JP2014050810A - Water treatment apparatus and operation method of water treatment apparatus - Google Patents

Water treatment apparatus and operation method of water treatment apparatus Download PDF

Info

Publication number
JP2014050810A
JP2014050810A JP2012197909A JP2012197909A JP2014050810A JP 2014050810 A JP2014050810 A JP 2014050810A JP 2012197909 A JP2012197909 A JP 2012197909A JP 2012197909 A JP2012197909 A JP 2012197909A JP 2014050810 A JP2014050810 A JP 2014050810A
Authority
JP
Japan
Prior art keywords
water
treated
treated water
raw
membrane
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2012197909A
Other languages
Japanese (ja)
Other versions
JP6141610B2 (en
Inventor
Tetsuo Namima
哲夫 浪間
Toshiyuki Fujioka
利幸 藤岡
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Kasei Chemicals Corp
Original Assignee
Asahi Kasei Chemicals Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Asahi Kasei Chemicals Corp filed Critical Asahi Kasei Chemicals Corp
Priority to JP2012197909A priority Critical patent/JP6141610B2/en
Publication of JP2014050810A publication Critical patent/JP2014050810A/en
Application granted granted Critical
Publication of JP6141610B2 publication Critical patent/JP6141610B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a water treatment apparatus and an operation method of the water treatment apparatus that when the water treatment apparatus with RO membrane is activated in emergency, time before providing treated water can be reduced, and degradation of the RO membrane in a stand-by state is prevented.SOLUTION: A water treatment apparatus 10 returns back both of treated water and concentrated water discharged from an RO membrane facility 16 to a raw water tank 11. The returned treated water and concentrated water are pooled in the raw water tank, the pooled water to be treated is pressurized by pressurize means, and the pressurized water to be treated is supplied to the RO membrane. The water treatment apparatus continues supplying the water to be treated to the RO membrane by circulate operation circulating the treated water and the concentrated water in a stand-by state where the treated water is not supplied to outside of the apparatus as drinking water.

Description

本発明は、原水を、RO膜を用いて処理する水処理装置、及び水処理装置の運転方法に関する。   The present invention relates to a water treatment apparatus that treats raw water using an RO membrane, and a method for operating the water treatment apparatus.

例えば地下水(原水)を、RO膜(Reverse Osmosis、逆浸透膜)を用いて処理することで、飲用水や雑用水を製造する水処理装置が知られている(例えば、特許文献1)。このような水処理装置は、取水した原水を、RO膜を用いて処理し、RO膜を透過した処理水を飲用水として配水する。また、RO膜を透過しなかった濃縮水は、一般的に廃棄されている。   For example, a water treatment apparatus for producing drinking water or miscellaneous water by treating groundwater (raw water) with an RO membrane (Reverse Osmosis, reverse osmosis membrane) is known (for example, Patent Document 1). Such a water treatment apparatus processes the raw | natural water taken using the RO membrane, and distributes the treated water which permeate | transmitted the RO membrane as drinking water. Further, the concentrated water that has not permeated the RO membrane is generally discarded.

特開2011−177653号公報JP 2011-177653 A

例えば、通常の上水道が使用できない非常時などにおいて、応急的に地下水を取水して、飲用水を得ることが求められている。しかしながら、従来の技術では、停止している水処理装置を、緊急で立ち上げるには時間を要していた。また、RO膜は乾燥や微生物の繁殖等に弱く、劣化の懸念がある為、不定期に利用される水処理装置に適用することが困難であり、応急対応の装置には不向きであった。   For example, in an emergency in which a normal water supply cannot be used, it is required to take groundwater in an emergency to obtain drinking water. However, in the prior art, it takes time to start up the water treatment apparatus that is stopped urgently. In addition, the RO membrane is vulnerable to drying, microbial growth, and the like, and there is a concern about deterioration. Therefore, it is difficult to apply the RO membrane to a water treatment device that is used irregularly, and is not suitable for an emergency response device.

そこで、RO膜を備えた水処理装置において、緊急で装置を立ち上げる際に、処理水を提供するまでの時間を短縮することが可能であり、待機状態におけるRO膜の劣化を抑制することが可能な水処理装置、及び水処理装置の運転方法を提供することを目的とする。   Therefore, in a water treatment device equipped with an RO membrane, when the device is urgently started up, it is possible to shorten the time until the treated water is provided, and to suppress degradation of the RO membrane in a standby state. It is an object of the present invention to provide a possible water treatment device and a method for operating the water treatment device.

本発明は、原水を貯留する原水槽と、原水槽に貯留された被処理水を昇圧する昇圧手段と、当該昇圧手段によって昇圧された被処理水を処理するRO膜と、当該RO膜を透過した処理水を貯留する処理水槽と、処理水を装置外へ給水する給水部と、処理水槽に貯留された処理水を原水槽へ返送可能な処理水返送手段と、RO膜を透過しなかった濃縮水(RO膜濃縮水)を原水槽へ返送可能な濃縮水返送手段と、を備える水処理装置を提供する。   The present invention relates to a raw water tank for storing raw water, a pressure increasing means for boosting the water to be treated stored in the raw water tank, an RO membrane for treating the water to be treated that has been pressurized by the pressure raising means, and the RO membrane. The treated water tank that stores the treated water, the water supply unit that supplies the treated water to the outside of the apparatus, the treated water return means that can return the treated water stored in the treated water tank to the raw water tank, and the RO membrane did not permeate There is provided a water treatment device comprising: concentrated water returning means capable of returning concentrated water (RO membrane concentrated water) to a raw water tank.

この水処理装置は、例えば飲用水を製造する場合には、原水を受入れて原水槽で貯留し、貯留された被処理水を昇圧手段によって昇圧し、昇圧された被処理水をRO膜によって処理することができる。水処理装置は、RO膜を透過した処理水を、飲用水として提供することができる。水処理装置は、例えば、非常時のみに飲用水を提供し、通常時は、飲用水を提供しない待機状態としてもよい。   For example, in the case of producing potable water, this water treatment apparatus receives raw water and stores it in a raw water tank, pressurizes the stored treated water by a boosting means, and treats the pressurized treated water with an RO membrane. can do. The water treatment apparatus can provide treated water that has passed through the RO membrane as drinking water. For example, the water treatment device may provide drinking water only in an emergency, and may be in a standby state in which drinking water is not provided during normal times.

この水処理装置は、処理水を処理水槽に貯留し、貯留された処理水を処理水返送手段によって原水槽へ返送すると共に、RO膜を透過しなかった濃縮水を、濃縮水返送手段によって原水槽へ返送することができる。水処理装置は、返送された処理水及び濃縮水を原水槽で貯留し、貯留された被処理水を昇圧手段によって昇圧し、昇圧された被処理水をRO膜へ供給することができる。水処理装置は、RO膜を透過した処理水と、RO膜を透過しなかった濃縮水との両方を、再び、原水槽へ戻すことができる。これにより、水処理装置は、処理水及び濃縮水を循環させる循環運転を行うことで、RO膜に被処理水を供給し続けることができる。水処理装置は、処理水を飲用水として装置外へ給水しない待機状態において、循環運転を行うことで、水処理装置の管路を清潔に保ち、さらにRO膜の劣化を防止することができる。   In this water treatment apparatus, treated water is stored in a treated water tank, and the stored treated water is returned to the raw water tank by the treated water returning means, and concentrated water that has not permeated the RO membrane is returned to the original by the concentrated water returning means. Can be returned to the aquarium. The water treatment apparatus can store the returned treated water and concentrated water in the raw water tank, pressurize the stored treated water by a pressure-increasing means, and supply the pressurized treated water to the RO membrane. The water treatment apparatus can return both the treated water that has passed through the RO membrane and the concentrated water that has not passed through the RO membrane to the raw water tank again. Thereby, the water treatment apparatus can continue supplying the water to be treated to the RO membrane by performing a circulation operation for circulating the treated water and the concentrated water. The water treatment device can keep the pipeline of the water treatment device clean and prevent deterioration of the RO membrane by performing a circulation operation in a standby state where the treated water is not supplied as drinking water to the outside of the device.

水処理装置は、昇圧手段の上流側に配置され、原水槽から供給された被処理水中の不純物を分離する濾過器と、処理水を濾過器に供給して、当該濾過器を逆流洗浄する逆洗手段と、を備える構成でもよい。これにより、処理水を利用して、濾過器を逆流洗浄することで、濾過器の機能を回復させることができる。   The water treatment device is disposed upstream of the pressure increasing means, and a filter that separates impurities in the water to be treated supplied from the raw water tank, and a reverse water supply that supplies the treated water to the filter and backwashes the filter. And a washing means. Thereby, the function of a filter can be recovered | restored by carrying out backwashing of a filter using treated water.

水処理装置は、処理水槽内に次亜塩素酸を注入する次亜塩素酸注入手段と、RO膜の上流側で、被処理水に還元剤を注入する還元剤注入手段と、を備える構成でもよい。これにより、原水槽へ返送される処理水に次亜塩素酸を注入することができ、装置内の殺菌を行うことができる。また、RO膜の上流側に還元剤を注入することができるので、被処理水中の次亜塩素酸を還元剤により還元した後に、被処理水中をRO膜に供給できる。従って、RO膜の次亜塩素酸による劣化を抑制することができる。   The water treatment apparatus may include a hypochlorous acid injecting means for injecting hypochlorous acid into the treated water tank, and a reducing agent injecting means for injecting a reducing agent into the water to be treated on the upstream side of the RO membrane. Good. Thereby, hypochlorous acid can be inject | poured into the treated water returned to a raw | natural water tank, and the inside of an apparatus can be sterilized. In addition, since the reducing agent can be injected upstream of the RO membrane, after the hypochlorous acid in the water to be treated is reduced by the reducing agent, the water to be treated can be supplied to the RO membrane. Therefore, the deterioration of the RO membrane due to hypochlorous acid can be suppressed.

水処理装置は、処理水槽内に次亜塩素酸を注入する次亜塩素酸注入手段と、昇圧手段の上流側で、被処理水に還元剤を注入する還元剤注入手段と、を備える構成でもよい。これにより、原水槽へ返送される処理水に次亜塩素酸を注入することができ、装置内の殺菌を行うことができる。また、昇圧手段の上流側に還元剤を注入することができるので、注入された還元剤は、昇圧手段によって拡散されて、被処理水中における次亜塩素酸を均一に還元することができる。従って、RO膜の次亜塩素酸による劣化をより好適に抑制することができる。   The water treatment apparatus may include a hypochlorous acid injection means for injecting hypochlorous acid into the treated water tank, and a reducing agent injection means for injecting a reducing agent into the water to be treated on the upstream side of the pressure raising means. Good. Thereby, hypochlorous acid can be inject | poured into the treated water returned to a raw | natural water tank, and the inside of an apparatus can be sterilized. In addition, since the reducing agent can be injected upstream of the pressurizing means, the injected reducing agent is diffused by the pressurizing means, and hypochlorous acid in the water to be treated can be uniformly reduced. Therefore, it is possible to more suitably suppress the deterioration of the RO membrane due to hypochlorous acid.

水処理装置は、被処理水の一部を分流し、分流された当該被処理水を流通させながら水質を検査する被処理水の水質センサを更に備え、当該水質センサによって検査された被処理水を原水槽に返送する構成でもよい。これにより、循環する水の流量を減らすことなく、水質の管理を行うことができる。また、水処理装置では、殆どの領域が水で満たされており、検査後の水を合流可能な場所が限られているが、内部が大気圧に近い原水槽に注入することで、検査後の水を廃棄することなく循環させることができる。   The water treatment device further includes a water quality sensor for water to be inspected by distributing a part of the water to be treated and inspecting the water quality while circulating the water to be treated, and the water to be treated inspected by the water quality sensor. The structure which returns to a raw | natural water tank may be sufficient. Thereby, water quality can be managed without reducing the flow rate of circulating water. In addition, in the water treatment device, most of the area is filled with water, and the place where the water after inspection can be merged is limited, but by injecting the water into the raw water tank close to atmospheric pressure, Water can be circulated without being discarded.

水処理装置は、処理水の一部を分流し、分流された当該処理水を流通させながら水質を検査する処理水の水質センサと、を更に備え、当該水質センサによって検査された処理水を処理水槽に返送する構成でもよい。これにより、循環する水の流量を減らすことなく、水質の管理を行うことができる。また、水処理装置では、殆どの領域が水で満たされており、検査後の水を合流可能な場所が限られているが、内部が大気圧に近い処理水槽に注入することで、検査後の水を廃棄することなく循環させることができる。   The water treatment apparatus further includes a treated water quality sensor that divides a part of the treated water and inspects the water quality while distributing the separated treated water, and treats the treated water inspected by the water quality sensor. The structure which returns to a water tank may be sufficient. Thereby, water quality can be managed without reducing the flow rate of circulating water. In addition, in the water treatment device, most of the area is filled with water, and the place where the water after inspection can be merged is limited. However, by injecting the water into the treatment water tank close to atmospheric pressure, Water can be circulated without being discarded.

水処理装置は、昇圧手段の上流側に配置され、原水槽から供給された被処理水中の不純物を分離する濾過器を、砂濾過装置及び/又は膜濾過装置とする構成でもよい。これにより、RO膜に供給する被処理水から不純物を好適に除去することができる。   The water treatment device may be configured such that the filter disposed on the upstream side of the pressurizing unit and separating impurities in the for-treatment water supplied from the raw water tank is a sand filtration device and / or a membrane filtration device. Thereby, impurities can be suitably removed from the water to be treated supplied to the RO membrane.

水処理装置は、原水槽に供給される原水に次亜塩素酸を注入する第二の次亜塩素酸注入手段を備える構成でもよい。これにより、原水を殺菌した上で原水槽に供給することができるため、水処理装置の管路をより清潔に保つことができる。 The water treatment apparatus may include a second hypochlorous acid injection unit that injects hypochlorous acid into the raw water supplied to the raw water tank. Thereby, since it can supply to a raw | natural water tank after sterilizing raw | natural water, the pipe line of a water treatment apparatus can be kept cleaner.

本発明は、原水を原水槽に受入れて貯留し、原水槽に貯留された被処理水を、RO膜を用いて処理し、RO膜を透過した処理水を装置外へ給水可能な水処理装置の運転方法において、原水槽に貯留された被処理水を昇圧する昇圧工程と、昇圧工程で昇圧された被処理水を、RO膜を用いて処理する逆浸透膜処理工程と、RO膜を透過した処理水を前記原水槽へ返送する処理水返送工程と、RO膜濃縮水を原水槽へ返送する濃縮水返送工程と、を備える水処理装置の運転方法を提供する。   The present invention is a water treatment device that receives raw water in a raw water tank and stores it, treats water to be treated stored in the raw water tank using an RO membrane, and supplies the treated water that has passed through the RO membrane to the outside of the device. In the above operation method, the pressurizing step for boosting the water to be treated stored in the raw water tank, the reverse osmosis membrane treatment step for treating the water to be treated in the pressure boosting step using the RO membrane, and the permeation through the RO membrane A method of operating a water treatment apparatus comprising: a treated water returning step for returning the treated water to the raw water tank; and a concentrated water returning step for returning the RO membrane concentrated water to the raw water tank is provided.

本発明の水処理装置の運転方法では、原水槽で貯留された被処理水を昇圧し、昇圧された被処理水をRO膜によって処理する。この運転方法では、RO膜を透過した処理水が、原水槽に返送されると共に、RO膜を透過しなかった濃縮水も、原水槽に返送される。返送された処理水及び濃縮水は、原水槽で貯留され、再び昇圧されてRO膜に供給される。水処理装置の運転方法では、RO膜を透過した処理水と、RO膜を透過しなかった濃縮水との両方を、原水槽へ戻すことができる。これにより、処理水及び濃縮水を循環させる循環運転を行うことで、RO膜に被処理水を供給し続けることができる。水処理装置の運転方法では、処理水を飲用水として装置外へ給水しない待機状態において、循環運転を行うことで、RO膜の劣化を防止することができる。   In the operation method of the water treatment apparatus of the present invention, the water to be treated stored in the raw water tank is pressurized, and the pressurized water to be treated is treated with the RO membrane. In this operation method, treated water that has passed through the RO membrane is returned to the raw water tank, and concentrated water that has not passed through the RO membrane is also returned to the raw water tank. The treated water and concentrated water that have been returned are stored in the raw water tank, pressurized again, and supplied to the RO membrane. In the operation method of the water treatment apparatus, both the treated water that has permeated the RO membrane and the concentrated water that has not permeated the RO membrane can be returned to the raw water tank. Thereby, the to-be-processed water can be continuously supplied to RO membrane by performing the circulating operation which circulates treated water and concentrated water. In the operation method of the water treatment apparatus, the RO membrane can be prevented from deteriorating by performing the circulation operation in a standby state where the treated water is not supplied as drinking water to the outside of the apparatus.

処理水返送工程では、処理水に次亜塩素酸を注入し、次亜塩素酸が注入された処理水を返送し、被処理水をRO膜に供給する前に被処理水に還元剤を注入してもよい。これにより、原水槽へ返送される処理水に次亜塩素酸を注入することができ、装置内の殺菌を行うことができる。また、被処理水は、注入された還元剤により次亜塩素酸を還元された後に、RO膜へ供給されるので、RO膜の次亜塩素酸による劣化が好適に抑制される。   In the treated water return process, hypochlorous acid is injected into the treated water, the treated water into which hypochlorous acid has been injected is returned, and a reducing agent is injected into the treated water before supplying the treated water to the RO membrane. May be. Thereby, hypochlorous acid can be inject | poured into the treated water returned to a raw | natural water tank, and the inside of an apparatus can be sterilized. In addition, since the water to be treated is supplied to the RO membrane after hypochlorous acid is reduced by the injected reducing agent, deterioration of the RO membrane due to hypochlorous acid is suitably suppressed.

処理水返送工程では、処理水に次亜塩素酸を注入し、次亜塩素酸が注入された処理水を返送し、原水槽に貯留された被処理水を昇圧する前に被処理水に還元剤を注入してもよい。これにより、原水槽へ返送される処理水に次亜塩素酸を注入することができ、装置内の殺菌を行うことができる。また、注入された還元剤は、昇圧工程によって拡散されるので、被処理水中の次亜塩素酸は還元剤により均一に還元される。還元剤により次亜塩素酸を均一に還元した被処理水がRO膜に供給されるので、RO膜の次亜塩素酸による劣化がさらに好適に抑制される。   In the treated water return process, hypochlorous acid is injected into the treated water, the treated water into which hypochlorous acid has been injected is returned, and the treated water stored in the raw water tank is reduced to the treated water before being pressurized. An agent may be injected. Thereby, hypochlorous acid can be inject | poured into the treated water returned to a raw | natural water tank, and the inside of an apparatus can be sterilized. Further, since the injected reducing agent is diffused by the pressurizing step, hypochlorous acid in the for-treatment water is uniformly reduced by the reducing agent. Since the treated water in which hypochlorous acid is uniformly reduced by the reducing agent is supplied to the RO membrane, the deterioration of the RO membrane due to hypochlorous acid is further suitably suppressed.

水処理装置の運転方法は、昇圧工程の前に実行され、被処理水中の不純物を分離する濾過工程を更に備えていてもよい。これにより、昇圧工程及び逆浸透膜処理工程の前段において、被処理水中の不純物を分離することができる。   The operation method of the water treatment apparatus may further include a filtration step that is performed before the pressure increasing step and separates impurities in the water to be treated. Thereby, the impurities in to-be-processed water can be isolate | separated in the front | former stage of a pressure | voltage rise process and a reverse osmosis membrane process.

水処理装置の運転方法は、処理水返送工程による処理水の原水槽への返送を停止し、処理水を濾過工程で使用された濾過器に供給して、当該濾過器の逆流洗浄を行う逆洗工程を更に備えていてもよい。これにより、処理水を利用して、濾過器を逆流洗浄することで、濾過器の機能を回復させることができる。   The operation method of the water treatment device is to reverse the treated water returning process to the raw water tank, supply the treated water to the filter used in the filtration process, and perform reverse flow cleaning of the filter. You may further provide the washing process. Thereby, the function of a filter can be recovered | restored by carrying out backwashing of a filter using treated water.

水処理装置の運転方法は、被処理水の一部を分流し、分流された当該被処理水を流通させながら水質を検査し、検査された被処理水を原水槽に返送する被処理水の水質検査工程を更に備えていてもよい。これにより、循環する水の流量を減らすことなく、水質の管理を行うことができる。また、水処理装置では、殆どの領域が水で満たされており、検査後の水を合流可能な場所が限られているが、内部が大気圧に近い原水槽に注入することで、検査後の水を廃棄することなく循環させることができる。   The operation method of the water treatment apparatus is to divide a part of the treated water, inspect the water quality while circulating the separated treated water, and return the treated water to the raw water tank. A water quality inspection process may be further provided. Thereby, water quality can be managed without reducing the flow rate of circulating water. In addition, in the water treatment device, most of the area is filled with water, and the place where the water after inspection can be merged is limited, but by injecting the water into the raw water tank close to atmospheric pressure, Water can be circulated without being discarded.

水処理装置の運転方法は、処理水の一部を分流し、分流された当該処理水を流通させながら水質を検査し、検査された処理水を処理水槽に返送する処理水の水質検査工程を更に備えていてもよい。これにより、循環する水の流量を減らすことなく、水質の管理を行うことができる。また、水処理装置では、殆どの領域が水で満たされており、検査後の水を合流可能な場所が限られているが、内部が大気圧に近い処理水槽に注入することで、検査後の水を廃棄することなく循環させることができる。   The operation method of the water treatment apparatus is a process of water quality inspection for distributing a part of the treated water, inspecting the water quality while distributing the separated treated water, and returning the inspected treated water to the treated water tank. Furthermore, you may provide. Thereby, water quality can be managed without reducing the flow rate of circulating water. In addition, in the water treatment device, most of the area is filled with water, and the place where the water after inspection can be merged is limited. However, by injecting the water into the treatment water tank close to atmospheric pressure, Water can be circulated without being discarded.

水処理装置の運転方法は、処理水返送工程による処理水の返送を停止すると共に、濃縮水返送工程による濃縮水の返送を停止し、処理水及び濃縮水を装置外へ排出せずに、原水の原水槽への受入れを開始し、昇圧工程及び逆浸透膜処理工程を実行し当該逆浸透膜処理工程で処理された処理水を装置外へ給水することができる。これにより、非常時に処理水を飲用水として直ちに供給することができる。   The operation method of the water treatment equipment is to stop the return of treated water in the treated water return process, stop the return of concentrated water in the concentrated water return process, and discharge raw water without discharging treated water and concentrated water outside the equipment. The raw water tank is started to be received, the pressure increasing step and the reverse osmosis membrane treatment step are executed, and the treated water treated in the reverse osmosis membrane treatment step can be supplied to the outside of the apparatus. Thereby, treated water can be immediately supplied as drinking water in an emergency.

水処理装置の運転方法は、処理水返送工程による処理水の返送を停止すると共に、濃縮水返送工程による濃縮水の返送を停止し、処理水及び濃縮水を装置外へ排出した後又は排出と同時に、原水の原水槽への受入れを開始し、昇圧工程及び逆浸透膜処理工程を実行し当該逆浸透膜処理工程で処理された処理水を装置外へ給水することができる。処理水を装置外へ給水する前に水処理装置内の処理水及び濃縮水を排水した後又は排水と同時に、新たな原水を受入れて飲用水の製造を行うことができる。これにより、飲用水の利用者に安心感を与えることができる。   The operation method of the water treatment apparatus is to stop returning the treated water in the treated water returning process, stop returning the concentrated water in the concentrated water returning process, and discharge or discharge the treated water and the concentrated water to the outside of the apparatus. At the same time, it is possible to start receiving raw water into the raw water tank, execute the pressurization step and the reverse osmosis membrane treatment step, and supply the treated water treated in the reverse osmosis membrane treatment step to the outside of the apparatus. Before the treated water is supplied to the outside of the apparatus, after the treated water and concentrated water in the water treatment apparatus are drained or simultaneously with the drainage, new raw water can be received to produce potable water. Thereby, a sense of security can be given to the user of drinking water.

本発明の水処理装置及び水処理装置の運転方法によれば、待機状態におけるRO膜の劣化を抑制しつつ、緊急で装置を立ち上げる際に、処理水を提供するまでの時間を短縮することができる。   According to the water treatment apparatus and the water treatment apparatus operating method of the present invention, it is possible to shorten the time until the treated water is provided when the apparatus is started up urgently while suppressing the deterioration of the RO membrane in the standby state. Can do.

本発明の実施形態に係る水処理装置を示す概略構成図である。It is a schematic block diagram which shows the water treatment apparatus which concerns on embodiment of this invention. 水質センサ回りの配管の接続を示す概略構成図である。It is a schematic block diagram which shows the connection of piping around a water quality sensor. 本発明の実施形態に係る水処理装置の運転方法の手順を示す工程図である。It is process drawing which shows the procedure of the operating method of the water treatment apparatus which concerns on embodiment of this invention. スタートアップ工程における手順を示す工程図である。It is process drawing which shows the procedure in a startup process. 循環運転工程における手順を示す工程図である。It is process drawing which shows the procedure in a circulating operation process.

以下、本発明による水処理装置及び水処理装置の運転方法の好適な実施形態について図面を参照しながら説明する。なお、図面の説明において同一または相当要素には同一の符号を付し、重複する説明は省略する。   Hereinafter, preferred embodiments of a water treatment apparatus and a water treatment apparatus operating method according to the present invention will be described with reference to the drawings. In the description of the drawings, the same or corresponding elements are denoted by the same reference numerals, and redundant description is omitted.

図1に示す水処理装置10は、例えば非常時において、原水に逆浸透膜処理を施すことで飲用水を製造することができる装置である。水処理装置10は、通常時は、待機状態とし、非常時のみ飲用水を製造することとしてもよい。原水として、例えば地下水、貯水池に貯留された水などを使用することができる。   A water treatment device 10 shown in FIG. 1 is a device that can produce drinking water by applying a reverse osmosis membrane treatment to raw water in an emergency, for example. The water treatment apparatus 10 may be in a standby state during normal times and produce potable water only in an emergency. As raw water, for example, groundwater, water stored in a reservoir, or the like can be used.

水処理装置10は、取得した原水を貯留可能な原水槽11を備えている。原水槽11は、水を貯留可能な容器である。原水槽11には、例えば、通気管が接続され、内部は大気圧に維持されている。   The water treatment apparatus 10 includes a raw water tank 11 that can store the acquired raw water. The raw water tank 11 is a container capable of storing water. For example, a vent pipe is connected to the raw water tank 11, and the inside is maintained at atmospheric pressure.

原水槽11は、原水を受け入れるための取水配管21が接続されている。原水は、取水配管21を通り、原水槽11内に供給される。取水配管21には、原水の受入れを停止可能な開閉弁41が設けられている。開閉弁41(流量調整部)が閉止されることで、原水の受入れが停止される。   The raw water tank 11 is connected to a water intake pipe 21 for receiving raw water. The raw water passes through the intake pipe 21 and is supplied into the raw water tank 11. The intake pipe 21 is provided with an on-off valve 41 that can stop receiving raw water. By closing the on-off valve 41 (flow rate adjusting unit), the acceptance of raw water is stopped.

水処理装置10は、原水槽11内に次亜塩素酸を注入可能な注入管22(第2の次亜塩素酸注入手段)を有する。次亜塩素酸の注入管22は、取水配管21に接続されていてもよく、原水槽11に接続されていてもよい。   The water treatment apparatus 10 has an injection pipe 22 (second hypochlorous acid injection means) capable of injecting hypochlorous acid into the raw water tank 11. The hypochlorous acid injection pipe 22 may be connected to the intake pipe 21 or may be connected to the raw water tank 11.

原水槽11は、配管23を介して、砂ろ過器12(濾過器)に接続されている。配管23には、砂ろ過器12に供給される被処理水を送水するためのポンプ13が接続されている。被処理水は、原水槽11に貯留されていた水である。原水槽11に貯留された被処理水は、ポンプ13によって送水されて砂ろ過器12に供給される。   The raw water tank 11 is connected to a sand filter 12 (filter) via a pipe 23. A pump 13 for feeding the water to be treated supplied to the sand filter 12 is connected to the pipe 23. The treated water is water stored in the raw water tank 11. The treated water stored in the raw water tank 11 is fed by the pump 13 and supplied to the sand filter 12.

砂ろ過器12は、被処理水中の固形物(不純物)を取り除くものである。砂ろ過器12は、濾材としての砂を容器内に収容している。被処理水は、砂ろ過器12の上部側から供給され、砂層を通過し、所定の大きさの固形物が取り除かれて、下部側から排出される。水処理装置10は、砂ろ過器12に代えて、その他の濾過器(膜濾過装置)を備える構成でもよい。その他の濾過器としては、MF膜(Microfiltration)、UF膜(Ultra filtration)等が挙げられる。   The sand filter 12 removes solids (impurities) in the water to be treated. The sand filter 12 accommodates sand as a filter medium in a container. The water to be treated is supplied from the upper side of the sand filter 12, passes through the sand layer, solids of a predetermined size are removed, and the water is discharged from the lower side. The water treatment device 10 may be configured to include other filter (membrane filter device) instead of the sand filter 12. Examples of other filter include MF membrane (Microfiltration), UF membrane (Ultra filtration) and the like.

砂ろ過器12の下部側には、固形物が取り除かれた被処理水が送水される配管24が接続されている。砂ろ過器12は、配管24を介して、プレフィルタ14に接続されている。砂ろ過器12を通過した被処理水は、配管24内を流通し、プレフィルタ14に供給される。プレフィルタ14は、砂ろ過器12の砂が流出した場合に、被処理水中に含まれる砂を除去する。プレフィルタ14は、砂を除去可能な濾材を容器内に有する。   A pipe 24 is connected to the lower side of the sand filter 12 to which the water to be treated from which the solid matter has been removed is sent. The sand filter 12 is connected to the prefilter 14 via a pipe 24. The water to be treated that has passed through the sand filter 12 circulates in the pipe 24 and is supplied to the prefilter 14. The prefilter 14 removes the sand contained in the water to be treated when the sand of the sand filter 12 flows out. The prefilter 14 has a filter medium capable of removing sand in the container.

プレフィルタ14には、プレフィルタ14内を通過した被処理水を送水する配管25が接続されている。プレフィルタ14は、配管25を介して混合器15に接続されている。プレフィルタ14を通過した被処理水は、配管25内を流通し、混合器15に供給される。   The pre-filter 14 is connected to a pipe 25 that feeds the water to be treated that has passed through the pre-filter 14. The prefilter 14 is connected to the mixer 15 via a pipe 25. The water to be treated that has passed through the prefilter 14 flows through the pipe 25 and is supplied to the mixer 15.

配管25には、還元剤を注入可能な注入管26(還元剤注入手段)が接続されている。還元剤は、被処理水中に含まれる次亜塩素酸を中和するものである。還元剤としては、SBS(NaHSO3、重亜硫酸ソーダ)を用いることができる。 An injection pipe 26 (reducing agent injection means) that can inject a reducing agent is connected to the pipe 25. The reducing agent neutralizes hypochlorous acid contained in the water to be treated. As the reducing agent, SBS (NaHSO 3 , sodium bisulfite) can be used.

また、配管25には、分散剤を注入可能な注入管27(分散剤注入手段)が接続されている。分散剤は、RO膜でのカルシウムの析出、シリカの析出を抑えるために注入されている。注入管27は、例えば、注入管26の下流側に設けられている。   Further, an injection pipe 27 (dispersant injection means) capable of injecting a dispersant is connected to the pipe 25. The dispersant is injected in order to suppress calcium precipitation and silica precipitation on the RO membrane. The injection tube 27 is provided on the downstream side of the injection tube 26, for example.

混合器15は、被処理水を混合するものであり、被処理水中に含まれる還元剤及び分散剤が拡散されて、濃度の均一化が図られる。   The mixer 15 mixes the water to be treated, and the reducing agent and the dispersant contained in the water to be treated are diffused to make the concentration uniform.

混合器15には、混合器15内を通過した被処理水を送水する配管28が接続されている。混合器15は、配管28を介してRO膜設備16に接続されている。混合器15から排出された被処理水は、配管28に接続された高圧ポンプ17(昇圧手段)によって昇圧されてRO膜設備16に供給される。高圧ポンプ17は、被処理水を浸透圧よりも大きな圧力まで昇圧する。   A pipe 28 is connected to the mixer 15 for feeding the water to be treated that has passed through the mixer 15. The mixer 15 is connected to the RO membrane facility 16 via a pipe 28. The water to be treated discharged from the mixer 15 is pressurized by the high-pressure pump 17 (pressure increase means) connected to the pipe 28 and supplied to the RO membrane facility 16. The high pressure pump 17 raises the water to be treated to a pressure larger than the osmotic pressure.

RO膜設備16は、被処理水を逆浸透膜処理するものであり、容器内にRO膜を備えている。RO膜設備16は、RO膜を透過した処理水と、RO膜を透過しなかった濃縮水(RO膜濃縮水)とに分けられる。水処理装置10は、複数のRO膜設備16を備え、上流側のRO膜設備16から送水された濃縮水を下流側のRO膜設備16に供給してもよい。   The RO membrane facility 16 performs reverse osmosis membrane treatment of water to be treated, and includes an RO membrane in the container. The RO membrane facility 16 is divided into treated water that has permeated through the RO membrane and concentrated water that has not permeated through the RO membrane (RO membrane concentrated water). The water treatment apparatus 10 may include a plurality of RO membrane facilities 16 and supply the concentrated water sent from the upstream RO membrane facility 16 to the downstream RO membrane facility 16.

RO膜設備16には、処理水が送水される配管29が接続されている。RO膜設備16は、配管29を介して処理水槽18に接続されている。RO膜設備16から送水された処理水は、配管29内を流通し、処理水槽18に供給される。   A piping 29 through which treated water is sent is connected to the RO membrane facility 16. The RO membrane facility 16 is connected to the treated water tank 18 via a pipe 29. The treated water sent from the RO membrane facility 16 circulates in the pipe 29 and is supplied to the treated water tank 18.

RO膜設備16には、濃縮水が送水される配管30が接続されている。配管30は、水処理装置10の下水配管31に接続されている。下水配管31は、水処理装置10から排出される水(不要な水)を装置10外へ排出する配管である。配管30と下水配管31と間には、開閉弁42が設けられている。濃縮水を装置10外へ排水しない場合には、開閉弁42が閉じられている。   A piping 30 through which concentrated water is fed is connected to the RO membrane facility 16. The pipe 30 is connected to the sewage pipe 31 of the water treatment apparatus 10. The sewage pipe 31 is a pipe that discharges water (unnecessary water) discharged from the water treatment apparatus 10 to the outside of the apparatus 10. An open / close valve 42 is provided between the pipe 30 and the sewage pipe 31. When the concentrated water is not drained out of the apparatus 10, the on-off valve 42 is closed.

処理水槽18は、処理水を貯留可能な容器である。処理水槽18には、例えば、通気管が接続され、内部は大気圧に維持されている。   The treated water tank 18 is a container capable of storing treated water. For example, a vent pipe is connected to the treated water tank 18, and the inside is maintained at atmospheric pressure.

処理水槽18には、処理水槽18に貯留された処理水が送水される配管32が接続されている。配管32は、装置10外の受水槽に接続されている。例えば、処理水を飲用水として提供する場合には、処理水槽18に貯留された処理水は、装置10外の受水槽に供給される。配管32には、処理水を送水するための送水ポンプ19が接続されている。   A pipe 32 through which treated water stored in the treated water tank 18 is fed is connected to the treated water tank 18. The pipe 32 is connected to a water receiving tank outside the apparatus 10. For example, when providing treated water as drinking water, the treated water stored in the treated water tank 18 is supplied to a water receiving tank outside the apparatus 10. A water supply pump 19 for supplying treated water is connected to the pipe 32.

また、配管32には、開閉弁43(給水量調節部)が設けられている。処理水を飲用水として提供する場合には、開閉弁43が開放されて、処理水は配管32を通り、装置10外の受水槽に供給される。開閉弁43の弁の開度を調節することで、装置10外への飲用水の給水量を調整することができる。   In addition, the pipe 32 is provided with an on-off valve 43 (water supply amount adjusting unit). When the treated water is provided as drinking water, the on-off valve 43 is opened, and the treated water passes through the pipe 32 and is supplied to the water receiving tank outside the apparatus 10. By adjusting the opening of the on-off valve 43, the amount of drinking water supplied to the outside of the apparatus 10 can be adjusted.

ここで、本実施形態の水処理装置10は、処理水槽18に貯留された処理水を原水槽11へ返送する処理水返送手段50と、RO膜設備16から排出された濃縮水を原水槽11へ返送する濃縮水返送手段60とを備えている。水処理装置10は、処理水及び濃縮水を原水槽11へ返送することができ、原水槽11に返送され水を再度、RO膜設備16に供給し、処理水及び濃縮水を循環させる循環運転を実行することができる。すなわち、水処理装置10は、飲用水を製造しない待機状態において、循環運転を実行することができる。   Here, the water treatment apparatus 10 of the present embodiment has a treated water returning means 50 that returns treated water stored in the treated water tank 18 to the raw water tank 11 and concentrated water discharged from the RO membrane facility 16. And a concentrated water returning means 60 for returning to the home. The water treatment apparatus 10 can return the treated water and the concentrated water to the raw water tank 11, and returns the raw water tank 11 to the RO membrane facility 16 again to circulate the treated water and the concentrated water. Can be executed. That is, the water treatment apparatus 10 can perform the circulating operation in a standby state where no potable water is produced.

処理水返送手段50は、配管32から分岐された処理水返送配管51を有する。処理水槽18は、配管32及び処理水返送配管51を介して、原水槽11に接続されている。配管32と処理水返送配管51との間には、開閉弁44が設けられている。開閉弁44が開放され、開閉弁43が閉じられた状態において、処理水槽18から原水槽11へ、処理水が返送される。処理水槽18に貯留された処理水は、送水ポンプ19によって送水され、配管32及び処理水返送配管51を通り、原水槽11へ供給される。   The treated water return means 50 has a treated water return pipe 51 branched from the pipe 32. The treated water tank 18 is connected to the raw water tank 11 via a pipe 32 and a treated water return pipe 51. An open / close valve 44 is provided between the pipe 32 and the treated water return pipe 51. In a state where the on-off valve 44 is opened and the on-off valve 43 is closed, the treated water is returned from the treated water tank 18 to the raw water tank 11. The treated water stored in the treated water tank 18 is fed by the water pump 19, passes through the pipe 32 and the treated water return pipe 51, and is supplied to the raw water tank 11.

濃縮水返送手段60は、配管30から分岐された濃縮水返送配管61を有する。RO膜設備16の濃縮水の出口は、配管30及び濃縮水返送配管61を介して、原水槽11に接続されている。配管30と濃縮水返送配管61との間には、開閉弁45が設けられている。開閉弁45が開放され、開閉弁42が閉じられた状態において、RO膜設備16から原水槽11へ濃縮水が返送される。RO膜設備16から排出された濃縮水は、配管30及び濃縮水返送配管61を通り、原水槽11へ供給される。水処理装置10は、例えば、濃縮水を貯留可能な貯留槽を備えている構成でもよい。RO膜設備16から排出された濃縮水を貯留した後に、原水槽11へ送水してもよい。   The concentrated water return means 60 has a concentrated water return pipe 61 branched from the pipe 30. The outlet of the concentrated water of the RO membrane facility 16 is connected to the raw water tank 11 through the pipe 30 and the concentrated water return pipe 61. An open / close valve 45 is provided between the pipe 30 and the concentrated water return pipe 61. In a state where the on-off valve 45 is opened and the on-off valve 42 is closed, the concentrated water is returned from the RO membrane facility 16 to the raw water tank 11. The concentrated water discharged from the RO membrane facility 16 is supplied to the raw water tank 11 through the pipe 30 and the concentrated water return pipe 61. The water treatment apparatus 10 may have a configuration including a storage tank capable of storing concentrated water, for example. After the concentrated water discharged from the RO membrane facility 16 is stored, the raw water tank 11 may be supplied with water.

また、水処理装置10は、処理水槽18内に次亜塩素酸を注入可能な注入管33(次亜塩素酸注入手段)を有する。次亜塩素酸を処理水槽18内に供給することで、処理水返送配管51内を流れる処理水を消毒することができる。水処理装置10を循環する処理水の水質を維持することができる。   Further, the water treatment apparatus 10 has an injection pipe 33 (hypochlorous acid injection means) capable of injecting hypochlorous acid into the treated water tank 18. By supplying hypochlorous acid into the treated water tank 18, the treated water flowing in the treated water return pipe 51 can be disinfected. The quality of the treated water circulating through the water treatment apparatus 10 can be maintained.

水処理装置10は、処理水を砂ろ過器12に供給して、砂ろ過器12の逆流洗浄を行う逆流洗浄手段70を備えていてもよい。逆流洗浄手段70は、処理水返送配管51から分岐された逆洗用配管71を有する。処理水槽18は、配管32、処理水返送配管及び逆洗用配管71を介して、砂ろ過器12の出口側12bに接続されている。逆洗用配管71は、砂ろ過器12の出口側12bに接続された、配管24に接続されている。   The water treatment apparatus 10 may include backflow cleaning means 70 that supplies treated water to the sand filter 12 and performs backflow cleaning of the sand filter 12. The backwashing means 70 has a backwash pipe 71 branched from the treated water return pipe 51. The treated water tank 18 is connected to the outlet side 12 b of the sand filter 12 through a pipe 32, a treated water return pipe and a backwash pipe 71. The backwash pipe 71 is connected to the pipe 24 connected to the outlet side 12 b of the sand filter 12.

配管24には、開閉弁46が設けられている。逆洗用配管71は、開閉弁46よりも砂ろ過器12側に接続されている。また、逆洗用配管71には、開閉弁47が設けられている。処理水返送配管51には、逆洗用配管71との分岐点より下流側(原水槽11側)に開閉弁48が設けられている。開閉弁47が開放され、開閉弁46,48が閉じられた状態において、処理水が処理水返送配管51から砂ろ過器12の出口側12bに供給される。   The pipe 24 is provided with an open / close valve 46. The backwash pipe 71 is connected to the sand filter 12 side from the on-off valve 46. The backwash pipe 71 is provided with an on-off valve 47. The treated water return pipe 51 is provided with an open / close valve 48 on the downstream side (raw water tank 11 side) from the branch point with the backwash pipe 71. In a state where the on-off valve 47 is opened and the on-off valves 46 and 48 are closed, treated water is supplied from the treated water return pipe 51 to the outlet side 12 b of the sand filter 12.

砂ろ過器12の入口側12aは、配管23から分岐された下水配管31に接続されている。下水配管31には、開閉弁49が設けられている。また、配管23には、下水配管31との分岐点より上流側(送水ポンプ13と砂ろ過器12との間)に逆止弁が設けられている。逆止弁は、砂ろ過器12側から送水ポンプ13側への水の流入を防止する。開閉弁49が開放された状態において、砂ろ過器12の入口側12aから排水された洗浄後の水が、下水配管31を通り、装置10外へ廃棄される。   The inlet side 12 a of the sand filter 12 is connected to a sewage pipe 31 branched from the pipe 23. An open / close valve 49 is provided in the sewage pipe 31. The pipe 23 is provided with a check valve upstream of the branch point with the sewage pipe 31 (between the water pump 13 and the sand filter 12). The check valve prevents inflow of water from the sand filter 12 side to the water pump 13 side. In the state where the on-off valve 49 is opened, the washed water drained from the inlet side 12 a of the sand filter 12 passes through the sewage pipe 31 and is discarded outside the apparatus 10.

砂ろ過器12の出口側12bに処理水を供給して逆流洗浄を行うことにより、砂ろ過器12の砂がまき上がり、砂上に堆積していた固形物、砂に付着していた固形物などが、水流によって取り除かれる。固形物を含む排水は、砂ろ過器12の入口側12から排出される。これにより、砂ろ過器12の機能を回復させることができる。   By supplying the treated water to the outlet side 12b of the sand filter 12 and performing back-flow cleaning, the sand of the sand filter 12 is rolled up, and solids deposited on the sand, solids attached to the sand, etc. Is removed by the water stream. Waste water containing solid matter is discharged from the inlet side 12 of the sand filter 12. Thereby, the function of the sand filter 12 can be recovered.

次に、図2を参照して、水処理装置10の水質センサについて説明する。水処理装置10は、被処理水の水質を検査する水質センサ81、及び処理水の水質を検査する水質センサ82を備えている。図2では、処理水槽18に貯留された処理水を検査する場合について示している。なお、原水槽11に貯留された被処理水を検査する場合も同様の構成であるため、図2では、被処理水を検査する場合の構成については、括弧内に符号を付している。   Next, the water quality sensor of the water treatment apparatus 10 will be described with reference to FIG. The water treatment apparatus 10 includes a water quality sensor 81 that inspects the quality of the water to be treated and a water quality sensor 82 that inspects the quality of the treated water. FIG. 2 shows a case where the treated water stored in the treated water tank 18 is inspected. In addition, since it is the same structure also when inspecting the to-be-processed water stored in the raw | natural water tank 11, in FIG. 2, the code | symbol is attached | subjected about the structure in the case of inspecting to-be-processed water.

処理水の水質センサ82に供給される処理水は、配管32から分岐された配管83を通り、水質センサ82に供給される。配管83には、送水ポンプ84が接続されている。処理水槽18に貯留された処理水は、配管32を通り、処理水の一部が分流されて配管83内に流入する。分流された処理水は、送水ポンプ84によって送水されて水質センサ82に供給される。   The treated water supplied to the treated water quality sensor 82 passes through the pipe 83 branched from the pipe 32 and is supplied to the water quality sensor 82. A water supply pump 84 is connected to the pipe 83. The treated water stored in the treated water tank 18 passes through the pipe 32, and a part of the treated water is divided and flows into the pipe 83. The separated treated water is fed by the water feed pump 84 and supplied to the water quality sensor 82.

水質センサ82には、検査後の処理水を送水する配管85が接続されている。水質センサ82は、配管85を介して処理水槽18に接続されている。検査後の処理水は、配管85を通り、処理水槽18へ戻される。これにより、検査後の処理水を廃棄することなく、処理水槽18に戻すことができる。そのため、新たな原水を受入れることなく、循環運転による流量を維持することができる。   The water quality sensor 82 is connected to a pipe 85 for supplying treated water after inspection. The water quality sensor 82 is connected to the treated water tank 18 through a pipe 85. The treated water after the inspection passes through the pipe 85 and is returned to the treated water tank 18. Thereby, the treated water after the inspection can be returned to the treated water tank 18 without being discarded. Therefore, the flow rate by the circulation operation can be maintained without receiving new raw water.

被処理水の水質センサ81に供給される処理水は、配管23から分岐された配管83を通り、水質センサ81に供給される。配管83には、送水ポンプ84が接続されている。原水槽11に貯留された被処理水は、配管23を通り、被処理水の一部が分流されて配管83内に流入する。分流された被処理水は、送水ポンプ84によって送水されて水質センサ81に供給される。   The treated water supplied to the water quality sensor 81 to be treated passes through the pipe 83 branched from the pipe 23 and is supplied to the water quality sensor 81. A water supply pump 84 is connected to the pipe 83. The treated water stored in the raw water tank 11 passes through the pipe 23, a part of the treated water is diverted and flows into the pipe 83. The treated water that has been diverted is fed by the water feed pump 84 and supplied to the water quality sensor 81.

水質センサ81には、検査後の被処理水を送水する配管85が接続されている。水質センサ81は、配管85を介して原水槽11に接続されている。検査後の被処理水は、配管85を通り、原水槽11へ戻される。これにより、検査後の被処理水を廃棄することなく、原水槽11に戻すことができる。そのため、新たな原水を受入れることなく、循環運転による流量を維持することができる。   The water quality sensor 81 is connected to a pipe 85 for supplying the treated water after the inspection. The water quality sensor 81 is connected to the raw water tank 11 through a pipe 85. The treated water after the inspection passes through the pipe 85 and is returned to the raw water tank 11. Thereby, the to-be-processed water after a test | inspection can be returned to the raw | natural water tank 11, without discarding. Therefore, the flow rate by the circulation operation can be maintained without receiving new raw water.

なお、水質センサ81,82にとしては、水のPH値を測定するPH計、水の濁り度合や水の色を測定する濁度計・色度計、水に含まれる塩分を測定する残塩計などが挙げられる。   The water quality sensors 81 and 82 include a pH meter that measures the pH value of water, a turbidity meter / colorimeter that measures the turbidity of water and the color of water, and residual salt that measures the salinity contained in water. Totals are listed.

次に、水処理装置10の運転方法について説明する。水処理装置10は、通常時において飲用水を製造しない待機状態となり、例えば上水道が使用できない非常時において飲用水を製造する給水状態となる。   Next, the operation method of the water treatment apparatus 10 will be described. The water treatment apparatus 10 is in a standby state in which drinking water is not produced at normal times, and is in a water supply state in which drinking water is produced, for example, in an emergency when the water supply cannot be used.

図3は、水処理装置10の運転方法の手順を示す工程図である。水処理装置10の運転方法では、原水の受入工程(ステップS1)、スタートアップ工程(ステップS2)、循環運転工程(ステップS3)、濃縮水の排水工程(ステップS4)、逆流洗浄工程(ステップS5)、濃縮水及び処理水の排水工程(ステップS6)、飲用水製造工程(ステップS7)を実行する。   FIG. 3 is a process diagram showing the procedure of the operation method of the water treatment apparatus 10. In the operation method of the water treatment apparatus 10, the raw water receiving process (step S1), the start-up process (step S2), the circulation operation process (step S3), the concentrated water draining process (step S4), and the backwashing process (step S5). Then, a draining process of concentrated water and treated water (step S6) and a potable water manufacturing process (step S7) are executed.

原水の受入工程S1では、水処理装置10は、原水の受入を行う。水処理装置10は、例えば原水として、地下水を汲み上げ、原水槽11に貯留する。このとき、次亜塩素酸を注入しながら、原水を受入れる。   In the raw water receiving step S1, the water treatment device 10 receives the raw water. The water treatment device 10 pumps up groundwater as raw water, for example, and stores it in the raw water tank 11. At this time, raw water is received while injecting hypochlorous acid.

スタートアップ工程S2では、原水槽11に貯留された被処理水(原水)に対して逆浸透膜処理を開始して、処理水を貯留する。図4は、スタートアップ工程における手順を示す工程図である。スタートアップ工程S2は、具体的には、ろ過工程(ステップS11)、還元剤注入工程(ステップS12)、分散剤注入工程(ステップS13)、混合工程(ステップS14)、昇圧工程(ステップS15)、逆浸透膜処理工程(ステップS16)、及び処理水貯留工程(ステップS17)を実行する。スタートアップ工程S2では、処理水が一定量分、貯留されるまで、原水の受入が継続されている。   In the start-up process S2, reverse osmosis membrane treatment is started on the treated water (raw water) stored in the raw water tank 11, and the treated water is stored. FIG. 4 is a process diagram showing a procedure in the startup process. Specifically, the startup process S2 includes a filtration process (step S11), a reducing agent injection process (step S12), a dispersant injection process (step S13), a mixing process (step S14), a pressure increasing process (step S15), and the reverse. An osmosis membrane treatment process (Step S16) and a treated water storage process (Step S17) are performed. In the start-up process S2, the raw water is continuously received until a certain amount of treated water is stored.

ろ過工程S11では、砂ろ過器12を用いて被処理水中の固形物を除去する。原水槽11に貯留された被処理水は、配管23を通り砂ろ過器12に供給され、固形物が除去される。砂ろ過器12から送水された処理水は、配管24を通りプレフィルタ14に供給される。砂ろ過器12から砂が流出した場合には、プレフィルタ14によって被処理水中の砂が除去される。   In filtration process S11, the solid substance in to-be-processed water is removed using the sand filter 12. FIG. The treated water stored in the raw water tank 11 is supplied to the sand filter 12 through the pipe 23, and the solid matter is removed. The treated water sent from the sand filter 12 is supplied to the prefilter 14 through the pipe 24. When sand flows out from the sand filter 12, the pre-filter 14 removes sand in the water to be treated.

還元剤注入工程S12では、被処理水中に還元剤を注入する。還元剤は、注入管26を通じて、配管25内に注入される。分散剤注入工程S13では、被処理水中に分散剤を注入する。分散剤は、注入管27を通じて、配管25内に注入される。   In the reducing agent injection step S12, a reducing agent is injected into the water to be treated. The reducing agent is injected into the pipe 25 through the injection pipe 26. In the dispersant injection step S13, the dispersant is injected into the water to be treated. The dispersant is injected into the pipe 25 through the injection pipe 27.

混合工程S14では、被処理水中の還元剤及び分散剤を混合して、被処理水中の還元剤の濃度及び分散剤の濃度を均一化させる。混合工程S14では、被処理水を混合器15に供給して、被処理水中の還元剤及び分散剤の混合を行う。   In the mixing step S14, the reducing agent and the dispersing agent in the for-treatment water are mixed to make the concentration of the reducing agent and the dispersing agent in the for-treatment water uniform. In the mixing step S14, the water to be treated is supplied to the mixer 15, and the reducing agent and the dispersant in the water to be treated are mixed.

昇圧工程S15では、高圧ポンプ17を用いて、被処理水を昇圧する。昇圧工程S15では、混合器15から排出された被処理水を高圧ポンプ17に供給し、逆浸透膜処理に必要な圧力まで昇圧する。   In the boosting step S15, the water to be treated is boosted using the high-pressure pump 17. In the pressure increasing step S15, the water to be treated discharged from the mixer 15 is supplied to the high pressure pump 17 to increase the pressure to a pressure required for the reverse osmosis membrane treatment.

逆浸透膜処理工程S16では、RO膜設備16を用いて逆浸透膜処理を行う。逆浸透膜処理工程S16では、高圧ポンプ17で昇圧された被処理水をRO膜設備16に供給し、被処理水を、RO膜を透過した処理水と、RO膜を透過しなかった濃縮水とに分離する。   In the reverse osmosis membrane treatment step S <b> 16, the reverse osmosis membrane treatment is performed using the RO membrane equipment 16. In the reverse osmosis membrane treatment step S16, the treated water pressurized by the high-pressure pump 17 is supplied to the RO membrane facility 16, and the treated water is treated water that has permeated the RO membrane and concentrated water that has not permeated the RO membrane. And to separate.

処理水貯留工程S17では、処理水を処理水槽18に貯留する。処理水貯留工程S17では、RO膜設備16から排出された処理水を処理水槽18に供給する。このとき、RO膜設備16から排出された濃縮水は、装置10外へ排出される。また、処理水貯留工程S17では、処理水槽18への次亜塩素酸の注入を行う。   In the treated water storage step S <b> 17, treated water is stored in the treated water tank 18. In the treated water storage step S <b> 17, treated water discharged from the RO membrane facility 16 is supplied to the treated water tank 18. At this time, the concentrated water discharged from the RO membrane facility 16 is discharged outside the apparatus 10. In the treated water storage step S17, hypochlorous acid is injected into the treated water tank 18.

スタートアップ工程S2は、処理水槽18に処理水が一定量、貯留されるまで実行される。処理水が一定量、貯留された後、循環運転工程S3に進む。   The start-up process S2 is executed until a certain amount of treated water is stored in the treated water tank 18. After a certain amount of treated water is stored, the process proceeds to the circulation operation step S3.

循環運転工程S3では、濃縮水及び処理水を原水槽11へ戻し、循環運転を実行する。図5は、循環運転工程における手順を示す工程図である。循環運転工程S3は、具体的には、ろ過工程(ステップS11)、還元剤注入工程(ステップS12)、分散剤注入工程(ステップS13)、混合工程(ステップS14)、昇圧工程(ステップS15)、逆浸透膜処理工程(ステップS16)、処理水貯留工程(ステップS17)、処理水返送工程(ステップS21)、及び濃縮水返送工程(ステップS22)を実行する。循環運転工程S3は、一定期間、継続される。循環運転工程S3を実行する際には、原水の受入を停止する。また、処理水の装置外への給水を停止している状態である。   In the circulation operation step S3, the concentrated water and the treated water are returned to the raw water tank 11, and the circulation operation is executed. FIG. 5 is a process diagram showing a procedure in the circulation operation process. Specifically, the circulation operation step S3 includes a filtration step (step S11), a reducing agent injection step (step S12), a dispersant injection step (step S13), a mixing step (step S14), a pressure increase step (step S15), A reverse osmosis membrane treatment process (step S16), a treated water storage process (step S17), a treated water return process (step S21), and a concentrated water return process (step S22) are executed. Circulation operation process S3 is continued for a fixed period. When the circulation operation step S3 is executed, the raw water reception is stopped. Moreover, it is the state which has stopped the water supply outside the apparatus of a treated water.

ろ過工程(ステップS11)、還元剤注入工程(ステップS12)、分散剤注入工程(ステップS13)、混合工程(ステップS14)、昇圧工程(ステップS15)、逆浸透膜処理工程(ステップS16)、処理水貯留工程(ステップS17)は、スタートアップ工程S2と同じであるためここでの説明は省略する。   Filtration step (step S11), reducing agent injection step (step S12), dispersant injection step (step S13), mixing step (step S14), pressure increasing step (step S15), reverse osmosis membrane treatment step (step S16), processing Since the water storage process (step S17) is the same as the startup process S2, description thereof is omitted here.

循環運転工程S3では、処理水貯留工程S17の後に、処理水返送工程S21を実行する。処理水返送工程S21では、処理水槽18に貯留された処理水を原水槽11へ返送する。処理水は、送水ポンプ19によって送水され、処理水返送配管51を通り、原水槽11に供給される。   In the circulation operation step S3, the treated water return step S21 is executed after the treated water storage step S17. In the treated water returning step S <b> 21, the treated water stored in the treated water tank 18 is returned to the raw water tank 11. The treated water is fed by the water pump 19, passes through the treated water return pipe 51, and is supplied to the raw water tank 11.

循環運転工程S3では、RO膜設備16から排出された濃縮水を原水槽11返送する濃縮水返送工程S22を実行する。濃縮水は、濃縮水返送配管61を通り、原水槽11に供給される。   In the circulation operation step S3, a concentrated water returning step S22 for returning the concentrated water discharged from the RO membrane facility 16 to the raw water tank 11 is executed. The concentrated water passes through the concentrated water return pipe 61 and is supplied to the raw water tank 11.

原水槽11に返送された処理水及び濃縮水は、再度、砂ろ過器12へ供給されて、ろ過工程S11が実行される。同様に、ステップS12〜S17、S21、S22が繰り返し実行される。これにより、水処理装置10の待機状態において、処理水及び濃縮水を循環させる循環運転を行うことができる。この循環運転により、RO膜に水を供給し続けることができるので、RO膜の劣化を抑制することができる。   The treated water and concentrated water returned to the raw water tank 11 are again supplied to the sand filter 12, and the filtration step S11 is performed. Similarly, steps S12 to S17, S21, and S22 are repeatedly executed. Thereby, in the standby state of the water treatment apparatus 10, the circulation operation which circulates treated water and concentrated water can be performed. By this circulation operation, water can be continuously supplied to the RO membrane, so that deterioration of the RO membrane can be suppressed.

濃縮水の排水工程S4では、循環運転を停止して濃縮水の排水を行う。例えば、1ヶ月間の循環運転の継続後、飲用水の製造を実行しない場合には、ステップS4に進む。   In the concentrated water draining step S4, the circulating operation is stopped and the concentrated water is drained. For example, if the production of potable water is not executed after the circulation operation for one month is continued, the process proceeds to step S4.

濃縮水の排水工程S4では、処理水槽18に砂ろ過器12に逆洗可能な水量が貯水されるまで、濃縮水を廃棄する。このとき、処理水の原水槽11への返送、及び濃縮水の原水槽11への返送は、停止されている。RO膜設備16から排出された濃縮水は、装置外へ廃棄される。RO膜設備16から排出された処理水は、処理水槽18に貯留される。   In the concentrated water draining step S <b> 4, the concentrated water is discarded until the treated water tank 18 stores an amount of water that can be backwashed in the sand filter 12. At this time, the return of the treated water to the raw water tank 11 and the return of the concentrated water to the raw water tank 11 are stopped. The concentrated water discharged from the RO membrane facility 16 is discarded outside the apparatus. The treated water discharged from the RO membrane facility 16 is stored in the treated water tank 18.

逆流洗浄工程S5は、処理水を砂ろ過器12へ供給して、砂ろ過器12の逆流洗浄を行う。処理水を砂ろ過器12の出口側12bに供給し、砂ろ過器12からの排水は、入口側12aから排出して、装置外へ廃棄する。これにより、砂ろ過器12の機能を回復させることができる。   In the backwashing step S <b> 5, treated water is supplied to the sand filter 12 to perform backwashing of the sand filter 12. The treated water is supplied to the outlet side 12b of the sand filter 12, and the waste water from the sand filter 12 is discharged from the inlet side 12a and discarded outside the apparatus. Thereby, the function of the sand filter 12 can be recovered.

逆流洗浄工程S5の実行後、再び、スタートアップ工程S2を実行する。水処理装置10の待機状態において、飲用水を製造しない場合には、ステップS2〜S5を繰り返す。   After the backwash process S5 is performed, the start-up process S2 is performed again. When potable water is not manufactured in the standby state of the water treatment apparatus 10, steps S2 to S5 are repeated.

例えば、非常時において、飲用水を製造する必要が生じた場合には、ステップS6及びS7を実行する。ここでは、循環運転工程S3の実行中に、ステップ6及びS7に移行する場合について説明する。   For example, when it becomes necessary to produce potable water in an emergency, steps S6 and S7 are executed. Here, a case will be described in which the process proceeds to steps 6 and S7 during the execution of the circulation operation step S3.

循環運転中に、飲用水を製造することが求められた場合には、濃縮水及び処理水の排水工程S6に進む。濃縮水及び処理水の排水工程S6では、循環運転を停止して濃縮水及び処理水の排水を行う。処理水槽18に貯留されていた処理水は、下水配管31を通り、装置外へ排出される。排水工程S6は、処理水槽18が空になるまで実行される。   When it is required to produce potable water during the circulation operation, the process proceeds to the drainage step S6 of concentrated water and treated water. In the drainage step S6 of the concentrated water and the treated water, the circulation operation is stopped and the concentrated water and the treated water are drained. The treated water stored in the treated water tank 18 passes through the sewage pipe 31 and is discharged outside the apparatus. The drainage step S6 is executed until the treated water tank 18 becomes empty.

濃縮水及び処理水の排水工程S6の実行後、飲用水の製造工程S7が実行される。飲用水の製造工程S7では、原水を原水槽11に貯留した後、ステップS11〜S17を実行する。処理水槽18に貯留された処理水は、飲用水として装置外へ給水される。RO膜設備16から排出された濃縮水は、下水配管31を通り、装置外11へ廃棄される。   After the execution of the drainage step S6 of the concentrated water and the treated water, a potable water production step S7 is executed. In potable water manufacturing process S7, after storing raw | natural water in the raw | natural water tank 11, steps S11-S17 are performed. The treated water stored in the treated water tank 18 is supplied outside the apparatus as drinking water. The concentrated water discharged from the RO membrane facility 16 passes through the sewage pipe 31 and is discarded outside the apparatus 11.

また、飲用水を装置外へ提供する場合には、処理水中に中和剤が供給されて、pHを調整したのちに装置外へ給水される。   Moreover, when providing drinking water outside the apparatus, a neutralizing agent is supplied into the treated water, and after adjusting the pH, the water is supplied outside the apparatus.

また、循環運転工程S3及び飲用水製造工程S7の実行中には、処理水の水質検査及び被処理水の水質検査が実行されている。処理水の一部は、分流されて水質センサ82に供給される。検査後の処理水は、処理水槽18に戻される。被処理水の一部は、分流されて水質センサ81に供給される。検査後の被処理水は、原水槽11に戻される。   In addition, during the execution of the circulation operation step S3 and the potable water production step S7, a water quality test for treated water and a water quality test for treated water are performed. A portion of the treated water is diverted and supplied to the water quality sensor 82. The treated water after the inspection is returned to the treated water tank 18. A part of the water to be treated is diverted and supplied to the water quality sensor 81. The treated water after the inspection is returned to the raw water tank 11.

このような水処理装置10及び運転方法によれば、処理水及び濃縮水を循環させる循環運転を行うことで、RO膜に被処理水を供給し続けることができる。水処理装置10は、処理水を飲用水として装置外へ給水しない待機状態において、循環運転を行うことで、水処理装置10の管路を清潔に保ち、さらに、RO膜の劣化を防止することができる。また、非常時において、飲用水の製造工程に移行する場合には、速やかに飲用水の製造を実行することができる。   According to such a water treatment device 10 and an operation method, the water to be treated can be continuously supplied to the RO membrane by performing a circulation operation for circulating the treated water and the concentrated water. The water treatment device 10 keeps the pipeline of the water treatment device 10 clean and prevents the RO membrane from being deteriorated by performing a circulation operation in a standby state where the treated water is not supplied as drinking water to the outside of the device. Can do. Moreover, when it transfers to the manufacturing process of drinking water in an emergency, manufacturing of drinking water can be performed rapidly.

また、水処理装置10は、処理水槽18内に次亜塩素酸を注入する注入管33(次亜塩素酸注入手段)と、RO膜設備16の上流側で、被処理水に還元剤を注入する注入管26(還元剤注入手段)と、を備えている。これにより、原水槽11へ返送される処理水に次亜塩素酸を注入することができ、装置10内の殺菌を行うことができる。また、RO膜設備18の上流側に還元剤を注入することができるので、被処理水中の次亜塩素酸を還元剤により還元した後に、被処理水をRO膜設備16に供給できる。従って、RO膜の次亜塩素酸による劣化を抑制することができる。   Further, the water treatment apparatus 10 injects a reducing agent into the water to be treated on the upstream side of the injection pipe 33 (hypochlorous acid injection means) for injecting hypochlorous acid into the treated water tank 18 and the RO membrane facility 16. And an injection pipe 26 (reducing agent injection means). Thereby, hypochlorous acid can be inject | poured into the treated water returned to the raw | natural water tank 11, and the sterilization in the apparatus 10 can be performed. Further, since the reducing agent can be injected upstream of the RO membrane facility 18, the treated water can be supplied to the RO membrane facility 16 after reducing hypochlorous acid in the treated water with the reducing agent. Therefore, the deterioration of the RO membrane due to hypochlorous acid can be suppressed.

また、水処理装置10は、原水槽11に供給される原水に次亜塩素酸を注入する注入管22(第二の次亜塩素酸注入手段)を備えている。これにより、原水を殺菌した上で原水槽11に供給することができるため、水処理装置10の管路をより清潔に保つことができる。   Further, the water treatment apparatus 10 includes an injection pipe 22 (second hypochlorous acid injection means) for injecting hypochlorous acid into the raw water supplied to the raw water tank 11. Thereby, after sterilizing raw | natural water, it can supply to the raw | natural water tank 11, Therefore The pipe line of the water treatment apparatus 10 can be kept more clean.

以上、本発明をその実施の形態に基づき具体的に説明したが、本発明は上記実施形態に限定されるものではない。上記実施形態では、非常時に飲用水を製造する水処理装置について説明しているが、常時飲用水を製造する水処理装置10に本発明を適用してもよい。例えば、水処理装置10の下流側の装置において、保全作業を行う場合などに、飲用水の製造を中止して、処理水及び濃縮水を循環させてもよい。   Although the present invention has been specifically described above based on the embodiment, the present invention is not limited to the above embodiment. Although the said embodiment demonstrated the water treatment apparatus which manufactures drinking water at the time of emergency, you may apply this invention to the water treatment apparatus 10 which always manufactures drinking water. For example, in a device downstream of the water treatment device 10, when maintenance work is performed, the production of potable water may be stopped and the treated water and concentrated water may be circulated.

また、上記実施形態では、処理水及び濃縮水を別々に原水槽11へ返送しているが、処理水及び濃縮水を合流させた後に、原水槽11へ返送してもよい。   Moreover, in the said embodiment, although treated water and concentrated water are separately returned to the raw | natural water tank 11, you may return to raw | natural water tank 11, after making treated water and concentrated water merge.

また、上記実施形態の運転方法では、ステップS6において処理水の排水を実施しているが、処理水を装置外へ排出せずに原水の原水槽11への受入れを開始し、昇圧工程S15及び逆浸透膜処理工程S16を実行し、当該逆浸透膜処理工程S16で処理された処理水を装置10外へ給水してもよい。   Further, in the operation method of the above embodiment, the treated water is drained in step S6. However, the receiving of the raw water into the raw water tank 11 is started without discharging the treated water to the outside of the apparatus, and the boosting step S15 and The reverse osmosis membrane treatment step S16 may be executed, and the treated water treated in the reverse osmosis membrane treatment step S16 may be supplied to the outside of the apparatus 10.

また、上記実施形態の運転方法では、ステップS6において処理水及び濃縮水を装置外へ排水した後に、原水の原水槽11への受入れを開始しているが、処理水及び濃縮水の装置外への排水と同時に、原水の原水槽11への受入れを開始し、昇圧工程S15及び逆浸透膜処理工程S16を実行し、当該逆浸透膜処理工程S16で処理された処理水を装置10外へ給水してもよい。   In the operation method of the above embodiment, after draining the treated water and the concentrated water to the outside of the apparatus in step S6, the acceptance of the raw water into the raw water tank 11 is started. At the same time as the drainage of the raw water, acceptance of the raw water into the raw water tank 11 is started, the pressurization step S15 and the reverse osmosis membrane treatment step S16 are executed, and the treated water treated in the reverse osmosis membrane treatment step S16 is supplied to the outside of the apparatus 10 May be.

10…水処理装置、11…原水槽、12…砂ろ過器、16…RO膜設備、17…高圧ポンプ(昇圧手段)、18…処理水槽、22…注入管(第2の次亜塩素酸注入手段)、26…注入管(還元剤注入手段)、33…注入管(次亜塩素酸注入手段)、41…開閉弁(流入量調整部)、50…処理水返送手段、51…処理水返送配管、60…濃縮水返送手段、61…濃縮水返送配管、70…逆流洗浄手段、71…逆洗用配管、81…被処理水の水質センサ、82…処理水の水質センサ。   DESCRIPTION OF SYMBOLS 10 ... Water treatment apparatus, 11 ... Raw water tank, 12 ... Sand filter, 16 ... RO membrane equipment, 17 ... High pressure pump (pressure | voltage riser), 18 ... Treatment water tank, 22 ... Injection pipe | tube (2nd hypochlorous acid injection) Means), 26 ... injection pipe (reducing agent injection means), 33 ... injection pipe (hypochlorous acid injection means), 41 ... on-off valve (inflow adjustment part), 50 ... treated water return means, 51 ... treated water return Pipe: 60 ... Concentrated water return means, 61 ... Concentrated water return pipe, 70 ... Backwashing means, 71 ... Backwash pipe, 81 ... Water quality sensor for treated water, 82 ... Water quality sensor for treated water.

Claims (17)

原水を貯留する原水槽と、
前記原水槽に貯留された被処理水を昇圧する昇圧手段と、
前記昇圧手段によって昇圧された前記被処理水を処理するRO膜と、
前記RO膜を透過した処理水を貯留する処理水槽と、
前記処理水を装置外へ給水する給水部と、
前記処理水槽に貯留された前記処理水を前記原水槽へ返送可能な処理水返送手段と、
RO膜濃縮水を前記原水槽へ返送可能な濃縮水返送手段と、
を備える水処理装置。
A raw water tank for storing raw water,
Pressurizing means for boosting the water to be treated stored in the raw water tank;
An RO membrane for treating the water to be treated that has been pressurized by the boosting means;
A treated water tank for storing treated water that has passed through the RO membrane;
A water supply unit for supplying the treated water to the outside of the apparatus;
Treated water return means capable of returning the treated water stored in the treated water tank to the raw water tank;
Concentrated water returning means capable of returning the RO membrane concentrated water to the raw water tank;
A water treatment apparatus comprising:
前記昇圧手段の上流側に配置され、前記原水槽から供給された被処理水中の不純物を分離する濾過器と、
前記処理水を前記濾過器に供給して、当該濾過器を逆流洗浄する逆洗手段と、を備える請求項1に記載の水処理装置。
A filter that is disposed on the upstream side of the pressurizing means and separates impurities in the water to be treated supplied from the raw water tank;
The water treatment apparatus according to claim 1, further comprising backwashing means for supplying the treated water to the filter and backwashing the filter.
前記処理水槽内に次亜塩素酸を注入する次亜塩素酸注入手段と、
前記RO膜の上流側で、前記被処理水に還元剤を注入する還元剤注入手段と、を備える請求項1又は2に記載の水処理装置。
Hypochlorous acid injection means for injecting hypochlorous acid into the treated water tank;
The water treatment apparatus according to claim 1, further comprising a reducing agent injection unit that injects a reducing agent into the water to be treated on an upstream side of the RO membrane.
前記処理水槽内に次亜塩素酸を注入する次亜塩素酸注入手段と、
前記昇圧手段の上流側で、前記被処理水に還元剤を注入する還元剤注入手段と、を備える請求項1又は2に記載の水処理装置。
Hypochlorous acid injection means for injecting hypochlorous acid into the treated water tank;
The water treatment apparatus according to claim 1, further comprising a reducing agent injection unit that injects a reducing agent into the water to be treated on an upstream side of the pressure increasing unit.
前記被処理水の一部を分流し、分流された当該被処理水を流通させながら水質を検査する被処理水の水質センサを更に備え、
前記水質センサによって検査された前記被処理水を前記原水槽に返送する請求項1〜4の何れか一項に記載の水処理装置。
A water quality sensor is further provided for inspecting water quality while distributing a part of the treated water and distributing the separated treated water.
The water treatment apparatus as described in any one of Claims 1-4 which returns the said to-be-processed water test | inspected by the said water quality sensor to the said raw | natural water tank.
前記処理水の一部を分流し、分流された当該処理水を流通させながら水質を検査する処理水の水質センサと、を更に備え、
前記水質センサによって検査された前記処理水を前記処理水槽に返送する請求項1〜4の何れか1項に記載の水処理装置。
A part of the treated water, and further comprising a treated water quality sensor for inspecting the water quality while circulating the separated treated water,
The water treatment apparatus according to any one of claims 1 to 4, wherein the treated water inspected by the water quality sensor is returned to the treated water tank.
前記濾過器が、砂濾過装置及び/又は膜濾過装置である請求項2〜6の何れか1項に記載の水処理装置。   The water treatment device according to any one of claims 2 to 6, wherein the filter is a sand filtration device and / or a membrane filtration device. 前記原水槽に原水を供給する際に、前記原水に次亜塩素酸を注入する第二の次亜塩素酸注入手段を備える請求項2〜7の何れか1項に記載の水処理装置。   The water treatment apparatus according to any one of claims 2 to 7, further comprising second hypochlorous acid injection means for injecting hypochlorous acid into the raw water when supplying the raw water to the raw water tank. 原水を原水槽に受入れて貯留し、前記原水槽に貯留された被処理水を、RO膜を用いて処理し、前記RO膜を透過した処理水を装置外へ給水可能な水処理装置の運転方法において、
前記原水槽に貯留された被処理水を昇圧する昇圧工程と、
前記昇圧工程で昇圧された前記被処理水を、前記RO膜を用いて処理する逆浸透膜処理工程と、
前記RO膜を透過した処理水を前記原水槽へ返送する処理水返送工程と、
RO膜濃縮水を前記原水槽へ返送する濃縮水返送工程と、
を備える水処理装置の運転方法。
Operation of a water treatment apparatus that receives raw water in a raw water tank, stores the treated water stored in the raw water tank using an RO membrane, and supplies the treated water that has passed through the RO membrane to the outside of the apparatus In the method
A step of boosting the water to be treated stored in the raw water tank;
A reverse osmosis membrane treatment step of treating the water to be treated that has been pressurized in the pressure raising step with the RO membrane;
A treated water returning step of returning treated water that has passed through the RO membrane to the raw water tank;
A concentrated water returning step of returning the RO membrane concentrated water to the raw water tank;
A method for operating a water treatment apparatus comprising:
前記処理水返送工程では、前記処理水に次亜塩素酸を注入し、前記次亜塩素酸が注入された前記処理水を返送し、
前記被処理水を前記RO膜に供給する前に、当該被処理水に還元剤を注入する還元剤注入工程を更に備える請求項9に記載の水処理装置の運転方法。
In the treated water returning step, hypochlorous acid is injected into the treated water, and the treated water into which the hypochlorous acid has been injected is returned,
The method for operating a water treatment apparatus according to claim 9, further comprising a reducing agent injection step of injecting a reducing agent into the water to be treated before supplying the water to be treated to the RO membrane.
前記処理水返送工程では、前記処理水に次亜塩素酸を注入し、前記次亜塩素酸が注入された前記処理水を返送し、
前記原水槽に貯留された被処理水を昇圧する前に前記被処理水に還元剤を注入する還元剤注入工程を更に備える請求項9に記載の水処理装置の運転方法。
In the treated water returning step, hypochlorous acid is injected into the treated water, and the treated water into which the hypochlorous acid has been injected is returned,
The operating method of the water treatment apparatus of Claim 9 further equipped with the reducing agent injection | pouring process which inject | pours a reducing agent into the said to-be-processed water before pressurizing the to-be-processed water stored in the said raw | natural water tank.
前記昇圧工程の前に実行され、前記被処理水中の不純物を分離する濾過工程を更に備える請求項9〜11の何れか一項に記載の水処理装置の運転方法。   The operation method of the water treatment apparatus according to any one of claims 9 to 11, further comprising a filtration step that is performed before the pressurization step and separates impurities in the water to be treated. 前記処理水返送工程による前記処理水の前記原水槽への返送を停止し、前記処理水を前記濾過工程で使用された濾過器に供給して、当該濾過器の逆流洗浄を行う逆洗工程を更に備える請求項12に記載の水処理装置の運転方法。   Stopping the return of the treated water to the raw water tank by the treated water returning process, supplying the treated water to the filter used in the filtering process, and performing a backwashing process for backwashing the filter The operation method of the water treatment apparatus according to claim 12 further provided. 前記被処理水の一部を分流し、分流された当該被処理水を流通させながら水質を検査し、検査された前記被処理水を前記原水槽に返送する被処理水の水質検査工程を更に備える請求項9〜13の何れか一項に記載の水処理装置の運転方法。   A water quality inspection step of diverting a part of the treated water, inspecting the water quality while distributing the separated treated water, and returning the inspected treated water to the raw water tank The operation method of the water treatment apparatus as described in any one of Claims 9-13 provided. 前記処理水の一部を分流し、分流された当該処理水を流通させながら水質を検査し、検査された前記処理水を処理水槽に返送する処理水の水質検査工程を更に備える請求項9〜14の何れか一項に記載の水処理装置の運転方法。   A part of the treated water is diverted, water quality is inspected while circulating the treated water that has been diverted, and a water quality inspection step for returning the inspected treated water to the treated water tank is further provided. The operation method of the water treatment apparatus as described in any one of 14. 前記処理水返送工程による前記処理水の返送を停止すると共に、前記濃縮水返送工程による前記濃縮水の返送を停止し、
前記処理水を装置外へ排出せずに前記原水の前記原水槽への受入れを開始し、
前記昇圧工程及び前記逆浸透膜処理工程を実行し当該逆浸透膜処理工程で処理された前記処理水を装置外へ給水する請求項9〜15の何れか一項に記載の水処理装置の運転方法。
While stopping the return of the treated water by the treated water return step, stopping the return of the concentrated water by the concentrated water return step,
Start accepting the raw water into the raw water tank without discharging the treated water outside the apparatus,
Operation of the water treatment apparatus as described in any one of Claims 9-15 which performs the said pressure | voltage rise process and the said reverse osmosis membrane treatment process, and supplies the said treated water processed by the said reverse osmosis membrane treatment process out of an apparatus. Method.
前記処理水返送工程による前記処理水の返送を停止すると共に、前記濃縮水返送工程による前記濃縮水の返送を停止し、
前記処理水及び前記濃縮水を装置外へ排出した後又は排出と同時に、前記原水の前記原水槽への受入れを開始し、
前記昇圧工程及び前記逆浸透膜処理工程を実行し当該逆浸透膜処理工程で処理された前記処理水を装置外へ給水する請求項9〜15の何れか一項に記載の水処理装置の運転方法。
While stopping the return of the treated water by the treated water return step, stopping the return of the concentrated water by the concentrated water return step,
After discharging the treated water and the concentrated water to the outside of the apparatus or at the same time as discharging, start receiving the raw water into the raw water tank,
Operation of the water treatment apparatus as described in any one of Claims 9-15 which performs the said pressure | voltage rise process and the said reverse osmosis membrane treatment process, and supplies the said treated water processed by the said reverse osmosis membrane treatment process out of an apparatus. Method.
JP2012197909A 2012-09-07 2012-09-07 Method for operating water treatment apparatus and method for producing potable water Expired - Fee Related JP6141610B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2012197909A JP6141610B2 (en) 2012-09-07 2012-09-07 Method for operating water treatment apparatus and method for producing potable water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2012197909A JP6141610B2 (en) 2012-09-07 2012-09-07 Method for operating water treatment apparatus and method for producing potable water

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2017092380A Division JP6300988B2 (en) 2017-05-08 2017-05-08 Method for operating water treatment apparatus and method for producing potable water

Publications (2)

Publication Number Publication Date
JP2014050810A true JP2014050810A (en) 2014-03-20
JP6141610B2 JP6141610B2 (en) 2017-06-07

Family

ID=50609815

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2012197909A Expired - Fee Related JP6141610B2 (en) 2012-09-07 2012-09-07 Method for operating water treatment apparatus and method for producing potable water

Country Status (1)

Country Link
JP (1) JP6141610B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015199020A (en) * 2014-04-07 2015-11-12 株式会社神鋼環境ソリューション Method and installation for water treatment
JP2020104038A (en) * 2018-12-26 2020-07-09 三菱ケミカルアクア・ソリューションズ株式会社 Water treatment system operation method and water treatment system
KR20210076485A (en) * 2019-12-16 2021-06-24 남은경 Method for seawater desalination available of non-stop osmotic backwashing cleaning

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5584586A (en) * 1978-09-20 1980-06-25 Mitsubishi Heavy Ind Ltd Treatment of waste water
JPS57165205U (en) * 1981-04-09 1982-10-18
JPH1099605A (en) * 1996-10-01 1998-04-21 Kajima Corp Device for chemical injection for turbid water treatment
JP2001047045A (en) * 1999-08-17 2001-02-20 Japan Organo Co Ltd Reverse osmosis membrane type desalination apparatus
JP2002126733A (en) * 2000-10-26 2002-05-08 Teraoka Seiko Co Ltd Water cleaning apparatus
JP2002307058A (en) * 2001-04-17 2002-10-22 Ebara Corp Pure water producing apparatus using reverse osmosis membrane module, and method of using the same
JP2006272136A (en) * 2005-03-29 2006-10-12 Toray Ind Inc Membrane separation method and membrane separation device
JP2007105572A (en) * 2005-10-11 2007-04-26 Teraoka Seiko Co Ltd Reverse osmosis membrane type water-purifying device
JP2009022886A (en) * 2007-07-19 2009-02-05 Kurita Water Ind Ltd Method for improving blocking rate of permeable membrane, blocking rate improved permeable membrane, and permeable membrane treatment method and apparatus
JP2011031121A (en) * 2009-07-29 2011-02-17 Mitsubishi Heavy Ind Ltd Desalination apparatus and washing method of pretreatment membrane of desalination apparatus
JP2011242036A (en) * 2010-05-17 2011-12-01 Hitachi Plant Technologies Ltd Air conditioner and system using deep seawater
JP2012120970A (en) * 2010-12-07 2012-06-28 Mitsubishi Heavy Ind Ltd Desalination apparatus and desalination method
JP2014018403A (en) * 2012-07-18 2014-02-03 Jms Co Ltd Manufacturing apparatus of ro water to be supplied to medical apparatus and method for manufacturing ro water using the same

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5584586A (en) * 1978-09-20 1980-06-25 Mitsubishi Heavy Ind Ltd Treatment of waste water
JPS57165205U (en) * 1981-04-09 1982-10-18
JPH1099605A (en) * 1996-10-01 1998-04-21 Kajima Corp Device for chemical injection for turbid water treatment
JP2001047045A (en) * 1999-08-17 2001-02-20 Japan Organo Co Ltd Reverse osmosis membrane type desalination apparatus
JP2002126733A (en) * 2000-10-26 2002-05-08 Teraoka Seiko Co Ltd Water cleaning apparatus
JP2002307058A (en) * 2001-04-17 2002-10-22 Ebara Corp Pure water producing apparatus using reverse osmosis membrane module, and method of using the same
JP2006272136A (en) * 2005-03-29 2006-10-12 Toray Ind Inc Membrane separation method and membrane separation device
JP2007105572A (en) * 2005-10-11 2007-04-26 Teraoka Seiko Co Ltd Reverse osmosis membrane type water-purifying device
JP2009022886A (en) * 2007-07-19 2009-02-05 Kurita Water Ind Ltd Method for improving blocking rate of permeable membrane, blocking rate improved permeable membrane, and permeable membrane treatment method and apparatus
JP2011031121A (en) * 2009-07-29 2011-02-17 Mitsubishi Heavy Ind Ltd Desalination apparatus and washing method of pretreatment membrane of desalination apparatus
JP2011242036A (en) * 2010-05-17 2011-12-01 Hitachi Plant Technologies Ltd Air conditioner and system using deep seawater
JP2012120970A (en) * 2010-12-07 2012-06-28 Mitsubishi Heavy Ind Ltd Desalination apparatus and desalination method
JP2014018403A (en) * 2012-07-18 2014-02-03 Jms Co Ltd Manufacturing apparatus of ro water to be supplied to medical apparatus and method for manufacturing ro water using the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015199020A (en) * 2014-04-07 2015-11-12 株式会社神鋼環境ソリューション Method and installation for water treatment
JP2020104038A (en) * 2018-12-26 2020-07-09 三菱ケミカルアクア・ソリューションズ株式会社 Water treatment system operation method and water treatment system
KR20210076485A (en) * 2019-12-16 2021-06-24 남은경 Method for seawater desalination available of non-stop osmotic backwashing cleaning
KR102276832B1 (en) 2019-12-16 2021-07-14 남은경 Method for seawater desalination available of non-stop osmotic backwashing cleaning

Also Published As

Publication number Publication date
JP6141610B2 (en) 2017-06-07

Similar Documents

Publication Publication Date Title
US6349835B1 (en) Water treatment installation
US8685249B2 (en) Multi-stage seawater desalination apparatus and operation control method of multi-stage seawater desalination apparatus
US6074551A (en) Automatic cleaning system for a reverse osmosis unit in a high purity water treatment system
CN110536742B (en) High recovery integrated UF/RO system
US20110049048A1 (en) Water purification system
KR102027026B1 (en) Ultrapure water production system, ultrapure water production supply system, and method for cleaning same
JP4241684B2 (en) Membrane module cleaning method
KR100987294B1 (en) Osmotic backwashing cleaning method of high pressure filtration and device using the same
Oka et al. Operation of passive membrane systems for drinking water treatment
WO2011010500A1 (en) Water producing system
KR101299165B1 (en) Pressured membrane filtration apparatus and method with chemical feed automatic control
US20190047878A1 (en) Residential grey water recycling system
JP5245216B2 (en) Hollow fiber membrane water treatment method and water treatment apparatus
Brover et al. Optimization of ultrafiltration as pre-treatment for seawater RO desalination
JP6141610B2 (en) Method for operating water treatment apparatus and method for producing potable water
JP6300988B2 (en) Method for operating water treatment apparatus and method for producing potable water
JP6344114B2 (en) Water treatment apparatus and water treatment equipment cleaning method
KR101730978B1 (en) Water treatment system and method with separation membrane washing using ozon and hydrogen peroxide
US20160101389A1 (en) Method of performing a cleaning operation on a water filtration device
KR101481075B1 (en) Continuous flow type apparatus for water treatment using submerged type membrane filtration and method for backwashing membrane thereof
JP2006122787A (en) Seawater desalting method
JP6428017B2 (en) Water treatment apparatus and water treatment equipment cleaning method
KR101987924B1 (en) Apparatus and method for injecting oxidizing agent capable of corresponding dissolved manganese in purification process of membrane filtration
JP2007301469A (en) Water treatment method
JP2007245051A (en) Method of cleaning filter membrane

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20150903

A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A712

Effective date: 20160405

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20160414

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20160518

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20160607

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20160805

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20161115

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20170113

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20170404

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20170508

R150 Certificate of patent or registration of utility model

Ref document number: 6141610

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

LAPS Cancellation because of no payment of annual fees