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JP4979964B2 - Chemical solution injection device for water treatment equipment - Google Patents
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JP4979964B2 - Chemical solution injection device for water treatment equipment - Google Patents

Chemical solution injection device for water treatment equipment Download PDF

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JP4979964B2
JP4979964B2 JP2006074484A JP2006074484A JP4979964B2 JP 4979964 B2 JP4979964 B2 JP 4979964B2 JP 2006074484 A JP2006074484 A JP 2006074484A JP 2006074484 A JP2006074484 A JP 2006074484A JP 4979964 B2 JP4979964 B2 JP 4979964B2
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chemical injection
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injection device
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康史 三塚
正晃 藤崎
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Metawater Co Ltd
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Description

この発明は、上水道、下水道、工業用水または廃水処理水など、原水中に含まれる汚濁物質をろ過膜により分離除去して浄化処理する、膜ろ過による水処理装置用の薬液注入装置に関わり、特に、原水を殺菌する薬液注入装置や薬品添加逆洗方式の水処理装置用の薬液注入装置に関する。   The present invention relates to a chemical liquid injection device for a water treatment device by membrane filtration, in which contaminants contained in raw water, such as waterworks, sewerage, industrial water or wastewater treated water, are separated and removed by a filtration membrane and purified. The present invention also relates to a chemical liquid injection device for sterilizing raw water and a chemical liquid injection device for a chemical treatment backwash type water treatment device.

被処理水中の汚濁物質を除去する方法として、膜ろ過を利用した水処理方法がよく知られている。この膜ろ過を用いた水処理においては、運転の継続に伴い、ろ過膜の表面に汚濁物質の付着層が生じ、目詰まり、固形物による流路閉塞などのファウリングが起こり、ろ過性能が低下する問題がある。   As a method for removing pollutants in the water to be treated, a water treatment method using membrane filtration is well known. In this water treatment using membrane filtration, as the operation continues, an adhering layer of pollutants is formed on the surface of the filtration membrane, clogging, fouling such as blockage of the flow path due to solid matter, and filtration performance decreases. There is a problem to do.

そのため運転サイクルにおいて、所定時間のろ過工程後に、物理洗浄または薬品洗浄を実施し、ファウリングを低減するようにしている。物理洗浄には、膜ろ過後の処理水を逆流させる逆流洗浄(逆洗)、膜の一次側での水流によるフラッシング、空気により膜を振動させるエアースクラビングなどがあり、物理的な作用によって付着物質を取り除いている。一方、薬品洗浄は、物理洗浄では除去しきれない物質を薬品によって分解または溶解させて除去する方法で、例えば次亜塩素酸ナトリウム、硫酸、塩酸などの薬品を添加した逆洗を用いた水処理方法が提案されている(特許文献1参照)。   Therefore, in the operation cycle, physical cleaning or chemical cleaning is performed after the filtration process for a predetermined time to reduce fouling. Physical cleaning includes backflow cleaning (backwashing) that reverses the treated water after membrane filtration, flushing by water flow on the primary side of the membrane, and air scrubbing that vibrates the membrane with air. Has been removed. On the other hand, chemical cleaning is a method of removing substances that cannot be removed by physical cleaning by decomposing or dissolving them with chemicals. For example, water treatment using backwashing with chemicals such as sodium hypochlorite, sulfuric acid and hydrochloric acid added. A method has been proposed (see Patent Document 1).

図6は、本発明の対象とする従来の薬品添加逆洗(CEB:Chemical Enhanced Back Wash)方式による一般的なろ過膜の洗浄方法の一例の概略システム系統図を示し、次亜塩素酸ナトリウム添加逆洗を行なう洗浄方法の一例を示す。   FIG. 6 shows a schematic system diagram of an example of a general filtration membrane cleaning method using a conventional chemical enhanced back wash (CEB) method, which is the subject of the present invention, and shows the addition of sodium hypochlorite. An example of the washing | cleaning method which performs backwashing is shown.

図6において、1は原水、2は原水タンク、3は主ポンプ、4は原水供給弁、5は膜入口圧力計、6は水温計、7は膜モジュール(又は膜ろ過ユニット)、8は膜出口圧力計、9は流量センサー、10はろ過水出口弁、11はろ過水タンク入口弁、12はろ過水タンク、13は処理水、14は逆洗ポンプ、15は逆洗水供給弁、16は排水弁、17は次亜塩素酸ナトリウムタンク、18は次亜塩素酸ナトリウム添加ポンプ、19は次亜塩素酸ナトリウム添加バルブである。なお、図6においては、次亜塩素酸ナトリウム添加量制御装置の図示を省略している。   In FIG. 6, 1 is raw water, 2 is a raw water tank, 3 is a main pump, 4 is a raw water supply valve, 5 is a membrane inlet pressure gauge, 6 is a water temperature gauge, 7 is a membrane module (or membrane filtration unit), and 8 is a membrane. Outlet pressure gauge, 9 is a flow sensor, 10 is a filtrate outlet valve, 11 is a filtrate tank inlet valve, 12 is a filtrate tank, 13 is treated water, 14 is a backwash pump, 15 is a backwash water supply valve, 16 Is a drain valve, 17 is a sodium hypochlorite tank, 18 is a sodium hypochlorite addition pump, and 19 is a sodium hypochlorite addition valve. In FIG. 6, the sodium hypochlorite addition amount control device is not shown.

次に、図6に示すろ過膜の水処理方法および洗浄方法等について説明する。原水タンク2に流入した原水1は、主ポンプ3により原水供給弁4を介して、膜モジュール7へ供給され、ろ過される(ろ過工程)。ここで、ろ過流量は、流量センサー9の値が一定となるように主ポンプ3をインバータ制御することにより行われる。ろ過された水は流量センサー9、ろ過水出口弁10、ろ過水タンク入口弁11を介して、ろ過水タンク12へ流入される。ろ過水タンク12で容量を越えたろ過水が処理水13として次工程へと通水される。所定時間のろ過が行われたところで、逆洗が実施される(逆洗工程)。逆洗工程は、ろ過水タンク12の水(もしくはろ過水タンクとは別に設けた図示しない逆洗水槽の水)を、逆洗ポンプ14により逆洗水供給弁15を介して、膜モジュール7の二次側から一次側へ流すことによりなされ、逆洗後の水は、排水弁16を介して排水される。   Next, a water treatment method and a cleaning method for the filtration membrane shown in FIG. 6 will be described. The raw water 1 flowing into the raw water tank 2 is supplied to the membrane module 7 by the main pump 3 via the raw water supply valve 4 and filtered (filtering step). Here, the filtration flow rate is performed by inverter-controlling the main pump 3 so that the value of the flow rate sensor 9 becomes constant. The filtered water flows into the filtrate water tank 12 through the flow rate sensor 9, the filtrate water outlet valve 10, and the filtrate water tank inlet valve 11. The filtered water exceeding the capacity in the filtered water tank 12 is passed to the next process as treated water 13. When filtration is performed for a predetermined time, backwashing is performed (backwashing step). In the backwashing process, the water in the filtrate water tank 12 (or the water in a backwash water tank (not shown) provided separately from the filtrate water tank) is supplied to the membrane module 7 by the backwash pump 14 via the backwash water supply valve 15. It is made by flowing from the secondary side to the primary side, and the water after backwashing is drained through the drain valve 16.

ろ過工程および逆洗工程の所定回数が終了した後に、薬品を添加して逆洗を実施する(薬品添加逆洗工程)。図6の場合、次亜塩素酸ナトリウム添加逆洗として、前記ろ過水による逆洗に続けて、次亜塩素酸ナトリウムタンク17に貯留された次亜塩素酸ナトリウムを、次亜塩素酸ナトリウム添加ポンプ18を用いて次亜塩素酸ナトリウム添加バルブ19を介して逆洗水に添加し、所定濃度の残留塩素濃度とした水を膜モジュールに注入する。膜モジュール7内が所定濃度の残留塩素水で満たされたところで一旦逆洗ポンプ14を停止し、各バルブを閉じて、所定時間膜モジュール7を残留塩素水に浸漬する(薬液浸漬工程)。所定時間浸漬後に再度逆洗ポンプを起動してろ過水にて逆洗を実施することにより膜モジュール内の塩素水を洗い流すリンスが実施される(リンス工程)。   After a predetermined number of times of the filtration step and the backwashing step are completed, the chemical is added to perform the backwashing (chemical addition backwashing step). In the case of FIG. 6, as sodium hypochlorite addition backwashing, sodium hypochlorite stored in the sodium hypochlorite tank 17 is replaced with sodium hypochlorite addition pump following the backwashing with the filtered water. 18 is added to the backwash water through a sodium hypochlorite addition valve 19 and water having a predetermined residual chlorine concentration is injected into the membrane module. When the inside of the membrane module 7 is filled with residual chlorine water of a predetermined concentration, the backwash pump 14 is temporarily stopped, each valve is closed, and the membrane module 7 is immersed in the residual chlorine water for a predetermined time (chemical solution immersion step). After immersing for a predetermined time, the backwash pump is started again, and backwashing is performed with filtered water, thereby rinsing off the chlorine water in the membrane module (rinsing step).

上記のように、逆洗工程、薬品添加逆洗工程、薬液浸漬工程およびリンス工程を含むろ過膜の洗浄方式を、薬品添加逆洗方式と称する。なお、膜面へのファウリング物質の洗浄薬品としては、上記の次亜塩素酸ナトリウム以外に、硫酸、塩酸、その他の薬品が使われる場合もある。さらに、前記特許文献1に開示されたように複数の薬品が使われる場合もある。   As described above, a cleaning method for a filtration membrane including a backwashing step, a chemical addition backwashing step, a chemical solution immersion step, and a rinsing step is referred to as a chemical addition backwashing method. In addition to the above sodium hypochlorite, sulfuric acid, hydrochloric acid, and other chemicals may be used as cleaning chemicals for fouling substances on the membrane surface. Further, as disclosed in Patent Document 1, a plurality of chemicals may be used.

ところで、前記通常の逆洗工程や薬品添加逆洗工程における逆洗水の流量制御方法としては、例えば、インバータを用いたPID制御により定流量制御が行われている。上記従来の制御方法及び装置について図5に基づいて述べる。図5は、ろ過水タンクとは別に設けた逆洗水槽22の水を、逆洗ポンプ22を有する逆洗ライン30を介して膜ろ過ユニット21に通流し、逆洗ライン30の途中に、薬液注入ライン24を設けた例を示す。図5において、25は流量計(伝送器)、26は流量制御器(PID調節計)、27はインバータ、28は制御コントローラ(PLC)、29はプログラマブル操作表示器(POD)である。   By the way, as a flow control method of the backwash water in the normal backwashing process or the chemical addition backwashing process, for example, constant flow control is performed by PID control using an inverter. The conventional control method and apparatus will be described with reference to FIG. In FIG. 5, water in a backwash water tank 22 provided separately from the filtrate water tank is passed through a membrane filtration unit 21 via a backwash line 30 having a backwash pump 22, and a chemical solution is placed in the middle of the backwash line 30. An example in which an injection line 24 is provided is shown. In FIG. 5, 25 is a flow meter (transmitter), 26 is a flow controller (PID controller), 27 is an inverter, 28 is a controller (PLC), and 29 is a programmable operation display (POD).

図5により、以下に述べるような流量制御を行うとともに流量監視を行う。流量計25の出力は、流量制御器(PID調節計)26→インバータ27→逆洗ポンプ23用モータのフィードバックループでポンプモータの制御を行う。また、流量計25の伝送出力を分岐して制御コントローラ28に直接入力し、指令流量に対して異常な偏差が生じていないか監視を行なう。さらに、制御コントローラ(通常PLC:プログラマブルコントローラ) 28から流量制御器26へ流量指令値や設定パラメータを伝送し、流量制御器26はこの指令値に従って制御を行う。   According to FIG. 5, flow control as described below is performed and flow monitoring is performed. The output of the flow meter 25 controls the pump motor in the feedback loop of the flow controller (PID controller) 26 → inverter 27 → backwash pump 23 motor. Further, the transmission output of the flow meter 25 is branched and directly input to the controller 28 to monitor whether or not an abnormal deviation has occurred with respect to the command flow rate. Further, a flow rate command value and setting parameters are transmitted from the control controller (normal PLC: programmable controller) 28 to the flow rate controller 26, and the flow rate controller 26 performs control according to this command value.

また、流量制御器26から制御コントローラ28へ現状運転値、異常情報を伝送する。流量制御器26で、設定流量に対する上下偏差を監視させ、偏差を超えた場合には制御コントローラ28に警報を伝え、制御コントローラ28は偏差異常通知を行う。さらに、各設定流量において想定される周波数範囲を設定し、その周波数範囲より外れる場合には、制御コントローラ28は警報を伝える機能(周波数監視機能)を備える。   Further, the current operation value and abnormality information are transmitted from the flow rate controller 26 to the control controller 28. The flow rate controller 26 monitors the vertical deviation with respect to the set flow rate. If the deviation is exceeded, an alarm is transmitted to the controller 28, and the controller 28 notifies the deviation abnormality. Furthermore, the frequency range assumed in each set flow rate is set, and when the frequency range is out of the frequency range, the controller 28 has a function of transmitting an alarm (frequency monitoring function).

上記説明は、薬品添加逆洗方式の水処理装置に関するが、後述する本発明が対象とする水処理装置用の薬液注入装置は、上記装置に限定されるものではない。例えば、図6において、次亜塩素酸ナトリウムタンク17に貯留された次亜塩素酸ナトリウムを、次亜塩素酸ナトリウム添加ポンプ18を用いて次亜塩素酸ナトリウム添加バルブ19を介して逆洗水に添加する薬液注入ラインを、水温計6と膜モジュール7との間の原水供給ラインに設け、原水に薬液を注入することにより、原水を殺菌する薬液注入装置も対象となる。この場合、薬品添加逆洗は実施せず原水殺菌のみとする場合と薬品添加逆洗を併用する場合とがあり、また小規模システムにおいては、通常の逆洗工程を実施しないこともある。
特開2004−41935号公報
Although the above description relates to a chemical treatment backwash type water treatment apparatus, a chemical liquid injection apparatus for a water treatment apparatus targeted by the present invention described later is not limited to the above apparatus. For example, in FIG. 6, sodium hypochlorite stored in the sodium hypochlorite tank 17 is converted into backwash water via a sodium hypochlorite addition valve 19 using a sodium hypochlorite addition pump 18. A chemical solution injection device that sterilizes raw water by providing a chemical solution injection line to be added to the raw water supply line between the water temperature gauge 6 and the membrane module 7 and injecting the chemical solution into the raw water is also an object. In this case, there is a case where chemical addition backwashing is not performed and only raw water sterilization is used, and a case where chemical addition backwashing is used in combination, and in a small scale system, a normal backwashing process may not be performed.
JP 2004-41935 A

ところで、上記のような原水を殺菌する水処理装置や薬品添加逆洗(CEB)方式の水処理装置における従来の薬液注入装置においては、下記のような問題があった。   By the way, the conventional chemical solution injection apparatus in the water treatment apparatus for sterilizing raw water or the chemical addition backwash (CEB) type water treatment apparatus as described above has the following problems.

薬品注入配管は、薬液ラインを分断する開閉弁(通常、自動開閉弁)によって薬液が漏洩するのを防止しているが、注入ノズル部に薬液が残存してしまう問題があった。これにより原水や逆洗水が通流する主配管に水が流れていない時、薬品注入配管の残存薬液が主配管内に流出して配管と接触することになり、配管の腐食要因となっていた。また薬液注入部の管は耐腐食性のプラスチック管で構成するすることが望まれる。しかしながら、強度的観点からはライニング管を使用することが望ましく、この場合には、ライニングが剥がれて注入管が腐食するといった問題も生じていた。   The chemical injection pipe prevents the chemical liquid from leaking by an on-off valve (usually an automatic on-off valve) that divides the chemical liquid line, but there is a problem that the chemical liquid remains in the injection nozzle portion. As a result, when water is not flowing into the main pipe through which raw water or backwash water flows, the chemical solution remaining in the chemical injection pipe flows into the main pipe and comes into contact with the pipe, which is a cause of corrosion of the pipe. It was. Further, it is desirable that the chemical solution injection tube is made of a corrosion-resistant plastic tube. However, from the viewpoint of strength, it is desirable to use a lining pipe. In this case, there is a problem that the lining is peeled off and the injection pipe is corroded.

この発明は、上記のような点に鑑みてなされたもので、この発明の課題は、水処理装置用の薬液注入装置において、薬品注入配管内の薬液残存を抑制し、薬品注入配管および主配管の腐食事故を防止することにある。   The present invention has been made in view of the above points, and an object of the present invention is to suppress the remaining of the chemical liquid in the chemical injection pipe in the chemical injection apparatus for the water treatment apparatus, and to connect the chemical injection pipe and the main pipe. It is to prevent corrosion accidents.

前述の課題を解決するため、この発明は、原水をろ過膜により浄化処理して処理水を得る水処理を対象とする薬液注入装置であって、前記水処理における原水またはろ過膜の洗浄用逆洗水が通流する主配管に設けた薬品注入用のポートに、薬品注入配管を開閉弁を介して挿入してなる水処理装置用の薬液注入装置において、前記主配管の前記ポート部上流側と前記薬品注入配管の前記開閉弁下流側との間を、水導入配管により継手を介して接続してなる薬品注入配管内の洗浄手段を備えたことを特徴とする(請求項1)。上記構成により、上流側と下流側の圧力差に基づき、前記水導入配管内において主配管側から薬品注入配管側への水の流れが生じ、薬品注入配管内が主配管の通流水により洗浄されて薬液残存が抑制される。これにより、配管の腐食事故を防止することができる。   In order to solve the above-described problems, the present invention is a chemical liquid injection device for water treatment that purifies raw water with a filtration membrane to obtain treated water, and is a reverse for washing raw water or a filtration membrane in the water treatment. In a chemical injection device for a water treatment apparatus, in which a chemical injection pipe is inserted through an opening / closing valve into a chemical injection port provided in a main pipe through which washing water flows, the upstream side of the port portion of the main pipe And cleaning means in the chemical injection pipe formed by connecting a water introduction pipe through a joint between the chemical injection pipe and the downstream side of the on-off valve (claim 1). With the above configuration, based on the pressure difference between the upstream side and the downstream side, water flows from the main pipe side to the chemical injection pipe side in the water introduction pipe, and the inside of the chemical injection pipe is washed with the flowing water of the main pipe. As a result, the remaining chemical is suppressed. Thereby, the corrosion accident of piping can be prevented.

また、上記請求項1の発明の実施態様としては、下記請求項2ないし5の発明が好ましい。即ち、前記請求項1に記載の薬液注入装置において、前記主配管のポートを設ける部分には、前記主配管通流水の圧力低減用の縮流部を設けたものとする(請求項2)。これにより、縮流部の減圧に基づき、前記水導入配管内の薬品注入配管側への水の流れが促進され、洗浄効果が向上する。   As an embodiment of the invention of claim 1, the inventions of claims 2 to 5 are preferable. That is, in the chemical injection device according to the first aspect, a portion for providing the port of the main pipe is provided with a contraction portion for reducing the pressure of the water flowing through the main pipe (claim 2). Thereby, the flow of water to the chemical injection pipe side in the water introduction pipe is promoted based on the decompression of the contraction portion, and the cleaning effect is improved.

さらに、薬品注入配管自体の腐食防止の観点から、前記請求項1または2に記載の薬液注入装置において、少なくとも前記薬品注入配管および薬品注入配管に設けた継手の材料を、前記薬品に対する耐腐食性材料とする(請求項3)。   Furthermore, from the viewpoint of preventing corrosion of the chemical injection pipe itself, the chemical injection apparatus according to claim 1 or 2, wherein at least a material of a joint provided in the chemical injection pipe and the chemical injection pipe is corrosion resistant to the chemical. Material (Claim 3).

また、洗浄効果向上に主配管通流水の動圧を利用する観点から、前記請求項1に記載の薬液注入装置において、前記主配管に設けた継手は、主配管の水通流部に挿入され、通流水の動圧を受けて前記水導入配管内の薬品注入配管側への水の流れを促進する動圧受部を備えたことを特徴とする(請求項4)。さらに、構造を簡単化する観点から、前記請求項4に記載の薬液注入装置において、前記動圧受部は、前記継手の主配管の水通流部に挿入された管の先端部を斜めにカットした傾斜開口部を通流水の上流側に向けて配設したものとする(請求項5)。   Further, from the viewpoint of using the dynamic pressure of the main pipe flowing water for improving the cleaning effect, in the chemical liquid injector according to claim 1, the joint provided in the main pipe is inserted into the water flowing portion of the main pipe. In addition, a dynamic pressure receiving portion that receives the dynamic pressure of the flowing water and promotes the flow of water to the chemical injection pipe side in the water introduction pipe is provided (Claim 4). Furthermore, from the viewpoint of simplifying the structure, in the chemical injection device according to claim 4, the dynamic pressure receiving portion cuts an end portion of a pipe inserted into a water flow portion of the main pipe of the joint obliquely. The inclined opening portion is disposed toward the upstream side of the flowing water (claim 5).

また、前述の課題は下記の請求項6ないし7の発明によっても解決できる。即ち、前記請求項1に記載の薬液注入装置において、前記薬品注入配管内の洗浄手段は、請求項1に記載のものに代えて、薬品注入配管周縁部の圧力差を利用した自己洗浄手段とし、この自己洗浄手段は、前記薬品注入配管を前記主配管に設けたフランジ付ポート内に隙間を設けて液密的に挿入し、かつ、主配管の水通流部に挿入された薬品注入配管の先端部を斜めにカットした傾斜開口部を通流水の下流側に向けて配設し、さらに、前記フランジ付ポート内の隙間に対向して薬品注入配管の外周部に穴を備えたものとし、主配管の通流水が前記フランジ付ポート内の隙間と前記薬品注入配管の穴を経由して前記傾斜開口部から流出する構成を備えたものとしたことを特徴とする(請求項6)。   The above-mentioned problems can also be solved by the inventions of claims 6 to 7 below. That is, in the chemical injection device according to claim 1, the cleaning means in the chemical injection pipe is a self-cleaning means using a pressure difference at the peripheral portion of the chemical injection pipe, instead of the one described in claim 1. In this self-cleaning means, the chemical injection pipe is inserted into the flanged port provided in the main pipe with a gap in a liquid-tight manner, and the chemical injection pipe is inserted into the water flow portion of the main pipe. It is assumed that the front end of the chemical is disposed obliquely through the inclined opening toward the downstream side of the flowing water, and further, a hole is provided in the outer peripheral portion of the chemical injection pipe facing the gap in the flanged port. The main pipe has a structure in which the flowing water flows out of the inclined opening via the gap in the flanged port and the hole of the chemical injection pipe (Claim 6).

さらに、前記請求項6に記載の薬液注入装置において、前記自己洗浄手段は、薬品注入配管を、前記主配管に設けたフランジ付ポート内に、スリーブを介して液密的に挿入してなり、前記スリーブの内周部には、薬品注入配管の軸方向に沿った逆洗水導入用の導入溝と前記穴への連通溝とを備えたものとし、主配管の通流水が前記導入溝および連通溝と前記薬品注入配管の穴を経由して前記傾斜開口部から流出する構成を備えたものとする(請求項7)。   Furthermore, in the chemical injection device according to claim 6, the self-cleaning means is configured to insert a chemical injection pipe in a liquid-tight manner through a sleeve into a flanged port provided in the main pipe, The inner peripheral portion of the sleeve is provided with an introduction groove for introducing backwash water along the axial direction of the chemical injection pipe and a communication groove to the hole. It is assumed that a structure is provided that flows out of the inclined opening via a communication groove and a hole of the chemical injection pipe (Claim 7).

また、薬品添加逆洗方式の水処理装置用の薬液注入装置の発明としては、原水を浄化処理して処理水を得るろ過膜と、前記処理水の一部を前記ろ過膜の逆洗水として用いてろ過膜の逆洗を行う逆洗ラインと、この逆洗ラインに薬品を添加して逆洗を行う薬品注入ラインとを備えた薬品添加逆洗方式の水処理装置用の薬液注入装置において、前記薬品注入ラインは、薬品注入配管を前記逆洗ラインに設けた薬品注入用のポートに開閉弁を介して挿入してなり、かつ前記薬品注入配管内の洗浄手段を備えるものとし、この洗浄手段は、前記逆洗ラインの前記ポート部上流側と前記薬品注入配管の前記開閉弁下流側との間を、水導入配管により継手を介して接続したものとしたことを特徴とする(請求項8)。   Moreover, as invention of the chemical | medical solution injection | pouring apparatus for water treatment apparatuses of a chemical addition backwash system, the filtration membrane which purifies raw water and obtains treated water, and a part of the treated water serves as backwash water for the filtration membrane In a chemical injection device for a water treatment device of a chemical addition backwashing system comprising a backwashing line for backwashing a filtration membrane and a chemical injection line for adding a chemical to the backwashing line for backwashing The chemical injection line is formed by inserting a chemical injection pipe into a chemical injection port provided in the backwash line via an on-off valve, and provided with cleaning means in the chemical injection pipe. The means is characterized in that the upstream side of the port portion of the backwash line and the downstream side of the on-off valve of the chemical injection pipe are connected by a water introduction pipe via a joint. 8).

この発明によれば、水処理装置用の薬液注入装置において、薬品注入配管内の薬液残存を抑制し、薬品注入配管および主配管の腐食事故を防止することができる。   According to this invention, in the chemical injection device for the water treatment device, the chemical solution remaining in the chemical injection piping can be suppressed, and corrosion accidents of the chemical injection piping and the main piping can be prevented.

本発明の実施例について、図1ないし図4に基づき、以下に述べる。なお、図1ないし図4の実施例は、薬品添加逆洗方式の水処理装置用の薬液注入装置を対象として述べるが、本発明はこの実施例によって限定されるものではない。   An embodiment of the present invention will be described below with reference to FIGS. 1 to 4 will be described with respect to a chemical injection device for a chemical treatment backwashing water treatment apparatus, but the present invention is not limited to this embodiment.

図1は、本発明の薬液注入装置の実施例に係る模式的構成図、図2は図1における継手(主配管側)の異なる実施例に係る模式的構成図、図3は図1とは異なる実施例に係る模式的構成図、図4は図3とは異なる実施例に係る模式的構成図である。上記各図において、機能が同一の部材には同一番号を付して示す。   1 is a schematic configuration diagram according to an embodiment of the chemical liquid injector of the present invention, FIG. 2 is a schematic configuration diagram according to a different embodiment of the joint (main pipe side) in FIG. 1, and FIG. FIG. 4 is a schematic configuration diagram according to an embodiment different from FIG. 3. In each said figure, the same number is attached | subjected and shown to the member with the same function.

図1において、24は薬液注入ライン、24aは薬液注入配管、30は主配管としての逆洗ライン、30aは薬品注入用のポート、30bは縮流部、41は開閉弁、42は絞り弁、50は継手(逆洗ライン側)、51は継手(薬液注入配管側)、52は水導入配管である。上記構成によれば、逆洗ライン30における逆洗水(流れをGで示す)上流側の圧力P1が下流側の圧力P2に比較して大きいので、逆洗水はその一部が、流れをFで示すように、水導入配管52を経由して、薬液注入配管24a内にも分岐して流れる。そのため、薬品添加後に開閉弁41を閉とした際に、薬液注入配管24a内に残留する薬品は、この分岐流によって洗い流される。従って、逆洗ラインの配管腐食事故を防止することができる。 In FIG. 1, 24 is a chemical liquid injection line, 24a is a chemical liquid injection pipe, 30 is a backwash line as a main pipe, 30a is a port for chemical injection, 30b is a flow reducing portion, 41 is an on-off valve, 42 is a throttle valve, 50 is a joint (backwash line side), 51 is a joint (chemical solution injection pipe side), and 52 is a water introduction pipe. According to the above configuration, the backwash water in the backwash line 30 (the flow is indicated by G) has a higher pressure P 1 on the upstream side than the pressure P 2 on the downstream side. As indicated by F, the water also branches and flows into the chemical liquid injection pipe 24a via the water introduction pipe 52. Therefore, when the on-off valve 41 is closed after the addition of the chemical, the chemical remaining in the chemical liquid injection pipe 24a is washed away by this branch flow. Therefore, a pipe corrosion accident in the backwash line can be prevented.

上記薬品注入配管24aおよび薬品注入配管に設けた継手51の材料は、薬品注入配管自体の腐食防止の観点から、薬品に対する耐腐食性材料とすることが好ましい。なお、前記縮流部30bは、かならずしも必要ではないが、上流側の圧力P1と下流側の圧力P2との差圧を高めて、分岐流による薬品洗浄効果を向上するためには、例えば、逆洗ラインの一部をベンチュリ形状にして縮流部を設けることが好ましい。 The material of the joint 51 provided in the chemical injection pipe 24a and the chemical injection pipe is preferably a corrosion-resistant material against chemicals from the viewpoint of preventing corrosion of the chemical injection pipe itself. Incidentally, the contraction portion 30b is not necessarily required, to increase the pressure difference between the pressure P 2 of the pressure P 1 and the downstream side of the upstream side, in order to improve the chemical cleaning effect by the branch stream, for example, In addition, it is preferable that a part of the backwash line is made into a venturi shape to provide a contracted portion.

次に、図2について述べる。図2の(a)は、図1における継手(逆洗ライン側)50を、50aで示すような継手構成とした実施例を示す。この継手50aは、逆洗ライン30の逆洗水通流部に挿入され、逆洗水の動圧(図示のPV)を受けて、前記水導入配管52内の薬品注入配管側への水の流れを促進するようにしたものである。 Next, FIG. 2 will be described. 2A shows an embodiment in which the joint (backwash line side) 50 in FIG. 1 has a joint configuration as indicated by 50a. This joint 50a is inserted into the backwash water flow portion of the backwash line 30, receives the dynamic pressure of backwash water (P V in the figure), and supplies water to the chemical injection pipe side in the water introduction pipe 52. It is intended to promote the flow of

図2の(b)は、図2の(a)とは異なる継手50bの実施例を示す。図2(b)の継手50bは、逆洗ラインの逆洗水通流部に挿入された管の先端部を斜めにカットした傾斜開口部を逆洗水の上流側に向けて配設したもので、図示のPVが動圧受部となる。図2(b)の継手構成の方が、図2(a)に比較して、構造が簡単である。 FIG. 2 (b) shows an embodiment of a joint 50b different from FIG. 2 (a). The joint 50b in FIG. 2 (b) is provided with an inclined opening portion formed by obliquely cutting the tip of a pipe inserted in the backwash water flow portion of the backwash line facing the upstream side of the backwash water. in, the P V Gado pressure receiving portion shown. The structure of the joint shown in FIG. 2B is simpler than that shown in FIG.

次に、図3の実施例について述べる。図3において、24は薬液注入ライン、24aは薬液注入配管、24bは傾斜開口部、24cおよび32はフランジ、30は逆洗ライン、31はフランジ付ポート、60は薬液注入配管に設けた穴、71はフランジ付ポートと薬液注入配管との間の隙間、75はシールである。   Next, the embodiment of FIG. 3 will be described. 3, 24 is a chemical injection line, 24a is a chemical injection pipe, 24b is an inclined opening, 24c and 32 are flanges, 30 is a backwash line, 31 is a port with a flange, 60 is a hole provided in the chemical injection pipe, Reference numeral 71 denotes a gap between the flanged port and the chemical solution injection pipe, and reference numeral 75 denotes a seal.

図3の実施例は、薬品注入配管周縁部の圧力差を利用した自己洗浄手段を備える実施例であり、この自己洗浄手段は、薬品注入配管24aを逆洗ライン30に設けたフランジ付ポート31内に隙間71を設けて液密的に挿入し、かつ、逆洗水通流部に挿入された薬品注入配管24aの先端部を斜めにカットした傾斜開口部24bを逆洗水の下流側に向けて配設し、さらに、前記フランジ付ポート内の隙間71に対向して薬品注入配管の外周部に穴60を備えたものとすることにより、逆洗水が前記フランジ付ポート31内の隙間71と薬品注入配管の穴60を経由して前記傾斜開口部24bから流出するように構成したものである。   The embodiment of FIG. 3 is an embodiment provided with a self-cleaning means using the pressure difference at the peripheral portion of the chemical injection pipe, and this self-cleaning means is a flanged port 31 provided with a chemical injection pipe 24a in the backwash line 30. An inclined opening 24b is formed on the downstream side of the backwash water by providing a gap 71 therein and liquid-tightly inserting it, and obliquely cutting the tip of the chemical injection pipe 24a inserted in the backwash water flow-through portion. The backwash water is further provided with a hole 60 in the outer peripheral portion of the chemical injection pipe so as to face the gap 71 in the flanged port, so that the backwash water is provided in the gap in the flanged port 31. 71 and the hole 60 of the chemical injection pipe are configured to flow out from the inclined opening 24b.

前記傾斜開口部24bの下流側の圧力P2は、逆洗ライン30における前記隙間71近傍部に示す圧力P1に比較して低い圧力(負圧)となるので、薬品注入配管周縁部の圧力差を利用した自己洗浄が可能となる。前記傾斜開口部24bの傾斜角は、例えば、30〜45°とする。薬品注入配管の穴60は、薬品注入配管上部外周に1〜4個設ける。 The pressure P 2 on the downstream side of the inclined opening 24b is lower than the pressure P 1 shown in the vicinity of the gap 71 in the backwash line 30 (negative pressure). Self-cleaning using the difference becomes possible. The inclination angle of the inclined opening 24b is, for example, 30 to 45 °. One to four holes 60 of the chemical injection pipe are provided on the outer periphery of the upper part of the chemical injection pipe.

なお、図1及び図3において、薬品注入配管24aの先端部である、薬液を添加する水流部での薬液投入位置は、水が流れる配管中の水通流部に対して中央部付近に配置されることが好ましいが、投入された薬液が水中に適切に混合されるのであれば、その位置は特にこれに限定されない。   In FIG. 1 and FIG. 3, the chemical solution input position in the water flow portion to which the chemical solution is added, which is the tip portion of the chemical injection pipe 24a, is arranged near the central portion with respect to the water flow portion in the pipe through which water flows. However, the position is not particularly limited as long as the charged chemical solution is appropriately mixed in water.

次に、図4の実施例について述べる。図4(a)は実施例に係る要部の側断面図、図4(b)は図4(a)におけるA−A線に沿った側断面図を示す。   Next, the embodiment of FIG. 4 will be described. 4A is a side cross-sectional view of a main part according to the embodiment, and FIG. 4B is a side cross-sectional view along the line AA in FIG. 4A.

図4の実施例は、図3の実施例をベースにスリーブ70を設けた実施例で、薬品注入配管24aを耐腐食性材料、例えばPVC等の樹脂材料で構成した場合の強度不足をスリーブ70によって補うようにした実施例であり、前記自己洗浄の基本的原理は、図3の実施例の場合と同様である。   The embodiment of FIG. 4 is an embodiment in which the sleeve 70 is provided based on the embodiment of FIG. 3, and the sleeve 70 shows insufficient strength when the chemical injection pipe 24a is made of a corrosion-resistant material, for example, a resin material such as PVC. The basic principle of the self-cleaning is the same as that of the embodiment of FIG.

図4の実施例における前記自己洗浄手段は、薬品注入配管24aを、逆洗ラインに設けたフランジ付ポート31内に、スリーブ70を介して液密的に挿入し、スリーブ70の内周部には、薬品注入配管の軸方向に沿った逆洗水導入用の導入溝72を例えば2個、ならびに薬品注入配管の穴付近に設けた穴への連通溝73を備えたものとし、傾斜開口部24b部の負圧に基づいて、逆洗水が、図示Fのように、前記導入溝72および連通溝73と薬品注入配管の穴60を経由して傾斜開口部24bから流出するような構成としている。   In the self-cleaning means in the embodiment of FIG. 4, the chemical injection pipe 24a is liquid-tightly inserted through the sleeve 70 into the flanged port 31 provided in the backwash line, and the inner periphery of the sleeve 70 is inserted. Is provided with, for example, two introduction grooves 72 for introducing backwash water along the axial direction of the chemical injection pipe, and a communication groove 73 to a hole provided near the hole of the chemical injection pipe. Based on the negative pressure of the portion 24b, backwash water flows out of the inclined opening 24b through the introduction groove 72, the communication groove 73 and the hole 60 of the chemical injection pipe as shown in FIG. Yes.

なお、スリーブ70の材料は、肉厚が取れ、強度保持上問題がない場合には樹脂材料でよいが、肉厚小で強度重視の場合には、耐食性のコーティングを行った鉄やステンレスとする。また、フランジ付ポート31は、強度上必要に応じてリブ33を備えるものとする。   The material of the sleeve 70 may be a resin material when the thickness is sufficient and there is no problem in strength maintenance. However, when the thickness is small and the strength is important, iron or stainless steel with a corrosion-resistant coating is used. . Further, the flanged port 31 is provided with ribs 33 as required for strength.

本発明の薬液注入装置の実施例に係る模式的構成図。The typical block diagram which concerns on the Example of the chemical | medical solution injection device of this invention. 図1における継手(主配管側)の異なる実施例に係る模式的構成図。The typical block diagram which concerns on the Example from which the coupling (main piping side) in FIG. 1 differs. 本発明の薬液注入装置の図1とは異なる実施例に係る模式的構成図。The typical block diagram which concerns on the Example different from FIG. 1 of the chemical injection device of this invention. 本発明の薬液注入装置の図3とは異なる実施例に係る模式的構成図。The typical block diagram which concerns on the Example different from FIG. 3 of the chemical | medical solution injection device of this invention. 逆洗水の流量を逆洗ポンプ用インバータによりPID制御する従来の制御方法及び装置の系統図。The system diagram of the conventional control method and apparatus which perform PID control of the flow volume of backwash water with the inverter for backwash pumps. 従来の薬品添加逆洗方式による一般的なろ過膜の洗浄方法の一例の概略システム系統図。Schematic system diagram of an example of a general filtration membrane cleaning method by a conventional chemical addition backwashing system.

符号の説明Explanation of symbols

24:薬液注入ライン、24a:薬液注入配管、24b:傾斜開口部、24c,32:フランジ、30:逆洗ライン、30a:ポート、30b:縮流部、31:フランジ付ポート、33:リブ、41:開閉弁、42:絞り弁、50,50a,50b:継手(逆洗ライン側)、51:継手(薬液注入配管側)、52:水導入配管、60:穴、70:スリーブ、71:隙間、72:導入溝、73:連通溝、75:シール。   24: Chemical liquid injection line, 24a: Chemical liquid injection pipe, 24b: Inclined opening, 24c, 32: Flange, 30: Backwash line, 30a: Port, 30b: Constricted part, 31: Port with flange, 33: Rib, 41: Open / close valve, 42: Throttle valve, 50, 50a, 50b: Fitting (backwash line side), 51: Fitting (chemical solution injection pipe side), 52: Water introduction pipe, 60: Hole, 70: Sleeve, 71: Gap, 72: introduction groove, 73: communication groove, 75: seal.

Claims (8)

原水をろ過膜により浄化処理して処理水を得る水処理を対象とする薬液注入装置であって、前記水処理における原水またはろ過膜の洗浄用逆洗水が通流する主配管に設けた薬品注入用のポートに、薬品注入配管を開閉弁を介して挿入してなる水処理装置用の薬液注入装置において、
前記主配管の前記ポート部上流側と前記薬品注入配管の前記開閉弁下流側との間を、水導入配管により継手を介して接続してなる薬品注入配管内の洗浄手段を備えたことを特徴とする水処理装置用の薬液注入装置。
A chemical injection device for water treatment that purifies raw water with a filtration membrane to obtain treated water, and is provided in a main pipe through which the raw water in the water treatment or backwash water for washing the filtration membrane flows In the chemical injection device for the water treatment device, in which the chemical injection pipe is inserted into the injection port via the on-off valve,
A cleaning means in the chemical injection pipe is provided in which the upstream side of the port portion of the main pipe and the downstream side of the on-off valve of the chemical injection pipe are connected via a joint by a water introduction pipe. A chemical solution injection device for a water treatment device.
請求項1に記載の薬液注入装置において、前記主配管のポートを設ける部分には、前記主配管通流水の圧力低減用の縮流部を設けたことを特徴とする水処理装置用の薬液注入装置。 2. The chemical injection device for water treatment apparatus according to claim 1, wherein a contraction portion for reducing the pressure of the water flowing through the main pipe is provided in a portion where the port of the main pipe is provided. 3. apparatus. 請求項1または2に記載の薬液注入装置において、少なくとも前記薬品注入配管および薬品注入配管に設けた継手の材料を、前記薬品に対する耐腐食性材料としたことを特徴とする水処理装置用の薬液注入装置。 The chemical solution injection apparatus according to claim 1 or 2, wherein at least the chemical injection pipe and a joint material provided in the chemical injection pipe are made of a corrosion-resistant material against the chemical. Injection device. 請求項1に記載の薬液注入装置において、前記主配管に設けた継手は、主配管の水通流部に挿入され、通流水の動圧を受けて前記水導入配管内の薬品注入配管側への水の流れを促進する動圧受部を備えたことを特徴とする水処理装置用の薬液注入装置。 2. The chemical injection device according to claim 1, wherein the joint provided in the main pipe is inserted into a water flow portion of the main pipe and receives the dynamic pressure of the flow water to the chemical injection pipe side in the water introduction pipe. A chemical injection device for a water treatment apparatus, comprising a dynamic pressure receiving portion that promotes the flow of water. 請求項4に記載の薬液注入装置において、前記動圧受部は、前記継手の主配管の水通流部に挿入された管の先端部を斜めにカットした傾斜開口部を通流水の上流側に向けて配設したものとしたことを特徴とする水処理装置用の薬液注入装置。 The chemical injection device according to claim 4, wherein the dynamic pressure receiving portion is arranged on the upstream side of the flowing water through an inclined opening portion that is obliquely cut at a tip portion of a pipe inserted into a water flow portion of the main pipe of the joint. A chemical liquid injection device for a water treatment device, characterized in that the chemical solution injection device is directed toward the water treatment device. 請求項1に記載の薬液注入装置において、前記薬品注入配管内の洗浄手段は、請求項1に記載のものに代えて、薬品注入配管周縁部の圧力差を利用した自己洗浄手段とし、この自己洗浄手段は、前記薬品注入配管を前記主配管に設けたフランジ付ポート内に隙間を設けて液密的に挿入し、かつ、主配管の水通流部に挿入された薬品注入配管の先端部を斜めにカットした傾斜開口部を通流水の下流側に向けて配設し、さらに、前記フランジ付ポート内の隙間に対向して薬品注入配管の外周部に穴を備えたものとし、主配管の通流水が前記フランジ付ポート内の隙間と前記薬品注入配管の穴を経由して前記傾斜開口部から流出する構成を備えたものとしたことを特徴とする水処理装置用の薬液注入装置。 The chemical injection device according to claim 1, wherein the cleaning means in the chemical injection pipe is a self-cleaning means using a pressure difference in the peripheral portion of the chemical injection pipe, instead of the one in the first aspect. The cleaning means inserts the chemical injection pipe into the flanged port provided in the main pipe in a liquid-tight manner, and the tip of the chemical injection pipe inserted into the water flow portion of the main pipe An inclined opening that is cut obliquely is arranged toward the downstream side of the flowing water, and further, a hole is provided in the outer peripheral portion of the chemical injection pipe so as to face the gap in the flanged port. The chemical liquid injection device for a water treatment device is provided with a configuration in which the flow-through water flows out from the inclined opening through a gap in the flanged port and a hole in the chemical injection pipe. 請求項6に記載の薬液注入装置において、前記自己洗浄手段は、薬品注入配管を、前記主配管に設けたフランジ付ポート内に、スリーブを介して液密的に挿入してなり、前記スリーブの内周部には、薬品注入配管の軸方向に沿った逆洗水導入用の導入溝と前記穴への連通溝とを備えたものとし、主配管の通流水が前記導入溝および連通溝と前記薬品注入配管の穴を経由して前記傾斜開口部から流出する構成を備えたものとしたことを特徴とする水処理装置用の薬液注入装置。 The chemical injection device according to claim 6, wherein the self-cleaning means is configured to insert a chemical injection pipe into a flanged port provided in the main pipe in a liquid-tight manner via a sleeve. The inner peripheral portion is provided with an introduction groove for introducing backwash water along the axial direction of the chemical injection pipe and a communication groove to the hole, and the flow water of the main pipe is connected to the introduction groove and the communication groove. A chemical solution injection device for a water treatment device, characterized in that the chemical solution injection device is configured to flow out from the inclined opening through a hole of the chemical injection pipe. 原水を浄化処理して処理水を得るろ過膜と、前記処理水の一部を前記ろ過膜の逆洗水として用いてろ過膜の逆洗を行う逆洗ラインと、この逆洗ラインに薬品を添加して逆洗を行う薬品注入ラインとを備えた薬品添加逆洗方式の水処理装置用の薬液注入装置において、
前記薬品注入ラインは、薬品注入配管を前記逆洗ラインに設けた薬品注入用のポートに開閉弁を介して挿入してなり、かつ前記薬品注入配管内の洗浄手段を備えるものとし、この洗浄手段は、前記逆洗ラインの前記ポート部上流側と前記薬品注入配管の前記開閉弁下流側との間を、水導入配管により継手を介して接続したものとしたことを特徴とする水処理装置用の薬液注入装置。
A filtration membrane for purifying raw water to obtain treated water, a backwash line for backwashing the filtration membrane using a part of the treated water as backwash water for the filtration membrane, and chemicals in this backwash line In the chemical injection device for the water treatment device of the chemical addition backwashing method equipped with the chemical injection line for adding and backwashing,
The chemical injection line is formed by inserting a chemical injection pipe into a chemical injection port provided in the backwash line via an on-off valve, and includes a cleaning means in the chemical injection pipe. For the water treatment device, wherein the upstream side of the port part of the backwash line and the downstream side of the on-off valve of the chemical injection pipe are connected via a joint by a water introduction pipe. Chemical injection device.
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