length of about 24 cm), and a widened portion R is formed by widening the outer edge of the stirring blade 12, and the widened portion R is arranged so that it can contact the inner wall of the aggregation tank 11 when the stirring propeller 12 rotates.
In the portable wastewater treatment evaluation apparatus 10, the wastewater discharged from the oil refining facility is flowed into the flocculation tank 11 from the inlet Din at a speed of 20 ml/min, and the stirring propeller 12 is rotated at 1 to 10 rpm in the flocculation tank 11. While rotating at , aluminum sulfate was added as a flocculating agent to flocculate and precipitate the flocculate. The aggregate-treated water obtained by the aggregation treatment is made to flow into the storage chamber 15 through the through hole P, and the aggregate-treated water stored in the storage chamber 15 is discharged from the outlet Dout of the discharge pipe T at a rate of 15 ml/minute. drained.

このとき、(1)流入口Dinより流入する排水、(2)凝集槽11の水面近傍における排水、(3)貯留室15の水面近傍における排水、(4)流出口Dinより流出する排水を各々採取し、下記方法により吸光度(660nm)および浮遊粒子状物質量(mg/L)を測定した。結果を表1に示す。 At this time, (1) wastewater flowing in from the inlet Din, (2) wastewater near the water surface of the flocculation tank 11, (3) wastewater near the water surface of the storage chamber 15, and (4) wastewater flowing out from the outflow port Din, respectively. It was collected, and the absorbance (660 nm) and suspended particulate matter amount (mg/L) were measured by the following method. Table 1 shows the results.

<吸光度の測定方法>
各サンプルを測定用のセルに採取し、測定波長660nmにおける吸光度を測定した。
<Method for measuring absorbance>
Each sample was collected in a cell for measurement, and the absorbance at a measurement wavelength of 660 nm was measured.

<浮遊粒子状物質量の測定方法>
JIS K 0102工業排水試験方法に基づいて、各サンプルをそれぞれろ紙に捕集し、乾燥後の重量を秤量して、各サンプル1Lあたりの浮遊粒子状物質濃度(mg/L)を求めた。
<Method for measuring the amount of suspended particulate matter>
Based on the JIS K 0102 industrial wastewater test method, each sample was collected on filter paper, and the weight after drying was weighed to determine the suspended particulate matter concentration (mg/L) per liter of each sample.

Figure 0007333246000001
Figure 0007333246000001

表1より、本発明に係る携帯型排水処理評価用前処理装置により、(1)流入口Dinより流入する排水に対して凝集槽11で凝集処理を施すことにより、(2)凝集槽11の水面近傍における排水、(3)貯留室15の水面近傍における排水および(4)流出口Dinより流出する排水の吸光度および浮遊粒子状物質量が低下していること、特に貯留室15に設けた(4)流出口Dinより流出する排水の吸光度および浮遊粒子状物質量が低下していることを確認することができた。
このため、本発明に係る携帯型排水処理評価用前処理装置によれば、凝集槽11の槽壁への付着物層の形成を抑制しつつ簡便かつ迅速に凝集処理(前処理)を行って、排水処理条件を評価し得ることが分かる。
From Table 1, by the portable wastewater treatment evaluation pretreatment device according to the present invention, (1) by subjecting the wastewater flowing in from the inlet Din to flocculation treatment in the flocculation tank 11, (2) the flocculation tank 11 (3) drainage near the water surface of the storage chamber 15; 4) It was confirmed that the absorbance and the amount of suspended particulate matter of the wastewater flowing out from the outlet Din were reduced.
For this reason, according to the portable pretreatment apparatus for evaluating wastewater treatment according to the present invention, the flocculation treatment (pretreatment) can be performed simply and quickly while suppressing the formation of a deposit layer on the tank wall of the flocculation tank 11. , the wastewater treatment conditions can be evaluated.

(実施例2)
実施例1で用いた装置構成を有する携帯型排水処理評価用前処理装置10に対し、図8に示すように携帯型活性汚泥処理槽20を組み合わせ、携帯型排水処理評価装置を構成した。
図8に示すように、本実施例で用いた携帯型活性汚泥処理槽20は、内容量が5Lで、縦23cm、横15cm、高さ30cmの箱状の内部形状を有し、携帯型活性汚泥処理槽20で処理された活性汚泥処理水を排出する排出管t(内径20mm)を有している。
上記携帯型活性汚泥処理槽20は、厚さ4~6mmの透明な樹脂板により構成され、外部から容易に視認し得る状態になっている。
上記携帯型排水処理評価用装置10において、石油精製設備から排出される排水を、流入口Dinより凝集槽11に速度20ml/分間で流入させるとともに、凝集槽11内において攪拌プロペラ12を1~10rpmで回転させながら、凝集剤として硫酸アルミニウムを加えて当該凝集物を凝集、沈殿させた。係る凝集処理によって得られた凝集物処理水を貫通孔Pを介して貯留室15に流入させるとともに、貯留室15に貯留した凝集物処理水を排出管Tの流出口Doutより速度15ml/分間で流出させ、次いで、携帯型活性汚泥処理槽20で活性汚泥処理した後、得られた処理水を排出管tから速度15ml/分間で流出させた。
上記処理を5日間連続して行い、このときの(1)流入口Dinより流入する排水および(2)携帯型活性汚泥処理槽の排出管tより流出する排水を1日毎に各々採取した上で、下記方法により(1)流入口Dinより流入する排水1Lあたりのアンモニア態窒素濃度(mg N/L)および(2)携帯型活性汚泥処理槽の排出管tより流出する排水1Lあたりの硝酸態窒素濃度(mg N/L)を各々測定し、硝化率(%)(排水中のアンモニアが硝酸に酸化される割合)を算出した。
結果を表2に示す。
(Example 2)
A portable wastewater treatment evaluation apparatus was constructed by combining a portable activated sludge treatment tank 20 as shown in FIG.
As shown in FIG. 8, the portable activated sludge treatment tank 20 used in this example has an internal volume of 5 L and has a box-like internal shape measuring 23 cm long, 15 cm wide and 30 cm high. It has a discharge pipe t (inner diameter 20 mm) for discharging the activated sludge treated water treated in the sludge treatment tank 20 .
The portable activated sludge treatment tank 20 is composed of a transparent resin plate having a thickness of 4 to 6 mm and is easily visible from the outside.
In the portable wastewater treatment evaluation apparatus 10, the wastewater discharged from the oil refining facility is flowed into the flocculation tank 11 from the inlet Din at a speed of 20 ml/min, and the stirring propeller 12 is rotated at 1 to 10 rpm in the flocculation tank 11. While rotating at , aluminum sulfate was added as a flocculating agent to flocculate and precipitate the flocculate. The aggregate-treated water obtained by the aggregation treatment is made to flow into the storage chamber 15 through the through hole P, and the aggregate-treated water stored in the storage chamber 15 is discharged from the outlet Dout of the discharge pipe T at a rate of 15 ml/minute. Then, after the activated sludge treatment in the portable activated sludge treatment tank 20, the resulting treated water was allowed to flow out from the discharge pipe t at a rate of 15 ml/minute.
The above treatment was carried out continuously for 5 days, and (1) wastewater flowing in from the inlet Din and (2) wastewater flowing out from the discharge pipe t of the portable activated sludge treatment tank were sampled every day. , by the following methods: (1) ammonia nitrogen concentration (mg N / L) per liter of wastewater flowing in from the inlet Din and (2) nitrate nitrogen concentration per liter of wastewater flowing out from the discharge pipe t of the portable activated sludge treatment tank The nitrogen concentration (mg N/L) was measured for each, and the nitrification rate (%) (the rate at which ammonia in the waste water is oxidized to nitric acid) was calculated.
Table 2 shows the results.

<排水中のアンモニア態窒素濃度および硝酸態窒素濃度測定方法>
各々、イオンクロマトグラフで測定した。
<Method for measuring ammonia nitrogen concentration and nitrate nitrogen concentration in wastewater>
Each was measured by ion chromatography.

<硝化率>
{(2)携帯型活性汚泥処理槽の排出管tより流出する排水中の硝酸態窒素濃度/(1)流入口Dinより流入する排水中のアンモニア態窒素濃度}×100
<Nitrification rate>
{(2) Concentration of nitrate nitrogen in the wastewater flowing out from the discharge pipe t of the portable activated sludge treatment tank/(1) Concentration of ammonia nitrogen in the wastewater flowing in from the inflow port Din}×100

Figure 0007333246000002
Figure 0007333246000002

(参考例1) 本実施例に対応する条件で排水処理した実機(実際の排水処理プラント)において、実施例2に対応する排水処理を行ったときの、上記硝化率の5日間の平均値を求めたところ、97質量%であった。 (Reference Example 1) When the wastewater treatment corresponding to Example 2 was performed in an actual machine (actual wastewater treatment plant) in which wastewater was treated under the conditions corresponding to this example, the average value of the nitrification rate for 5 days was calculated. It was found to be 97% by mass.

(比較例1) 実施例2において、前処理装置として携帯型排水処理評価用前処理装置10を用いず、携帯型活性汚泥処理槽20のみを用いた以外は、実施例2と同様に排水処理を行い、上記硝化率の5日間の平均値を求めたところ、92質量%であった。 (Comparative Example 1) Wastewater treatment was carried out in the same manner as in Example 2, except that the portable activated sludge treatment tank 20 alone was used instead of the portable wastewater treatment evaluation pretreatment device 10 as the pretreatment device. and the average nitrification rate over 5 days was found to be 92% by mass.

上記実施例2、参考例1および比較例1における硝化率の5日間の平均値を表3に示す。 Table 3 shows the average value of the nitrification rate for 5 days in Example 2, Reference Example 1 and Comparative Example 1 above.

Figure 0007333246000003
Figure 0007333246000003

表2および表3より、本発明に係る携帯型排水処理評価用前処理装置を用いた実施例2の硝化率は、実機(実際の排水処理プラント)における対応する排水処理を行ったときの硝化率に整合する結果になっていることが分かる。
一方、表2および表3より、比較例1においては、本発明に係る携帯型排水処理評価用前処理装置を用いていないことから、硝化率が低下していることが分かる。
From Tables 2 and 3, the nitrification rate of Example 2 using the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention is the same as that of the corresponding wastewater treatment in the actual equipment (actual wastewater treatment plant). It can be seen that the results are consistent with the rate.
On the other hand, from Tables 2 and 3, it can be seen that in Comparative Example 1, since the portable pretreatment apparatus for wastewater treatment evaluation according to the present invention was not used, the nitrification rate was lowered.

本発明によれば、壁への付着物層の形成を抑制しつつ簡便かつ迅速に排水処理条件を評価するための携帯型排水処理評価前処理装置および排水処理評価方法を提供することができる。 According to the present invention, it is possible to provide a portable pretreatment apparatus for wastewater treatment evaluation and a wastewater treatment evaluation method for simply and quickly evaluating wastewater treatment conditions while suppressing the formation of a deposit layer on a wall.

10 携帯型排水処理評価用前処理装置
11 凝集槽
12 攪拌羽根
13 支持棒
14 上下位置移動手段
15 貯留室
16 回転装置
20 携帯型活性汚泥処理槽
Din 流入口
Dout 流出口
N 流入ノズル
WS 水面
B 底部
T、t 排出管
R 拡幅部
REFERENCE SIGNS LIST 10 Portable wastewater treatment evaluation pretreatment device 11 Aggregation tank 12 Stirring blade 13 Support rod 14 Vertical position moving means 15 Storage chamber 16 Rotating device 20 Portable activated sludge treatment tank Din Inlet Dout Outlet N Inflow nozzle WS Water surface B Bottom T, t Exhaust pipe R Widened part

Claims (5)

携帯型排水処理評価用前処理装置であって、
活性汚泥処理装置で処理される有機物含有排水を流入させて凝集物および凝集物処理水に分離する内容量3~12Lの凝集槽と、
前記凝集槽の槽内に、外縁部の少なくとも一部に柔軟性樹脂からなる拡幅部が設けられた攪拌羽根と、
前記攪拌羽根を凝集槽の上下方向に位置調整可能な上下位置移動手段とを有し、
前記攪拌羽根の拡幅部が撹拌羽根の回転時に凝集槽の内壁に接触し得るように配置されている
ことを特徴とする携帯型排水処理評価用前処理装置。
A pretreatment device for portable wastewater treatment evaluation,
a flocculation tank with an internal volume of 3 to 12 L into which organic matter-containing wastewater to be treated by the activated sludge treatment equipment is introduced and separated into flocculate and flocculate-treated water;
a stirring blade provided with a widened portion made of a flexible resin on at least a part of an outer edge portion in the tank of the aggregation tank;
A vertical position moving means capable of adjusting the position of the stirring blade in the vertical direction of the aggregation tank,
A portable pretreatment apparatus for evaluation of waste water treatment, wherein the widened portion of the stirring blade is arranged so as to come into contact with the inner wall of the coagulation tank when the stirring blade rotates.
前記活性汚泥処理装置で処理される有機物含有排水が、活性汚泥処理装置で処理される有機物を含有する工業排水および生活排水から選ばれる一種以上である請求項1に記載の携帯型排水処理評価用前処理装置。 2. The portable wastewater treatment evaluation method according to claim 1, wherein the organic matter-containing wastewater treated by the activated sludge treatment device is one or more selected from industrial wastewater and domestic wastewater containing organic matter treated by the activated sludge treatment device. Pretreatment device. 前記攪拌羽根が攪拌プロペラである請求項1または請求項2に記載の携帯型排水処理評価用前処理装置。 3. The portable pretreatment apparatus for evaluating wastewater treatment according to claim 1, wherein said stirring blade is a stirring propeller. 前記凝集槽と連通し当該凝集槽で処理された凝集物処理水を貯留する貯留室をさらに有するとともに、当該貯留室に貯留した凝集物処理水を排出する排出管を有し、
当該排出管の取水口が前記貯留室内に引き込まれるとともに前記貯留した凝集物処理水の水面近傍に位置するように上下移動可能に配置されている
請求項1~請求項3のいずれかに記載の携帯型排水処理評価用前処理装置。
further comprising a storage chamber communicating with the aggregation tank and storing the aggregate-treated water treated in the aggregation tank, and having a discharge pipe for discharging the aggregate-treated water stored in the storage chamber,
4. The water intake port of the discharge pipe according to any one of claims 1 to 3, wherein the water intake port is drawn into the storage chamber and arranged so as to be vertically movable so as to be positioned near the water surface of the stored aggregate-treated water. Pretreatment equipment for portable wastewater treatment evaluation.
請求項1~請求項のいずれかに記載の携帯型排水処理評価用前処理装置を用いて活性汚泥処理装置で処理される有機物含有排水を排水処理することを特徴とする排水処理評価方法。 A method for evaluating wastewater treatment , which comprises treating organic matter-containing wastewater treated by an activated sludge treatment apparatus using the portable pretreatment apparatus for evaluating wastewater treatment according to any one of claims 1 to 4 .
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007237014A (en) 2006-03-06 2007-09-20 Hitachi Plant Technologies Ltd Stirring device
JP2009241045A (en) 2008-03-31 2009-10-22 Ebara Environmental Plant Co Ltd Slurry circulation type coagulation and sedimentation treatment device, and its operation method
JP2019093351A (en) 2017-11-24 2019-06-20 コスモ石油株式会社 Portable wastewater treatment evaluation device and wastewater treatment evaluation method
JP2019118855A (en) 2017-12-28 2019-07-22 コスモ石油株式会社 Method of diagnosing operating condition of wastewater treatment facility and apparatus for diagnosing operating condition of waste water treatment facility

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007237014A (en) 2006-03-06 2007-09-20 Hitachi Plant Technologies Ltd Stirring device
JP2009241045A (en) 2008-03-31 2009-10-22 Ebara Environmental Plant Co Ltd Slurry circulation type coagulation and sedimentation treatment device, and its operation method
JP2019093351A (en) 2017-11-24 2019-06-20 コスモ石油株式会社 Portable wastewater treatment evaluation device and wastewater treatment evaluation method
JP2019118855A (en) 2017-12-28 2019-07-22 コスモ石油株式会社 Method of diagnosing operating condition of wastewater treatment facility and apparatus for diagnosing operating condition of waste water treatment facility

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