JP4893022B2 - Water quality measuring device - Google Patents

Water quality measuring device Download PDF

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JP4893022B2
JP4893022B2 JP2006046562A JP2006046562A JP4893022B2 JP 4893022 B2 JP4893022 B2 JP 4893022B2 JP 2006046562 A JP2006046562 A JP 2006046562A JP 2006046562 A JP2006046562 A JP 2006046562A JP 4893022 B2 JP4893022 B2 JP 4893022B2
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water quality
water
quality measuring
tank
measured
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JP2007192789A (en
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真一郎 淵上
昌隆 岩崎
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Panasonic Corp
Panasonic Holdings Corp
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Panasonic Corp
Matsushita Electric Industrial Co Ltd
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Priority to PCT/JP2006/305084 priority patent/WO2007069348A1/en
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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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Description

本発明は、工場や他の施設などから排出される被処理水である排水に含まれる浮遊性や沈降性を有するさまざまな異物について、フィルターを使用することなく分離し、前記異物を分離した排水の水質を計測する水質計測方法およびこれを用いた排水処理方法に関するものである。   The present invention separates various foreign matters having floatability and sedimentation contained in waste water that is treated water discharged from factories or other facilities without using a filter, and waste water from which the foreign matters are separated. The present invention relates to a water quality measurement method for measuring the water quality of water and a wastewater treatment method using the same.

従来、被処理水である排水を貯留する排水貯留槽または被処理水の好気性または嫌気性処理手段を備えた排水貯留槽の排水(被処理水と汚泥の混合水)の水質を計測する水質計測方法、この検出値に基づき水質を最適条件に制御する排水処理方法として、例えば排水貯留槽の排水に直接、溶存酸素濃度検出器を位置させて溶存酸素濃度(DO、Dissolved Oxygen)を検出し、この検出値に基づき排水貯留槽の曝気手段の曝気能力を制御するものがあるが、曝気による排水の流動化よって溶存酸素濃度検出器の検出値が不安定となり正確な値を検出することが困難である。また比較的大きい設備となる排水貯留槽に溶存酸素濃度検出器を設置することが必要で、メンテナンスも含め作業性等に課題がある。さらに曝気による多量の排水の流動化によって排水中の異物等が溶存酸素濃度検出器に付着しやすく、正確な値を検出することが困難となる課題がある。   Conventionally, water quality that measures the quality of wastewater (mixed water of treated water and sludge) from wastewater storage tanks that store wastewater that is treated water or wastewater storage tanks equipped with aerobic or anaerobic treatment means As a wastewater treatment method to control the water quality to the optimum condition based on the measurement method and the detected value, for example, a dissolved oxygen concentration detector (DO, Dissolved Oxygen) is detected by directly positioning the dissolved oxygen concentration detector in the wastewater in the wastewater storage tank. However, there are those that control the aeration capacity of the aeration means of the drainage storage tank based on this detection value, but the detection value of the dissolved oxygen concentration detector becomes unstable due to fluidization of the wastewater due to aeration, so that an accurate value can be detected. Have difficulty. In addition, it is necessary to install a dissolved oxygen concentration detector in a drainage storage tank, which is a relatively large facility, and there are problems in workability including maintenance. Furthermore, due to fluidization of a large amount of waste water by aeration, there is a problem that foreign matters in the waste water are likely to adhere to the dissolved oxygen concentration detector and it is difficult to detect an accurate value.

前記課題解決するために、排水貯留槽から、排水の一部を別設の計測槽に取り込み溶存酸素濃度、pH等の水質要素を検出するものがある。
In order to solve the above-mentioned problem , there is one that detects a water quality element such as dissolved oxygen concentration and pH by taking a part of waste water from a waste water storage tank into a separate measurement tank.

この代表的例として、同心の円筒形外周壁及びそれより低い同心の円筒形内周壁と両周壁間の底壁とで画成された環状水路内に排水を連続流入させて環状水流を形成し、環状水流中に水質計測プローブを垂下して排水の水質を計測するものがある(例えば特許文献1参照)。
特開2002−340883号公報
As a typical example, an annular water flow is formed by continuously flowing waste water into an annular water channel defined by a concentric cylindrical outer peripheral wall and a lower concentric cylindrical inner peripheral wall and a bottom wall between both peripheral walls. There is one that measures a water quality of drainage by dropping a water quality measurement probe in an annular water flow (see, for example, Patent Document 1).
JP 2002-340883 A

しかし、上記従来の特許文献1に記載のものは、被計測水中の浮遊物質の沈殿を防ぐために、環状水路内に被計測水を環状水路の接線方向に連続流入させ、被計測水の流入速度を利用することで浮遊物質の沈殿を防ぐことのできる程度の環状水流を形成させ、この環状水流中に水質計測プローブ(検出器)を垂下させており、水質計測プローブの検出部近傍によどみ点やカルマン渦が発生する構造となっており、水質計測プローブの検出部に接触する被計測水流が変動するため、検出値が不安定であり、水質計測プローブに異物が付着しやすい構造であった。また環状水流中の異物を除去する手段は提案されておらず、水質計測プローブによって正確な水質を検出することが困難であった。   However, in the above-mentioned conventional patent document 1, in order to prevent sedimentation of suspended matter in the measured water, the measured water is continuously flowed into the annular channel in the tangential direction of the annular channel, and the inflow speed of the measured water is An annular water flow that can prevent sedimentation of suspended solids is formed by using the, and a water quality measurement probe (detector) is suspended in the annular water flow. And Karman vortices are generated, and the measured water flow that contacts the detection part of the water quality measurement probe fluctuates, so the detection value is unstable and foreign matter easily attaches to the water quality measurement probe . In addition, no means for removing foreign substances in the annular water flow has been proposed, and it has been difficult to accurately detect water quality using a water quality measurement probe.

そこで本発明は水質計測槽へ流入させる被計測水の流入速度に依存することなく、被計測水中の浮遊物質の沈殿を防ぎ、水質計測プローブの検出部近傍によどみ点やカルマン渦が発生しないような水質計測装置を実現することを目的とする。また、被計測水中の異物を除去する手段を備えた水質計測装置を提供することを目的とする。   Therefore, the present invention does not depend on the flow rate of water to be measured flowing into the water quality measurement tank, prevents sedimentation of suspended solids in the water to be measured, and prevents stagnation and Karman vortices from occurring near the detection part of the water quality measurement probe. The purpose is to realize a simple water quality measuring device. Moreover, it aims at providing the water quality measuring device provided with the means to remove the foreign material in to-be-measured water.

上記従来の課題を解決するために、本発明の水質計測装置は、被計測水流入口と被計測水流出口を有する水質計測槽を備えた水質計測装置であって、前記水質計測槽に上下方向の循環流を形成するために、前記水質計測槽を上面から見て2つの空間に分け、かつ下端を水質計測槽の底面より上側に設け、上端を被計測水流出口より下側に設けた案内板からなる循環流形成手段と、この循環流形成手段の上下端の間に設置されるとともに上下方向の循環流を発生させるプロペラ形状の回転子を用いた循環流発生部を備えた循環流発生機と、水質計測プローブとを備え、前記被計測水流出口を前記循環流形成手段の上端より上側に配置するとともに、前記被計測水流入口を前記水質計測槽の底面より上側で前記循環流形成手段の下端より下側に配置し、前記水質計測プローブをその検出部が上下方向の循環流に対向する方向に設置したことを特徴とする。 In order to solve the above-described conventional problems, the water quality measurement device of the present invention is a water quality measurement device including a water quality measurement tank having a measured water inlet and a measured water outlet, and the water quality measurement tank has a vertical direction in the water quality measurement tank. In order to form a circulating flow, the water quality measuring tank is divided into two spaces when viewed from above, and a lower end is provided above the bottom surface of the water quality measuring tank, and an upper end is provided below the measured water outlet. And a circulating flow generator having a circulating flow generator using a propeller-shaped rotor that is installed between upper and lower ends of the circulating flow forming means and generates a circulating flow in the vertical direction. And a water quality measurement probe, the measured water outlet is located above the upper end of the circulating flow forming means, and the measured water inlet is located above the bottom surface of the water quality measuring tank of the circulating flow forming means. Arranged below the bottom And, characterized in that the water quality measuring probe detection unit is installed in a direction opposite to the vertical direction of the circulating flow.

本発明により、水質計測槽へ流入させる被計測水の流入速度に依存することなく、被計測水中の浮遊物質の沈殿を防ぎ、水質計測プローブの検出近傍によどみ点やカルマン渦が発生しないような水質計測装置を実現することができる。   According to the present invention, without depending on the flow rate of water to be measured flowing into the water quality measurement tank, sedimentation of suspended solids in the water to be measured is prevented, and stagnation points and Karman vortices are not generated near the detection of the water quality measurement probe. A water quality measuring device can be realized.

本発明の第1の実施の形態による水質計測装置は、被計測水流入口と被計測水流出口を有する水質計測槽を備えた水質計測装置であって、前記水質計測槽に上下方向の循環流を形成するために、前記水質計測槽を上面から見て2つの空間に分け、かつ下端を水質計測槽の底面より上側に設け、上端を被計測水流出口より下側に設けた案内板からなる循環流形成手段と、この循環流形成手段の上下端の間に設置されるとともに上下方向の循環流を発生させるプロペラ形状の回転子を用いた循環流発生部を備えた循環流発生機と、水質計測プローブとを備え、前記被計測水流出口を前記循環流形成手段の上端より上側に配置するとともに、前記被計測水流入口を前記水質計測槽の底面より上側で前記循環流形成手段の下端より下側に配置し、前記水質計測プローブをその検出部が上下方向の循環流に対向する方向に設置したものである。
The water quality measuring device according to the first embodiment of the present invention is a water quality measuring device including a water quality measuring tank having a measured water inlet and a measured water outlet, and a vertical circulation flow is applied to the water quality measuring tank. In order to form , the water quality measuring tank is divided into two spaces when viewed from the top, and the lower end is provided above the bottom of the water quality measuring tank, and the upper end is provided by a guide plate provided below the measured water outlet. A circulation flow generator having a circulation flow generation unit using a propeller-shaped rotor that is installed between the upper and lower ends of the circulation flow formation means and generates a vertical circulation flow; A measuring probe, and the measured water outlet is disposed above the upper end of the circulating flow forming means, and the measured water inlet is located above the bottom surface of the water quality measuring tank and below the lower end of the circulating flow forming means. place on a side, the In which the quality measurement probe detection unit is installed in a direction opposite to the vertical direction of the circulating flow.

本実施の形態によれば、水質計測槽へ取り込む被計測水の流量が少ない場合でも、上下方向の循環流により、被計測水に含まれる懸濁物の沈降を防止でき、被計測水が水質計測プローブの検出部に対向して流れてくるため、検出部によどみ点やカルマン渦が発生せず、正確な値を検出することができる。   According to the present embodiment, even when the flow rate of water to be measured taken into the water quality measurement tank is small, sedimentation of the suspension contained in the water to be measured can be prevented by the circulating flow in the vertical direction. Since it flows opposite to the detection part of the measurement probe, no stagnation point or Karman vortex is generated by the detection part, and an accurate value can be detected.

また、水質計測槽内の水面が循環流形成手段の上端より上側に位置するために、上下方向の循環流をスムーズに発生することができる。また、水質計測槽内の水面近傍に浮上する浮遊性の異物を被計測水流出口より効率よく流出させることができ、これらの異物によって水質計測プローブへの異物の付着を防止することができる。
Further , since the water surface in the water quality measuring tank is located above the upper end of the circulating flow forming means, the circulating flow in the vertical direction can be generated smoothly. In addition, floating foreign matters floating near the water surface in the water quality measurement tank can be efficiently discharged from the measured water outlet, and these foreign matters can prevent foreign matters from adhering to the water quality measurement probe.

さらに、水質計測槽内の水位が低い状態から被計測水を流入させる場合でも、被計測水に空気中のガスが溶け込む量を最小限に抑えることができ、水質計測槽への被計測水の流入開始から短時間で安定した計測値を得ることができる。
Furthermore , even when the water to be measured flows in from a state where the water level in the water quality measurement tank is low, the amount of gas in the air dissolved in the water to be measured can be minimized, and the water to be measured into the water quality measurement tank can be minimized. A stable measurement value can be obtained in a short time from the start of inflow.

本発明の第の実施の形態は、第1の実施の形態による水質計測装置において、水質計測槽に曝気手段を備え、この曝気手段を循環流発生機の循環流発生部の下流側と水質計測プローブの検出部との間に設置したものである。
The second embodiment of the present invention is the water quality measurement device according to the first embodiment, wherein the water quality measurement tank is provided with aeration means, and this aeration means is connected to the downstream side of the circulation flow generator of the circulation flow generator and the water quality. It is installed between the detection part of the measurement probe.

本実施の形態によれば、曝気手段により発生する気泡流が水質計測プローブに当たることにより、水質計測プローブに異物が付着しにくく、長期間安定した水質の計測を可能とすることができる。   According to the present embodiment, since the bubble flow generated by the aeration means hits the water quality measurement probe, it is difficult for foreign matters to adhere to the water quality measurement probe, and stable water quality measurement can be performed for a long period of time.

本発明の第の実施の形態は、第1と第2の実施の形態による水質計測装置において、水質計測槽に洗浄水流入口と、水質計測槽の底部に開閉可能な洗浄水流出口を備えたものである。
In the water quality measurement apparatus according to the first and second embodiments, the third embodiment of the present invention includes a washing water inlet in the water quality measuring tank and a washing water outlet that can be opened and closed at the bottom of the water quality measuring tank. Is.

本実施の形態によれば、水質計測プローブを洗浄することができ、水質計測プローブに付着した異物を除去したり、水質計測プローブ表面に付着した生物膜を除去することもでき、長期間安定した水質の計測を可能とすることができる。   According to the present embodiment, the water quality measurement probe can be washed, foreign matter adhering to the water quality measurement probe can be removed, and the biofilm adhering to the surface of the water quality measurement probe can be removed, which is stable for a long time. Water quality can be measured.

本発明の第の実施の形態は、第の実施の形態による水質計測装置において、水質計測プローブは被計測水の溶存酸素濃度を検出する溶存酸素濃度プローブであり、曝気手段により一定時間曝気することで、被計測水の溶存酸素濃度を高めた後、曝気手段による曝気を停止し、循環流発生機を運転しつつ、被計測水の溶存酸素濃度の変化量を計測するものである。
According to a fourth embodiment of the present invention, in the water quality measurement apparatus according to the second embodiment, the water quality measurement probe is a dissolved oxygen concentration probe that detects the dissolved oxygen concentration of the water to be measured, and is aerated for a predetermined time by the aeration means. Thus, after increasing the dissolved oxygen concentration of the water to be measured, aeration by the aeration means is stopped, and the amount of change in the dissolved oxygen concentration of the water to be measured is measured while operating the circulating flow generator.

本実施の形態によれば、被計測水の溶存酸素濃度を飽和濃度に近くなるまで高めた状態から溶存酸素濃度の変化量を計測することができるため、溶存酸素濃度の計測値が安定し、精度の高い計測を行うことができる。   According to the present embodiment, since the amount of change in dissolved oxygen concentration can be measured from a state in which the dissolved oxygen concentration in the water to be measured is increased to a saturation concentration, the measured value of the dissolved oxygen concentration is stable, Highly accurate measurement can be performed.

本発明の第実施の形態は、第の実施の形態による水質計測装置において、前記水質計測槽を縦方向が長く、横方向が短い形状としたものである。
In the water quality measurement apparatus according to the fourth embodiment, the fifth embodiment of the present invention is such that the water quality measurement tank has a shape having a long vertical direction and a short horizontal direction.

本実施の形態によれば、水質計測槽内の被計測水が空気と接触する面積を最小限にすることができるため、被計測水に空気中のガスが溶け込む量を最小限に抑えることができ、水質計測槽への被計測水の流入開始から短時間で安定した計測値を得ることができる。   According to the present embodiment, since the area where the water to be measured in the water quality measurement tank comes into contact with air can be minimized, the amount of gas in the air dissolved in the water to be measured can be minimized. It is possible to obtain a stable measurement value in a short time from the start of inflow of water to be measured into the water quality measurement tank.

本発明の第の実施の形態は、第1の実施の形態による水質計測装置において、循環流発生機が循環流発生部を複数段備えたものである。
According to a sixth embodiment of the present invention, in the water quality measurement apparatus according to the first embodiment, the circulating flow generator includes a plurality of circulating flow generators.

本実施の形態によれば、循環流発生機によって循環流発生部を高速回転させることなく、精度のよい水質計測に必要な被計測水の上下方向の循環流を得ることができるため、循環流発生機の所要動力低減することができる。
According to this embodiment, since the circulating flow generator can obtain a circulating flow in the vertical direction of the water to be measured necessary for accurate water quality measurement without rotating the circulating flow generator at high speed, The required power of the generator can be reduced.

本発明の第の実施の形態は、第1の実施の形態による水質計測装置において、被計測水中の異物を分離する高速旋回分離槽と低速旋回分離槽からなる異物分離手段を設け、異物分離後の処理水を水質計測槽に流入させるものである。
According to a seventh embodiment of the present invention, in the water quality measurement apparatus according to the first embodiment, a foreign matter separation means including a high-speed swirl separation tank and a low-speed swirl separation tank for separating foreign matter in the measurement target water is provided, and the foreign matter separation The treated water afterwards is made to flow into the water quality measuring tank.

本実施の形態によれば、被計測水中に含まれる異物を予め除去した被計測水を水質計測槽へ導入することができ、水質計測プローブによって長期間安定した計測を行うことができる。   According to the present embodiment, the water to be measured from which foreign matters contained in the water to be measured have been removed in advance can be introduced into the water quality measurement tank, and stable measurement can be performed for a long time using the water quality measurement probe.

本発明の第の実施の形態は、第の実施の形態による水質計測装置において、水質計測槽を上部、被計測水中の異物を分離する高速旋回分離槽と低速旋回分離槽からなる異物分離手段を下部として本体ケース内に配設したものである。
The eighth embodiment of the present invention is the water quality measuring apparatus according to the seventh embodiment, wherein the water quality measuring tank is an upper part, and the foreign matter separation is made up of a high speed swirl separation tank and a low speed swirl separation tank for separating foreign matter in the water to be measured The means is disposed in the main body case as a lower part.

本実施の形態によれば、コンパクトで省設置スペースの水質計測装置を実現することができる。   According to the present embodiment, it is possible to realize a water quality measuring device that is compact and saves installation space.

以下、本発明による実施例の水質計測装置について、図面を参照して説明する。本発明による一実施例の水質計測装置は異物分離部と水質計測部とからなっており、前段の生物処理も含めた説明とする。   Hereinafter, the water quality measuring device of the Example by this invention is demonstrated with reference to drawings. The water quality measuring apparatus according to an embodiment of the present invention includes a foreign matter separating unit and a water quality measuring unit, and the description includes the biological treatment in the previous stage.

図1は本発明による一実施例、本体ケース45内の下部に異物分離部14、上部に水質計測部30を配設した水質計測装置および生物処理手段1を示す構成図、図2は第1の分離槽、第2の分離槽からなる異物分離部の平面構成図である。なお図中の矢印は排水の流れを示す。   FIG. 1 is a block diagram showing an embodiment of the present invention, a water quality measuring device and a biological treatment means 1 in which a foreign matter separating unit 14 is disposed in the lower part of the main body case 45 and a water quality measuring unit 30 is disposed in the upper part. It is a plane block diagram of the foreign material separation part which consists of a 2nd separation tank and a 2nd separation tank. The arrows in the figure indicate the flow of drainage.

工場や他の施設などから排出される被処理水である排水を排水貯留槽に一時貯留し、次工程おいて生物処理等を行う場合があるが、以下、排水貯留槽の排水を曝気して生物処理を行う構成の一実施例に基づいて説明する。   Wastewater, which is treated water discharged from factories and other facilities, may be temporarily stored in a wastewater storage tank and biological treatment may be performed in the next process. A description will be given based on an embodiment of a configuration for performing biological treatment.

まず、生物処理手段1の構成、動作について説明する。流入管2から流量調節弁3を介して被処理水である排水を排水貯留槽である生物処理槽4に流入させ、一定量貯留する。生物処理槽4の排水(被処理水と汚泥の混合水)に供給管6、散気管7、散気管7に設けた多数の噴出孔8を介してブロワ5からの空気を供給する。この曝気によって、生物処理槽4の排水の溶存酸素濃度を高めて好気性化し、微生物による分解を促進する。生物処理槽4で浄化処理された排水は、接続管9を介して沈殿槽10に供給され、汚泥分が沈降することでこれを分離し、排出管11、開閉弁12を介して排出し活性汚泥として生物処理槽4に返送するか、余剰汚泥として排出する。汚泥分が除かれた処理水は、排出管13より排出し、放流または再利用するものである。排水の生物処理状況に応じて流量調節弁3により生物処理槽4への被処理水である排水の流入量(流入負荷)を制御する。   First, the configuration and operation of the biological treatment means 1 will be described. The wastewater that is the treated water is caused to flow from the inflow pipe 2 through the flow rate control valve 3 into the biological treatment tank 4 that is a drainage storage tank, and a certain amount is stored. Air from the blower 5 is supplied to the wastewater (mixed water of the water to be treated and sludge) from the biological treatment tank 4 through the supply pipe 6, the air diffusion pipe 7, and the numerous ejection holes 8 provided in the air diffusion pipe 7. By this aeration, the dissolved oxygen concentration of the waste water of the biological treatment tank 4 is increased to become aerobic, and the decomposition by microorganisms is promoted. The waste water purified in the biological treatment tank 4 is supplied to the sedimentation tank 10 through the connecting pipe 9, and the sludge is separated by sedimentation, and is discharged through the discharge pipe 11 and the on-off valve 12 to be activated. It returns to the biological treatment tank 4 as sludge, or discharges it as excess sludge. The treated water from which the sludge has been removed is discharged from the discharge pipe 13 and discharged or reused. The flow rate control valve 3 controls the inflow amount (inflow load) of the wastewater that is the treated water into the biological treatment tank 4 according to the biological treatment status of the wastewater.

次に、異物分離部14の構成、動作について説明する。図1に示すように工場や下水処理場などから排出される被処理水である排水は、生物処理槽4で浄化処理されるが、この排水の水質を精度よく、また長期にわたって安定して検出するには、水質検出器への異物の付着防止、さらに処理装置の配管等の閉塞を防ぐために、排水に含まれる異物を除去することが重要である。   Next, the configuration and operation of the foreign matter separation unit 14 will be described. As shown in FIG. 1, wastewater that is treated water discharged from a factory or a sewage treatment plant is purified in a biological treatment tank 4, and the quality of this wastewater is detected accurately and stably over a long period of time. In order to prevent the foreign matter from adhering to the water quality detector and to prevent the piping of the processing apparatus from being blocked, it is important to remove the foreign matter contained in the waste water.

本実施例による異物分離部14は、生物処理槽4から異物を含む排水(被処理水と汚泥の混合水)を汲み上げる排水導入ポンプ15と、排水導入ポンプ15から第1の分離槽17へ排水を取り込む排水取込み管16と、第1の分離槽17と第2の分離槽19とを結び、第1の分離槽17からの1次処理水(排水)を第2の分離槽19へ流入させる槽間接続管18と、第1の分離槽17で分離された異物を生物処理槽4へ返送する排水返送管20と、第1の分離槽17下部に設けられ排水返送管20につながる接続管21、第2の分離槽19下部に設けられ排水返送管20につながる接続管22によって構成される。   The foreign matter separation unit 14 according to the present embodiment drains the biological wastewater tank 4 from the biological treatment tank 4 to drainage water (mixed water of treated water and sludge), and drains the wastewater introduction pump 15 to the first separation tank 17. The drainage intake pipe 16 for taking in water, the first separation tank 17 and the second separation tank 19 are connected, and the primary treated water (drainage) from the first separation tank 17 flows into the second separation tank 19. Inter-tank connection pipe 18, drainage return pipe 20 for returning foreign matter separated in the first separation tank 17 to the biological treatment tank 4, and connection pipe provided at the lower part of the first separation tank 17 and connected to the drainage return pipe 20 21, a connection pipe 22 provided at the lower part of the second separation tank 19 and connected to the drainage return pipe 20.

第1の分離槽17は上部が円筒状で、下部が円錐状のケーシングから構成されており、排水取込み管16から取り込んだ排水を少量の1次処理水と残りの排水に分岐させるとともに、排水に含まれる比較的大きく、重い異物を排水とともに排水返送管20を通じて生物処理槽4へ還流させるものである。   The first separation tank 17 is composed of a casing having a cylindrical upper part and a conical lower part. The waste water taken in from the waste water intake pipe 16 is branched into a small amount of primary treated water and the remaining waste water. The relatively large and heavy foreign matter contained in the water is returned to the biological treatment tank 4 through the waste water return pipe 20 together with the waste water.

ここで、遠心力場における異物の分離速度はストークスの法則より(数1)で求めることができる。   Here, the separation speed of the foreign matters in the centrifugal force field can be obtained by (Equation 1) from Stokes' law.

Figure 0004893022
Figure 0004893022

(数1)において、vωは異物の分離速度、ρpは異物粒子の密度、ρfは液体の密度、Dpは異物粒子の直径(代表長さ)、rは異物粒子の旋回半径、ωは異物粒子の角速度、μは液体の粘度である。 In (Equation 1), vω is the separation speed of foreign matters, ρ p is the density of foreign particles, ρ f is the density of liquid, D p is the diameter (representative length) of foreign particles, r is the turning radius of foreign particles, ω Is the angular velocity of the foreign particles, and μ is the viscosity of the liquid.

つまり、排水から異物の分離を効率よく行うためには、異物粒子の回転角速度(ω)を大きくしなければならない。そこで、第1の分離槽17は排水取込み管16を通じて第1の分離槽17内の接線方向へ排水を取り込み、取り込んだ排水の流速を利用して第1の分離槽17内に強力な旋回液流を形成し、高速旋回角速度によって発生する強い遠心力で比較的直径(代表長さ)が大きく、重い質量の異物を高速旋回する第1の分離槽17の内周部へ移動させ、排水とともに接続管21、排水返送管20を通じて生物処理槽4へ還流させている。   That is, in order to efficiently separate foreign matter from wastewater, the rotational angular velocity (ω) of foreign matter particles must be increased. Therefore, the first separation tank 17 takes in the waste water in the tangential direction in the first separation tank 17 through the drainage intake pipe 16, and uses the flow velocity of the taken-in waste water to cause a powerful swirling liquid in the first separation tank 17. A strong centrifugal force generated by a high-speed swirling angular velocity has a relatively large diameter (representative length) and moves a heavy mass of foreign matter to the inner periphery of the first separation tank 17 that swirls at a high speed. It is refluxed to the biological treatment tank 4 through the connecting pipe 21 and the drainage return pipe 20.

一方、比較的大きく、重い質量の異物を分離した少量の1次処理水は槽間接続管18より流出させ、第1の分離槽17内の旋回液流によって分離された異物は、生物処理槽4へ還流する排水側へ誘引され、排水とともに生物処理槽4へと還流されている。ここで、1次処理水と生物処理槽4へ還流される排水の流量比は、3:7〜1:9とするのが好ましい。   On the other hand, a small amount of primary treated water from which foreign substances having a relatively large and heavy mass are separated flows out from the inter-tank connection pipe 18, and the foreign substances separated by the swirling liquid flow in the first separation tank 17 are separated from the biological treatment tank. 4 is attracted to the drainage side returning to 4 and is returned to the biological treatment tank 4 together with the wastewater. Here, it is preferable that the flow rate ratio between the primary treated water and the wastewater returned to the biological treatment tank 4 is 3: 7 to 1: 9.

また、第2の分離槽19は円筒状の胴部分19aとおわん状の底部分19bとで構成されている。第2の分離槽19の胴部分19aには、1次処理水を第2の分離槽19に導入する槽間接続管18と、2次処理水を導出する2次処理水導出管23とを第2の分離槽19内に突き出して設けている。2次処理水を導入する槽間接続管18は、2次処理水導出管23より下方側で、底部分19bよりも上方側に配置されている。槽間接続管18の流出口18aにはエルボが形成され(詳細は図2参照)、第2の分離槽19内で胴部分19aの接線方向へ1次処理水を流出させ、流出させた1次処理水の流速を使って第2の分離槽19に緩やかな旋回液流を形成し、第2の分離槽19内の流れを整流すると共に、低速旋回液流によって発生する弱い遠心力で1次処理水よりも重い質量の異物を第2の分離槽19の内周部へ緩やかに移動させつつ凝集させ、重力によって沈降分離させている。   The second separation tank 19 includes a cylindrical body portion 19a and a bowl-shaped bottom portion 19b. The trunk portion 19a of the second separation tank 19 includes an inter-tank connection pipe 18 for introducing the primary treated water into the second separation tank 19 and a secondary treated water outlet pipe 23 for leading the secondary treated water. It protrudes into the second separation tank 19. The inter-tank connection pipe 18 for introducing the secondary treated water is disposed below the secondary treated water outlet pipe 23 and above the bottom portion 19b. An elbow is formed at the outlet 18a of the inter-tank connecting pipe 18 (see FIG. 2 for details), and the first treated water is caused to flow out in the second separation tank 19 in the tangential direction of the barrel portion 19a. A gentle swirling liquid flow is formed in the second separation tank 19 using the flow velocity of the next treated water, the flow in the second separation tank 19 is rectified, and the weak centrifugal force generated by the low-speed swirling liquid flow 1 Foreign matter having a mass heavier than that of the next treated water is agglomerated while being slowly moved to the inner peripheral portion of the second separation tank 19, and is settled and separated by gravity.

ここで、重力場における異物の分離速度はストークスの法則より(数2)で求めることができる。   Here, the separation speed of the foreign matter in the gravitational field can be obtained by (Equation 2) from Stokes' law.

Figure 0004893022
Figure 0004893022

(数2)において、vfは異物の分離速度、ρpは異物粒子の密度、ρfは液体の密度、Dpは異物粒子の直径(代表長さ)、gは重力加速度、μは液体の粘度である。 In (Equation 2), v f is the separation speed of foreign matters, ρ p is the density of foreign particles, ρ f is the density of liquid, D p is the diameter (representative length) of foreign particles, g is gravitational acceleration, and μ is liquid. Of the viscosity.

つまり、重力を使って排水から異物の分離を効率よく行うためには、異物粒子の直径(代表長さ)(Dp)を大きくしなければならない。そこで、第2の分離槽19では接続管22に滞留時間調節弁24を設け、滞留時間調節弁24の開度を調節することにより、第2の分離槽19へと流入する1次処理水の流入速度を増減し、第2の分離槽19内の1次処理水の滞留時間を調節することで、1次処理水に含まれる異物の種類に応じた旋回流速の微調整が可能となり、効率よく異物粒子を凝集させて異物粒子の直径(Dp)を大きくし重力によって沈降分離させている。 That is, in order to efficiently separate foreign substances from wastewater using gravity, the diameter (representative length) (D p ) of the foreign particles must be increased. Therefore, in the second separation tank 19, the residence time adjustment valve 24 is provided in the connection pipe 22, and the primary treated water flowing into the second separation tank 19 is adjusted by adjusting the opening degree of the residence time adjustment valve 24. By adjusting the inflow rate and adjusting the residence time of the primary treated water in the second separation tank 19, it becomes possible to finely adjust the swirl flow velocity according to the type of foreign matter contained in the primary treated water, The foreign particles are often agglomerated to increase the diameter (D p ) of the foreign particles and settle by gravity.

一方、必要な2次処理水のみを第2の分離槽19から取り出し、分離した異物は第2の分離槽19の底部分19bの接続管22から生物処理槽4へ還流させているが、分離した異物が少ない場合、この滞留時間調節弁24を通常の運転時は閉じておき、メンテナンスを行う場合に開放し、第2の分離槽19に沈降分離した異物を排出することも可能である。   On the other hand, only necessary secondary treated water is taken out from the second separation tank 19, and the separated foreign matter is returned to the biological treatment tank 4 from the connection pipe 22 of the bottom portion 19b of the second separation tank 19, but the separation is performed. When there is little foreign matter, the residence time adjustment valve 24 can be closed during normal operation, opened for maintenance, and the foreign matter settled and separated in the second separation tank 19 can be discharged.

2次処理水導出管23の導入口23aは第2の分離槽19における旋回液流の中心軸もしくは中心軸近傍で、第2の分離槽19内の水面より下側で、上向きに開口しており、第2の分離槽19の水面に浮上した浮遊性の異物、底部分19bに沈降した沈降性の異物、及び旋回流による慣性力で第2の分離槽19の内周へ分離された異物を導入することなく、2次処理水の排出が可能となっている。   The inlet 23a of the secondary treated water outlet pipe 23 opens upward at the central axis of the swirling liquid flow in the second separation tank 19 or in the vicinity of the central axis, below the water surface in the second separation tank 19. Floating foreign matter floating on the water surface of the second separation tank 19, sedimentary foreign matter settled on the bottom portion 19b, and foreign matter separated to the inner periphery of the second separation tank 19 by the inertial force due to the swirling flow The secondary treated water can be discharged without introducing.

また、底部分19bに凝集沈降した沈降性の異物は、接続管22より生物処理槽4へ返送することが可能となっている。ここで、第2の分離槽19の上部には、空気抜き弁25を設け、第2の分離槽19内へ溜まった空気を外部へ排出するように構成することが好ましい。空気抜き弁25を設けることで、第2の分離槽19に余分な圧力がかからず、胴部分19aの強度を低く抑えることができ、第2の分離槽19のコンパクト化と低コスト化を実現できる。   In addition, the sedimentary foreign matter that has agglomerated and settled on the bottom portion 19 b can be returned to the biological treatment tank 4 through the connection pipe 22. Here, it is preferable to provide an air vent valve 25 in the upper part of the second separation tank 19 so that the air accumulated in the second separation tank 19 is discharged to the outside. By providing the air vent valve 25, no extra pressure is applied to the second separation tank 19, the strength of the body portion 19 a can be kept low, and the second separation tank 19 can be made compact and low in cost. it can.

接続管21には1次処理水の流量を調節する1次処理水流量調節弁26が、2次処理水導出管23には2次処理水流量計27が設けられている。1次処理水流量調節弁26の開度を調節することで、第1の分離槽17や第2の分離槽19へかかる圧力を調節することができ、その結果、2次処理水導出管23や槽間接続管18へと流出する1次処理水や2次処理水の流量を調節することができる。   The connection pipe 21 is provided with a primary treated water flow rate adjustment valve 26 for adjusting the flow rate of the primary treated water, and the secondary treated water outlet pipe 23 is provided with a secondary treated water flow meter 27. The pressure applied to the first separation tank 17 and the second separation tank 19 can be adjusted by adjusting the opening degree of the primary treated water flow rate adjustment valve 26, and as a result, the secondary treated water outlet pipe 23. In addition, the flow rate of the primary treated water and the secondary treated water flowing out to the inter-tank connecting pipe 18 can be adjusted.

すなわち、1次処理水の流量を増す場合は1次処理水流量調節弁26を閉じ、第1の分離槽17や第2の分離槽19へかかる圧力を高める。一方、1次処理水の流量を減らす場合は1次処理水流量調節弁26を開け、第1の分離槽17や第2の分離槽19へかかる圧力を減少させる。   That is, when increasing the flow rate of the primary treated water, the primary treated water flow rate adjustment valve 26 is closed to increase the pressure applied to the first separation tank 17 and the second separation tank 19. On the other hand, when reducing the flow rate of the primary treated water, the primary treated water flow rate control valve 26 is opened to reduce the pressure applied to the first separation tank 17 and the second separation tank 19.

このように、接続管22に1次処理水流量調節弁26を設けることで、2次処理水導出管23や槽間接続管18に異物が詰まった場合でも加圧量を増加することが可能となり、異物を押し流すことで配管の閉塞を防ぐことができる。また処理水流量の調節を流量の多い排水返送管20、接続管21で行うために、配管が細く、流量が少ない槽間接続管18や2次処理水導出管23で1次処理水の流量を調節する場合よりも1次処理水流量調節弁26の閉塞を防止することができる。   In this way, by providing the primary treated water flow rate adjustment valve 26 in the connection pipe 22, it is possible to increase the amount of pressurization even when foreign matter is clogged in the secondary treated water outlet pipe 23 and the inter-tank connection pipe 18. Thus, the blockage of the pipe can be prevented by flushing out the foreign matter. In addition, since the flow rate of the treated water is adjusted by the drainage return pipe 20 and the connecting pipe 21 having a large flow rate, the flow rate of the primary treated water is reduced by the inter-tank connecting pipe 18 and the secondary treated water outlet pipe 23 which are thin and have a low flow rate. It is possible to prevent the primary treatment water flow rate adjustment valve 26 from being blocked as compared with the case of adjusting the pressure.

図2は本実施例による異物分離部主要部の平面図である。本図に示すように、第1の分離槽17の中心軸と第2の分離槽19の中心軸が一致するように第1の分離槽17と第2の分離槽19を結ぶ槽間接続管18が設けられている。このように槽間接続管18を配置することで、配管の長さを短くすることができ、異物分離部全体をコンパクトに構成することができるとともに、配管の閉塞などの故障を最小限にすることもできる。   FIG. 2 is a plan view of the main part of the foreign matter separating part according to this embodiment. As shown in this figure, the inter-tank connection pipe connecting the first separation tank 17 and the second separation tank 19 so that the central axis of the first separation tank 17 and the central axis of the second separation tank 19 coincide with each other. 18 is provided. By arranging the inter-tank connecting pipe 18 in this way, the length of the pipe can be shortened, the entire foreign matter separating part can be configured compactly, and failures such as blockage of the pipe can be minimized. You can also.

次に、水質計測部30の構成、動作について図1を用いて説明する。   Next, the configuration and operation of the water quality measurement unit 30 will be described with reference to FIG.

水質計測槽32は上下方向が横方向よりも長い矩形の水槽で、水質計測槽32から被計測水をオーバーフローさせる被計測水流出口36とが備わっており、連続的に被計測水を水質計測槽32に流入させた場合でも、水質計測槽32内の水位は一定のレベルを保持するようになっている。   The water quality measurement tank 32 is a rectangular water tank whose vertical direction is longer than the horizontal direction, and is equipped with a measured water outlet 36 for overflowing the measured water from the water quality measurement tank 32, and continuously measures the measured water to the water quality measurement tank. Even in the case of flowing into the water level 32, the water level in the water quality measuring tank 32 is maintained at a constant level.

被計測水流入管31は被計測水流出口36よりも上側から水質計測槽32の底側へ向かって水質計測槽32内へ設置してあり、被計測水流入管31の流出口は水質計測槽32の底面近傍に位置するようになっている。
The measured water inlet pipe 31 is installed in the water quality measuring tank 32 from the upper side of the measured water outlet 36 toward the bottom of the water quality measuring tank 32, and the outlet of the measured water inlet pipe 31 is connected to the water quality measuring tank 32. It is located near the bottom.

また、水質計測槽32には上下方向の循環流を効率よく形成するための循環流形成手段として案内板35が配置されている。案内板35は水質計測槽32を上面からみると第1の矩形の空間と第2の矩形の空間とに分けるように設けてあり、かつ案内板35の下端は水質計測槽32の底面より所定間隔上側に、上端は被計測水流出口36より所定間隔下側に設けてある。   Further, a guide plate 35 is disposed in the water quality measuring tank 32 as a circulating flow forming means for efficiently forming a vertical circulating flow. The guide plate 35 is provided so as to divide the water quality measurement tank 32 into a first rectangular space and a second rectangular space when viewed from above, and the lower end of the guide plate 35 is predetermined from the bottom surface of the water quality measurement tank 32. On the upper side of the interval, the upper end is provided on the lower side of the measured water outlet 36 by a predetermined interval.

ここで、案内板35の下端と水質計測槽32の底面との間隔および案内板35の上端と被計測水流出口36との間隔は、水質計測槽32の底面から被計測水流出口36の距離の5%〜20%程度が好ましい。   Here, the distance between the lower end of the guide plate 35 and the bottom surface of the water quality measuring tank 32 and the distance between the upper end of the guide plate 35 and the measured water outlet 36 are the distance from the bottom surface of the water quality measuring tank 32 to the measured water outlet 36. About 5% to 20% is preferable.

水質計測槽32内に上下方向の循環流を発生させる循環流発生機37は駆動部と循環流発生部38からなり、第1の矩形の空間に備えてあり、駆動部によって駆動される循環流発生部38は案内板35の上端と下端との間に位置するように設置してある。   A circulating flow generator 37 for generating a circulating flow in the vertical direction in the water quality measuring tank 32 includes a driving unit and a circulating flow generating unit 38, and is provided in a first rectangular space. The circulating flow driven by the driving unit. The generator 38 is installed so as to be positioned between the upper end and the lower end of the guide plate 35.

循環流発生機37の駆動部は速度制御モーターを、循環流発生部38は下向き流れを発生させるような迎角に設定されたプロペラ形状の回転子を用いるのが好ましい。また、循環流発生部38は単段でもよいが、所定の流量が得られない場合は複数段用いればよく、所定の流量が得られる場合でも複数段用いれば高速回転させることなく、精度のよい水質計測に必要な被計測水の上下方向の循環流を得ることができるため、循環流発生機37の所要動力低減することができる。 The drive unit of the circulating flow generator 37 preferably uses a speed control motor, and the circulating flow generation unit 38 preferably uses a propeller-shaped rotor set at an angle of attack so as to generate a downward flow. The circulating flow generator 38 may be a single stage. However, if a predetermined flow rate cannot be obtained, a plurality of stages may be used. Even if a predetermined flow rate is obtained, if a plurality of stages are used, high-speed rotation is achieved without high-speed rotation. Since the circulating flow in the vertical direction of the water to be measured necessary for water quality measurement can be obtained, the required power of the circulating flow generator 37 can be reduced.

このように上下方向の循環流を発生させることで、水質計測槽32へ流入させる被計測水の流速に依存することなく、被計測水中の懸濁物質の沈降を防ぐことができる。   By generating the circulating flow in the vertical direction in this way, it is possible to prevent sedimentation of suspended substances in the measured water without depending on the flow rate of the measured water flowing into the water quality measurement tank 32.

水質計測プローブ33は検出部34を下端として、第2の矩形の空間に備えてあり、上下方向の循環流の上向き流れが検出部34に対向するようになっているため、循環流は検出部34に正面から衝突し、水質計測プローブ33の外面に沿って水質計測槽32の水面に到達するようになっている。   The water quality measurement probe 33 is provided in the second rectangular space with the detection unit 34 as a lower end, and the upward flow of the circulating flow in the vertical direction is opposed to the detection unit 34. It collides with 34 from the front, and reaches the water surface of the water quality measurement tank 32 along the outer surface of the water quality measurement probe 33.

したがって、よどみ点やカルマン渦が発生せず、水質計測プローブ33の検出部34に接触する被計測水流が変動しないため、検出値が安定しており、水質計測プローブ33に異物が付着し難い構造となっている。   Therefore, a stagnation point or Karman vortex does not occur, and the measured water flow that contacts the detection unit 34 of the water quality measurement probe 33 does not fluctuate, so that the detection value is stable, and foreign matter does not easily adhere to the water quality measurement probe 33. It has become.

また、水質計測槽32の上部には洗浄水として水道水の供給管42と、水道水の供給を開閉する開閉弁43が備えてあり、水質計測槽32の底部には洗浄水や被計測水の流出管40と洗浄水や被計測水の流出を開閉する開閉弁41が備えてあり、開閉弁41を開くことで水質計測槽32内の水道水や被計測水を生物処理槽4へと還流させることができるようになっている。   Further, a tap water supply pipe 42 as cleaning water and an open / close valve 43 for opening and closing the supply of tap water are provided in the upper part of the water quality measuring tank 32, and cleaning water and measured water are provided at the bottom of the water quality measuring tank 32. An on-off valve 41 for opening and closing the outflow pipe 40 and the outflow of washing water and measured water is provided. By opening the on-off valve 41, tap water and measured water in the water quality measuring tank 32 are transferred to the biological treatment tank 4. It can be refluxed.

曝気手段39は循環流発生部38と水質計測プローブ33の検出部34との間に設置されており、水質計測槽32内に水道水を溜め、ブロワ44から空気が送られることで、水道水による気泡流を水質計測槽32内に発生させ、水質計測プローブ33の検出部34を循環流と気泡流によって洗浄することができるようになっている。   The aeration means 39 is installed between the circulating flow generation section 38 and the detection section 34 of the water quality measurement probe 33. Tap water is stored in the water quality measurement tank 32 and air is sent from the blower 44, so that tap water is supplied. Is generated in the water quality measurement tank 32, and the detection unit 34 of the water quality measurement probe 33 can be cleaned by the circulation flow and the bubble flow.

この際、循環流発生機37を駆動し、より強力な循環水流を得ることも可能である。一定の時間間隔毎に水質計測プローブ33の検出部34を循環流と気泡流で洗浄することで、水質検出プローブ33に付着した異物を除去し、検出部34に生物膜が付着することを防止することが可能となる。   At this time, the circulating flow generator 37 can be driven to obtain a stronger circulating water flow. The detection unit 34 of the water quality measurement probe 33 is washed with a circulating flow and a bubbly flow at regular time intervals to remove foreign matters attached to the water quality detection probe 33 and prevent the biofilm from attaching to the detection unit 34. It becomes possible to do.

なお、上記のように循環流と気泡流による洗浄によっても、検出部34の生物膜などが除去できない場合は、水質計測槽32内の水道水や被計測水を排出した上で、水質計測プローブ33の検出部34へ直接水道水を噴射して、検出部34を洗浄してもよいが、検出部34にダメージを与える可能性があるので、噴射強度には注意を要する。   If the biofilm or the like of the detection unit 34 cannot be removed even by washing with the circulating flow and the bubble flow as described above, the water quality measurement probe is discharged after the tap water and the water to be measured in the water quality measurement tank 32 are discharged. Although the detection unit 34 may be cleaned by directly injecting tap water to the detection unit 34, there is a possibility that the detection unit 34 may be damaged.

また、水質計測プローブ33を溶存酸素濃度プローブとすると、水質計測槽32へ被計測水を溜め、被計測水の流入を止めた上で、循環流発生機37を駆動しつつ、曝気手段39より曝気を行い、被計測水の溶存酸素濃度を高めた後、曝気手段39による曝気を停止し、循環流発生機37のみ運転を継続することで、循環流を維持しつつ被計測水の溶存酸素濃度の変化量を計測することが可能となる。   Further, when the water quality measurement probe 33 is a dissolved oxygen concentration probe, the water to be measured is accumulated in the water quality measurement tank 32, and after the flow of the measurement water is stopped, the circulating flow generator 37 is driven and the aeration means 39 is used. After aeration and increasing the dissolved oxygen concentration of the water to be measured, aeration by the aeration means 39 is stopped, and the operation of only the circulating flow generator 37 is continued, so that the dissolved oxygen in the measured water is maintained while maintaining the circulating flow. The amount of change in density can be measured.

ここで、曝気手段39は多孔質の散気管やディフューザを用いて、微細気泡で曝気するのが好ましい。このように、水質計測部30は水質計測プローブ33に異物が付着し難く、異物が付着しても除去できるような構造となっているが、異物分離部14によって異物を除去した被計測水を水質計測槽32へ流入させることでより長期的に安定した計測値を得ることができるようになっている。   Here, the aeration means 39 is preferably aerated with fine bubbles using a porous diffuser tube or a diffuser. As described above, the water quality measurement unit 30 has a structure in which foreign matter hardly adheres to the water quality measurement probe 33 and can be removed even if foreign matter is attached. By flowing into the water quality measurement tank 32, a stable measurement value can be obtained for a longer period.

また、異物分離部14を下側に、水質計測部30を上側として本体ケースに内に配設することで、水質計測装置をコンパクトで省設置スペースにすることが可能となっている。   Further, the water quality measuring device can be made compact and save installation space by disposing the foreign matter separating unit 14 on the lower side and the water quality measuring unit 30 on the upper side in the main body case.

なお、本実施例においては曝気手段39への空気の供給はブロワ44から行っているが、装置外部の圧縮空気供給手段から供給を受けてもよい。   In this embodiment, air is supplied to the aeration means 39 from the blower 44, but may be supplied from compressed air supply means outside the apparatus.

また、本実施例においては水質計測槽32は上下方向が横方向よりも長い矩形の水槽であるが、上下方向が横方向よりも長い円筒状の水槽としてもよい。   In the present embodiment, the water quality measurement tank 32 is a rectangular water tank whose vertical direction is longer than the horizontal direction, but may be a cylindrical water tank whose vertical direction is longer than the horizontal direction.

なお、本実施例においては、被処理水である排水を汚泥とともに曝気して生物処理を生物処理槽4で行う構成、すなわち排水貯留槽を生物処理槽4とした場合の一実施例に基づいて説明したが、被処理水である排水を貯留する排水貯留槽に一時貯留した後、次工程に備えた生物処理槽4に供給して、被処理水である排水を汚泥とともに曝気して生物処理を行う場合にも適用できるものである。この場合には、排水貯留槽と生物処理槽4とも排水貯留槽として包含するものである。   In addition, in a present Example, based on one Example when the waste_water | drain which is to-be-processed water is aerated with sludge, and the biological treatment is performed in the biological treatment tank 4, ie, the waste water storage tank is used as the biological treatment tank 4. As described above, after temporarily storing in the wastewater storage tank that stores the wastewater that is the treated water, it is supplied to the biological treatment tank 4 prepared for the next process, and the wastewater that is the treated water is aerated with sludge for biological treatment. It can also be applied when performing In this case, both the waste water storage tank and the biological treatment tank 4 are included as a waste water storage tank.

以上のように、本発明によれば、水質計測槽へ流入させる被計測水の流入速度に依存することなく、被計測水中の浮遊物質の沈殿を防ぎ、水質計測プローブの検出近傍によどみ点やカルマン渦が発生しないような水質計測装置を実現することができる。また、被計測水中の異物を除去する手段を備えた水質計測装置を提供することができる。また、下部に異物分離部、上部に水質計測部を本体ケース内に配設したので、コンパクトで省設置スペースの水質計測装置を実現することができる。   As described above, according to the present invention, it is possible to prevent sedimentation of suspended solids in the water to be measured without depending on the inflow speed of the water to be measured flowing into the water quality measurement tank. It is possible to realize a water quality measuring device that does not generate Karman vortices. Moreover, the water quality measuring apparatus provided with the means to remove the foreign material in to-be-measured water can be provided. In addition, since the foreign substance separating unit is disposed in the lower part and the water quality measuring unit is disposed in the upper part of the main body case, a compact and space-saving water quality measuring apparatus can be realized.

本発明による水質計測装置は、工場や、排水処理施設などから排出されるさまざま排水に対して適用することができる。   The water quality measuring apparatus according to the present invention can be applied to various wastewater discharged from factories, wastewater treatment facilities, and the like.

本発明の一実施例における水質計測装置を示す構成図The block diagram which shows the water quality measuring device in one Example of this invention 図1における第1の分離槽、第2の分離槽の平面構成図Plane configuration diagram of the first separation tank and the second separation tank in FIG.

符号の説明Explanation of symbols

1 生物処理手段
2 流入管
3 流量調節弁
4 生物処理槽
5、44 ブロワ
6、42 供給管
7 散気管
8 噴出孔
9、21、22 接続管
10 沈殿槽
11、13 排出管
12、41、43 開閉弁
14 異物分離部
15 排水導入ポンプ
16 排水取込み管
17 第1の分離槽
18 槽間接続管
18a 流出口
19 第2の分離槽
19a 胴部分
19b 底部分
20 排水返送管
23 2次処理水導出管
23a 導入口
24 滞留時間調節弁
25 空気抜き弁
26 1次処理水流量調節弁
27 2次処理水流量計
30 水質計測部
31 被計測水流入管
32 水質計測槽
33 水質計測プローブ
34 検出部
35 案内板
36 被計測水流出口
37 循環流発生機
38 循環流発生部
39 曝気手段
40 流出管
45 本体ケース
DESCRIPTION OF SYMBOLS 1 Biological treatment means 2 Inflow pipe 3 Flow control valve 4 Biological treatment tank 5, 44 Blower 6, 42 Supply pipe 7 Air diffuser 8 Ejection hole 9, 21, 22 Connection pipe 10 Settling tank 11, 13 Exhaust pipe 12, 41, 43 On-off valve 14 Foreign matter separation part 15 Drainage introduction pump 16 Drainage intake pipe 17 First separation tank 18 Inter-tank connection pipe 18a Outlet 19 Second separation tank 19a Body part 19b Bottom part 20 Drainage return pipe 23 Derived secondary treated water Pipe 23a Inlet 24 Retention time control valve 25 Air vent valve 26 Primary treated water flow rate regulating valve 27 Secondary treated water flow meter 30 Water quality measuring part 31 Measured water inflow pipe 32 Water quality measuring tank 33 Water quality measuring probe 34 Detection part 35 Guide plate 36 Measured water outlet 37 Circulating flow generator 38 Circulating flow generator 39 Aeration means 40 Outflow pipe 45 Main body case

Claims (8)

被計測水流入口と被計測水流出口を有する水質計測槽を備えた水質計測装置であって、前記水質計測槽に上下方向の循環流を形成するために、前記水質計測槽を上面から見て2つの空間に分け、かつ下端を水質計測槽の底面より上側に設け、上端を被計測水流出口より下側に設けた案内板からなる循環流形成手段と、この循環流形成手段の上下端の間に設置されるとともに上下方向の循環流を発生させるプロペラ形状の回転子を用いた循環流発生部を備えた循環流発生機と、水質計測プローブとを備え、前記被計測水流出口を前記循環流形成手段の上端より上側に配置するとともに、前記被計測水流入口を前記水質計測槽の底面より上側で前記循環流形成手段の下端より下側に配置し、前記水質計測プローブをその検出部が上下方向の循環流に対向する方向に設置したことを特徴とする水質計測装置。 A water quality measuring device comprising a water quality measuring tank having a measured water inlet and a measured water outlet , wherein the water quality measuring tank is viewed from above in order to form a vertical circulation flow in the water quality measuring tank. Divided into two spaces, the lower end is provided above the bottom surface of the water quality measuring tank, and the upper end is located below the measured water outlet, and the circulating flow forming means is formed between the upper and lower ends of the circulating flow forming means. the circulation flow and circulation flow generator having a circulating flow generation section with the rotor of a propeller shape that generates the vertical circulation flow while being installed, and a water quality measuring probe, the object to be measured water outlet in The water inlet to be measured is arranged above the bottom of the water quality measuring tank and below the bottom of the circulating flow forming means, and the detection part of the water quality measuring probe is vertically arranged. Circulating flow in direction Water quality measuring device, characterized in that installed in opposite directions. 水質計測槽に曝気手段を備え、前記曝気手段を前記循環流発生機の循環流発生部の下流側と前記水質計測プローブの検出部との間に設置したことを特徴とする請求項1記載の水質計測装置。 The aeration means is provided in the water quality measurement tank, and the aeration means is installed between the downstream side of the circulation flow generation section of the circulation flow generator and the detection section of the water quality measurement probe. Water quality measuring device. 水質計測槽に洗浄水流入口と、前記水質計測槽の底部に開閉可能な洗浄水流出口を備え、前記水質計測プローブを洗浄することを特徴とする請求項1または2に記載の水質計測装置。 The water quality measuring device according to claim 1 or 2 , wherein the water quality measuring tank includes a cleaning water inlet and a wash water outlet that can be opened and closed at a bottom of the water quality measuring tank, and the water quality measuring probe is cleaned. 水質計測プローブは前記被計測水の溶存酸素濃度を検出する溶存酸素濃度プローブであり、前記曝気手段により一定時間曝気することで、被計測水の溶存酸素濃度を高めた後、前記曝気手段による曝気を停止し、前記循環流発生機を運転しつつ、被計測水の溶存酸素濃度の変化量を計測することを特徴とする請求項に記載の水質計測装置。 The water quality measurement probe is a dissolved oxygen concentration probe for detecting the dissolved oxygen concentration of the measurement target water. After the dissolved oxygen concentration of the measurement target water is increased by aeration for a certain period of time by the aeration unit, the aeration by the aeration unit is performed. the stops, while operating the circulation flow generator, water quality measuring apparatus according to claim 2, characterized in that to measure the amount of change in the dissolved oxygen concentration of the measurement water. 水質計測槽を縦方向が横方向より長い形状としたことを特徴とする請求項に記載の水質計測装置。 The water quality measuring device according to claim 4 , wherein the water quality measuring tank has a shape in which the vertical direction is longer than the horizontal direction. 循環流発生機が前記循環流発生部を複数段備えたことを特徴とする請求項1に記載の水質計測装置。 The water quality measuring device according to claim 1, wherein the circulating flow generator includes a plurality of stages of the circulating flow generator. 被計測水中の異物を分離する高速旋回分離槽と低速旋回分離槽からなる異物分離手段を設け、異物分離後の処理水を流入させることを特徴とする請求項1記載の水質計測装置。 2. The water quality measuring apparatus according to claim 1, wherein a foreign matter separating means comprising a high-speed swirling separation tank and a low-speed swirling separation tank for separating foreign matter in the water to be measured is provided, and treated water after the foreign matter separation is introduced. 水質計測槽を上部、前記異物分離手段を下部として本体ケース内に配設したことを特徴とする請求項に記載の水質計測装置。
8. The water quality measuring device according to claim 7 , wherein the water quality measuring tank is disposed in the main body case with the upper part being the upper part and the foreign matter separating means being the lower part.
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