JP2021065802A - Water treatment system and water treatment method - Google Patents

Water treatment system and water treatment method Download PDF

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JP2021065802A
JP2021065802A JP2019190348A JP2019190348A JP2021065802A JP 2021065802 A JP2021065802 A JP 2021065802A JP 2019190348 A JP2019190348 A JP 2019190348A JP 2019190348 A JP2019190348 A JP 2019190348A JP 2021065802 A JP2021065802 A JP 2021065802A
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water treatment
water
treatment facility
reserve
pipe
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JP7354756B2 (en
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英邦 亀田
Hidekuni Kameda
英邦 亀田
育野 望
Nozomi Ikuno
望 育野
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Kurita Water Industries Ltd
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Abstract

To provide a water treatment system and a water treatment method that enable efficient use of equipment in a water treatment system including water treatment equipment.SOLUTION: Raw water is supplied to an irrigation water treatment facility 2 by a pipe 1 for treatment, and treated water is supplied to a use point 4 by a pipe 3. Discharged water of the use point 4 is supplied to a wastewater treatment facility 6 by a pipe 5, and treated water is discharged by a pipe 7. A reserve water treatment facility 2A having substantially the same configuration as the water treatment facility 2 is provided, and if necessary, a part of the wastewater discharged from the use point 4 or the wastewater treatment facility 6 is received and treated, and returned to the water treatment facility 2 or the use point 4.SELECTED DRAWING: Figure 2

Description

本発明は水を処理して使用するための水処理システム及び水処理方法に関する。 The present invention relates to a water treatment system and a water treatment method for treating and using water.

純水や超純水等を用いる水使用設備に対し、原水を処理して所定水質の水を供給するために、水処理装置が用いられている。 A water treatment device is used to treat raw water and supply water of a predetermined water quality to a water-using facility that uses pure water, ultrapure water, or the like.

例えば、各種製造プラントにおいて、用水処理、排水処理、排水回収の工程において各工程に適した構成の装置が工程ごとに独立して設計される。そのため装置構成は不統一であり設計費用増加や現場試験長期化の傾向がある。 For example, in various manufacturing plants, in the processes of water treatment, wastewater treatment, and wastewater recovery, devices having a configuration suitable for each process are independently designed for each process. Therefore, the equipment configuration is inconsistent, and there is a tendency for design costs to increase and field tests to be lengthened.

特開平9−192643号公報には、純水使用排水を分別して、純水用に再利用する系と雑用水用に再利用する系の2系列において同じ装置構成のユニットを用いて回収系排水処理を行うことが記載されている。 Japanese Patent Application Laid-Open No. 9-192643 describes recovery system wastewater using units having the same device configuration in two systems, a system that separates wastewater using pure water and reuses it for pure water, and a system that reuses it for miscellaneous water. It is described that the processing is performed.

また特開2018−171578号公報、特開2018−158310号公報、特開2017−140577号公報、特開2017−170275号公報には、用水処理や排水回収に凝集→除濁→脱塩という同じ概念の水処理ユニットを用いることが記載されている。 Further, in JP-A-2018-171578, JP-A-2018-158310, JP-A-2017-140557, and JP-A-2017-170275, the same as aggregation-> turbidity-> desalting for water treatment and wastewater recovery. It is described to use the conceptual water treatment unit.

しかしこの場合も、一旦ユニットが用水処理用、排水回収用など用途が決まると、この用途に固定であり、途中で別の用途に変更することはなかった。そのため要求される水量が得られない場合や、要求が低く使用されない水処理ユニットが生じるなど非効率なケースがあった。 However, in this case as well, once the unit was determined to be used for water treatment, wastewater recovery, etc., it was fixed to this use and was not changed to another use on the way. Therefore, there have been cases of inefficiency such as the required amount of water cannot be obtained, or the demand is low and some water treatment units are not used.

特開平9−192643号公報Japanese Unexamined Patent Publication No. 9-192643 特開2018−171578号公報Japanese Unexamined Patent Publication No. 2018-171578 特開2018−158310号公報JP-A-2018-158310 特開2017−140577号公報Japanese Unexamined Patent Publication No. 2017-140577 特開2017−170275号公報JP-A-2017-170275

本発明は、用水処理設備を含む水処理システムにおいて設備の効率的な使用を可能とする水処理システム及び水処理方法を提供することを目的とする。 An object of the present invention is to provide a water treatment system and a water treatment method that enable efficient use of the equipment in a water treatment system including a water treatment equipment.

本発明の水処理システムは、原水を処理する用水処理設備を備えた主系列を有する水処理システムにおいて、該用水処理設備と略同一構成の予備水処理設備を備えており、該予備水処理設備が該主系列に組み込み可能となっていることを特徴とする。 The water treatment system of the present invention is a water treatment system having a main series equipped with a water treatment facility for treating raw water, and is provided with a reserve water treatment facility having substantially the same configuration as the water treatment facility. Is characterized in that it can be incorporated into the main series.

本発明の一態様では、前記用水処理設備及び予備水処理設備は、少なくとも、凝集装置、除濁装置及び脱塩装置を有する。 In one aspect of the present invention, the water treatment equipment and the reserve water treatment equipment include at least a coagulation device, a decontamination device, and a desalting device.

本発明の一態様では、前記主系列は、第1配管によって原水が供給される前記用水処理設備と、該用水処理設備からの処理水が第2配管によって供給されるユースポイントと、該ユースポイントからの排出水が第3配管によって供給される排水処理設備と、該排水処理設備の流出水を流すための第4配管とを備えている。 In one aspect of the present invention, the main series includes the water treatment facility to which raw water is supplied by the first pipe, a use point in which the treated water from the water treatment facility is supplied by the second pipe, and the use point. It is provided with a wastewater treatment facility in which the wastewater discharged from the wastewater is supplied by a third pipe, and a fourth pipe for flowing the outflow water of the wastewater treatment facility.

本発明の一態様では、前記第1、第2、第3及び第4配管に、それぞれ、配管接続部が設けられている。 In one aspect of the present invention, each of the first, second, third, and fourth pipes is provided with a pipe connection portion.

本発明の水処理方法は、かかる本発明の水処理システムを用いる水処理方法である。 The water treatment method of the present invention is a water treatment method using the water treatment system of the present invention.

本発明方法の一態様では、前記ユースポイントからの排出水の一部を前記予備水処理設備にて処理し、該予備水処理設備の処理水を前記用水処理設備又はユースポイントに返送する。 In one aspect of the method of the present invention, a part of the discharged water from the use point is treated by the reserve water treatment facility, and the treated water of the reserve water treatment facility is returned to the water treatment facility or the use point.

本発明方法の一態様では、前記配管からの排出水の一部を前記予備水処理設備にて処理し、該予備水処理設備の処理水を前記用水処理設備又はユースポイントに返送する。 In one aspect of the method of the present invention, a part of the discharged water from the pipe is treated by the reserve water treatment facility, and the treated water of the reserve water treatment facility is returned to the water treatment facility or the use point.

本発明方法の一態様では、前記ユースポイントからの排出水の一部を分岐させ、この分岐させた水の一部を前記用水処理設備に返送し、分岐させた水の残部を前記予備水処理設備にて処理し、該予備水処理設備の処理水を前記用水処理設備又はユースポイントに返送する。 In one aspect of the method of the present invention, a part of the discharged water from the use point is branched, a part of the branched water is returned to the water treatment facility, and the rest of the branched water is treated with the preliminary water. It is treated by the equipment and the treated water of the reserve water treatment equipment is returned to the water treatment equipment or the use point.

本発明方法の一態様では、前記排水処理設備からの排出水の一部を分岐させ、この分岐させた水の一部を前記用水処理設備に返送し、分岐させた水の残部を前記予備水処理設備にて処理し、該予備水処理設備の処理水を前記用水処理設備又はユースポイントに返送する。 In one aspect of the method of the present invention, a part of the discharged water from the wastewater treatment facility is branched, a part of the branched water is returned to the water treatment facility, and the rest of the branched water is the reserve water. It is treated by the treatment facility and the treated water of the reserve water treatment facility is returned to the water treatment facility or the use point.

本発明の水処理システムは、用水処理設備を有する主系列に対し組み込み可能な、且つ該用水処理設備と略同一構成の予備水処理設備を備えている。この予備水処理設備を、要求に応じて、用水処理、排水回収処理、予備待機のように使い分けることができる。 The water treatment system of the present invention includes a reserve water treatment facility that can be incorporated into a main series having a water treatment facility and has substantially the same configuration as the water treatment facility. This reserve water treatment facility can be used properly as a water treatment, a wastewater recovery treatment, and a preliminary standby, depending on the request.

実施の形態に係る水処理システムの構成図である。It is a block diagram of the water treatment system which concerns on embodiment. 実施の形態に係る水処理システムの構成図である。It is a block diagram of the water treatment system which concerns on embodiment. 実施の形態に係る水処理システムの構成図である。It is a block diagram of the water treatment system which concerns on embodiment. 実施の形態に係る水処理システムの構成図である。It is a block diagram of the water treatment system which concerns on embodiment. 実施の形態に係る水処理システムの構成図である。It is a block diagram of the water treatment system which concerns on embodiment. 実施の形態に係る水処理システムの構成図である。It is a block diagram of the water treatment system which concerns on embodiment. 実施の形態に係る水処理システムの構成図である。It is a block diagram of the water treatment system which concerns on embodiment. 実施の形態に係る水処理システムの構成図である。It is a block diagram of the water treatment system which concerns on embodiment.

図1は実施の形態に係る水処理システムの構成を示している。この水処理システムでは、原水を配管1を介して用水処理設備2に供給して処理して生産水とし、この生産水を配管3を介してユースポイント4に送水する。ユースポイント4で使用された水を配管5を介して排水処理設備6に供給して処理し、処理水を配管7から放流する。 FIG. 1 shows the configuration of the water treatment system according to the embodiment. In this water treatment system, raw water is supplied to the water treatment facility 2 via the pipe 1 and treated to be produced water, and the produced water is sent to the use point 4 via the pipe 3. The water used in the use point 4 is supplied to the wastewater treatment facility 6 via the pipe 5 for treatment, and the treated water is discharged from the pipe 7.

これらの配管1,3,5,7、用水処理設備2、ユースポイント4及び排水処理設備6よりなる主系列とは別に、該主系列に接続可能な予備水処理設備2Aが配備されている。 In addition to the main sequence consisting of these pipes 1, 3, 5, 7, the water treatment facility 2, the use point 4, and the wastewater treatment facility 6, a reserve water treatment facility 2A that can be connected to the main sequence is provided.

前記配管1,3,5,7には、予備水処理設備2Aを組み込むための配管接続部1a,3a,5a,7aが設けられている。予備水処理設備2Aの入口側は接続部1a,5a,7aに対し配管接続可能となっており、出口側は該接続部1a,3a,7aに対して配管接続可能となっている。 The pipes 1, 3, 5, and 7 are provided with pipe connection portions 1a, 3a, 5a, and 7a for incorporating the reserve water treatment facility 2A. The inlet side of the reserve water treatment equipment 2A can be connected to the connection portions 1a, 5a, 7a by piping, and the outlet side can be connected to the connection portions 1a, 3a, 7a by piping.

用水処理設備2及び予備水処理設備2Aは略同一構成のものである。用水処理設備2と予備水処理設備2Aとが略同一であるとは、各設備の主要な水処理機器の構成が同一であるか、又は一方の設備が他方の設備の主要な水処理機器をすべて備えると共にさらに他の水処理機器を備えることをいう。 The irrigation water treatment equipment 2 and the reserve water treatment equipment 2A have substantially the same configuration. The fact that the irrigation water treatment equipment 2 and the reserve water treatment equipment 2A are substantially the same means that the configurations of the main water treatment equipment of each equipment are the same, or that one equipment is the main water treatment equipment of the other equipment. It means to have all of them and to have other water treatment equipment.

この実施の形態では、用水処理設備2及び予備水処理設備2Aは、いずれも複数の水処理機器a,a,aを備えている。aは例えば凝集装置であり、aは除濁装置であり、aは脱塩装置である。 In this embodiment, the water treatment facility 2 and the reserve water treatment facility 2A each include a plurality of water treatment devices a 1 , a 2 , and a 3 . a 1 is, for example, a coagulation device, a 2 is a decontamination device, and a 3 is a desalination device.

除濁装置は、例えば以下のいずれかである。
・UF膜装置
・濾過器
・加圧浮上装置及びその後段の濾過器
・加圧浮上装置及びその後段のUF膜装置
・沈殿装置及びその後段の濾過器
・沈殿装置及びその後段のUF膜装置
除濁装置としては、上記の中でも、除濁膜装置が好ましい。除濁膜装置は、クロスフロー方式のものであっても全量濾過方式のものであってもよい。
The decontamination device is, for example, one of the following.
-UF membrane device-filter-pressurized levitation device and subsequent stage filter-pressurized levitation device and subsequent stage UF membrane device-precipitator and subsequent stage filter / sedimentation device and subsequent stage UF membrane device removal Among the above, the turbidizer is preferably an ultrafiltration membrane device. The decontamination membrane device may be a cross-flow type or a total filtration type.

除濁膜による除濁処理工程は、通水、エアバブリング、逆洗、及び水張り工程を有することが好ましい。濾過通水時間は20〜40分(通常30分)、差圧(入口圧力−出口圧力)は0.02〜0.04MPa程度が好ましい。なお、差圧が0.07〜0.10MPaになったときには定置洗浄することが好ましい。除濁膜の材質は耐薬品性に優れるPVDFが好ましく、孔径は0.02μm以上が好ましい。 The decontamination treatment step using the dehumidifying membrane preferably includes water flow, air bubbling, backwashing, and water filling steps. The filtration water flow time is preferably 20 to 40 minutes (usually 30 minutes), and the differential pressure (inlet pressure-outlet pressure) is preferably about 0.02 to 0.04 MPa. When the differential pressure reaches 0.07 to 0.10 MPa, it is preferable to perform clean-in-place cleaning. The material of the dehumidifying film is preferably PVDF having excellent chemical resistance, and the pore size is preferably 0.02 μm or more.

脱塩装置としてはRO膜装置、電気透析装置等が好適である。脱塩装置としては、イオン交換樹脂を用いるイオン交換樹脂塔や電気再生式脱イオン装置も用いることが可能であるが、排水処理に使用したものを用水処理に用いる場合のコンディショニングが大変なので、RO膜装置又は電気透析装置の方が好適である。ただし、RO膜装置等の後段側に電気脱イオン装置やイオン交換樹脂塔を設置してもよい。 As the desalting apparatus, an RO membrane apparatus, an electrodialysis apparatus and the like are suitable. As the desalination device, an ion exchange resin tower using an ion exchange resin or an electrodialyzed deionizer can also be used, but since it is difficult to condition the one used for wastewater treatment for water treatment, RO A membrane device or an electrodialysis device is more preferable. However, an electrodeionizer or an ion exchange resin tower may be installed on the rear side of the RO membrane device or the like.

脱塩装置としては、上記の中でもRO膜装置が好ましい。この場合、ライン量は3.6m/h以上を確保することが好ましい。 Among the above, the RO membrane device is preferable as the desalting device. In this case, it is preferable to secure a line amount of 3.6 m 3 / h or more.

逆浸透膜に制限はない。標準圧力0.735MPaの超低圧膜を採用することも可能である。膜面積は35〜41m程度が好ましく、0.735MPaでの初期純水フラックス:1.0m/d(25℃)以上程度、初期脱塩率:98%以上であることが好ましい。 There are no restrictions on the reverse osmosis membrane. It is also possible to use an ultra-low pressure film with a standard pressure of 0.735 MPa. The membrane area is preferably about 35 to 41 m 2 , the initial pure water flux at 0.735 MPa: about 1.0 m / d (25 ° C.) or more, and the initial desalting rate: 98% or more.

カルシウム硬度ランゲリア指数が0以下となるように回収率を設定することが好ましい。 It is preferable to set the recovery rate so that the calcium hardness Langeria index is 0 or less.

シリカはブライン水が溶解度以内となるように回収率を設定することが好ましい。回収率は50〜80%が通常である。 It is preferable to set the recovery rate of silica so that the brine water is within the solubility. The recovery rate is usually 50 to 80%.

RO膜のファウリングを防止するために、原水にスライムコントロール剤を添加してもよい。スライムコントロール剤としては、クロラミンやクロロスフファミン酸ナトリウムといった結合塩素系酸化剤でもイソチアゾロン系化合物でも構わない。スライムコントロール剤は、1種類単独で用いてもよく、2種類以上組み合わせて用いてもよい。 A slime control agent may be added to the raw water to prevent fouling of the RO membrane. The slime control agent may be a bound chlorine-based oxidizing agent such as chloramine or sodium chlorosfufamate, or an isothiazolone-based compound. The slime control agent may be used alone or in combination of two or more.

結合塩素系酸化剤の場合0.3〜1.0mg/L as Clとなるように添加することが好ましい。 In the case of a bound chlorine-based oxidizing agent, it is preferable to add it so as to be 0.3 to 1.0 mg / La as Cl 2.

クロロスフファミン酸ナトリウム酸化剤としては、例えば有効塩素濃度1〜8重量%、好ましくは3〜6重量%の塩素系酸化剤と、1.5〜9重量%、好ましくは4.5〜8重量%のスルファミン酸化合物を含む、pH≧12の水溶液を用いることができる。 Examples of the sodium chlorosulfamate oxidant include a chlorine-based oxidant having an effective chlorine concentration of 1 to 8% by weight, preferably 3 to 6% by weight, and 1.5 to 9% by weight, preferably 4.5 to 8% by weight. An aqueous solution having a pH of ≧ 12 containing% sulfamic acid compound can be used.

その他、スケール分散剤を添加してもよい。 In addition, a scale dispersant may be added.

なお、用水処理設備2及び予備水処理設備2Aには、除濁装置や脱塩装置からの逆洗排水、濃縮排水(引抜汚泥も含む)を排出するための排出部dが設けられる。 The water treatment facility 2 and the reserve water treatment facility 2A are provided with a discharge unit d for discharging backwash drainage and concentrated wastewater (including drawn sludge) from the decontamination device and the desalination device.

平常時は、図1の通り、予備水処理設備2Aを組み込まない主系列を用いて生産水の製造及びユースポイント排出水の処理を行う。なお、主系列の用水処理設備2の修理等の時には、用水処理設備2と予備水処理設備2Aとを入れ替えることができる。 In normal times, as shown in FIG. 1, production water is produced and use point discharged water is treated using a main sequence that does not incorporate the reserve water treatment facility 2A. When repairing the main sequence water treatment equipment 2, the water treatment equipment 2 and the reserve water treatment equipment 2A can be replaced.

排水の回収時、ユースポイントでの水需要量の増大時、原水の取水制限時、排水処理設備の能力低下時等には、予備水処理設備2Aを主系列に組み込み、予備水処理設備2Aによっても水処理を行う。 When collecting wastewater, increasing water demand at use points, restricting the intake of raw water, reducing the capacity of wastewater treatment equipment, etc., the reserve water treatment equipment 2A is incorporated into the main series, and the reserve water treatment equipment 2A is used. Also treats water.

予備水処理設備2Aの接続は、例えば、以下のいずれかによって行われる。
・主系列側から通水配管を外し、予備水処理設備2Aを主系列の近くに移動させ、通水配管を接続する。
・主系列側から通水配管を外し、予備水処理設備2A側に通水配管を接続し替える。
・予め用水処理設備2側及び排水処理設備6側の両方と、予備水処理設備2Aとを通水配管で図示しない弁等により切替え可能に接続しておき、通水方向を切替える。
The connection of the reserve water treatment facility 2A is performed by, for example, one of the following.
-Remove the water flow pipe from the main sequence side, move the reserve water treatment equipment 2A closer to the main series, and connect the water flow pipe.
-Remove the water flow pipe from the main sequence side and reconnect the water flow pipe to the reserve water treatment equipment 2A side.
-Both the water treatment equipment 2 side and the wastewater treatment equipment 6 side and the reserve water treatment equipment 2A are connected in advance by a valve or the like (not shown) with a water flow pipe to switch the water flow direction.

排水処理に使用した共通水処理ユニットを用水処理や排水回収に使用するべく通水を切替える時は、事前に機能材が汚れているか確認し、汚れていれば系内洗浄する。その後、処理水質が目標達成することを確認して予備コンディショニングを完了して通水開始する。 When switching the water flow to use the common water treatment unit used for wastewater treatment for water treatment and wastewater recovery, check in advance whether the functional material is dirty, and if it is dirty, clean the inside of the system. After that, after confirming that the treated water quality achieves the target, preliminary conditioning is completed and water flow is started.

予備水処理設備2Aを組み込んだ例を図2〜12に示す。 An example in which the reserve water treatment facility 2A is incorporated is shown in FIGS. 2 to 12.

図2及び図3は排水処理設備6からの処理水の一部を回収するために予備水処理設備2Aを組み込んだ例を示している。 2 and 3 show an example in which the reserve water treatment facility 2A is incorporated in order to recover a part of the treated water from the wastewater treatment facility 6.

図2aでは、ユースポイント4の流出水の一部を配管5から配管10によって予備水処理設備2Aの入口側に供給し、その処理水を配管11によって配管1に返送し、原水と共に用水処理設備2に送水する。 In FIG. 2a, a part of the outflow water of the use point 4 is supplied from the pipe 5 to the inlet side of the reserve water treatment equipment 2A by the pipe 10, the treated water is returned to the pipe 1 by the pipe 11, and the water treatment equipment is used together with the raw water. Send water to 2.

図2bでは、ユースポイント4の流出水の一部を配管5から配管10によって予備水処理設備2Aの入口側に供給する。該予備水処理設備2Aの処理水(生産水)の水質が良好であるため、該処理水(生産水)を配管1ではなく配管3に返送し、用水処理設備2からの生産水と共に、ユースポイント4に送水する。 In FIG. 2b, a part of the outflow water of the use point 4 is supplied from the pipe 5 to the inlet side of the reserve water treatment facility 2A by the pipe 10. Since the quality of the treated water (produced water) of the reserve water treatment facility 2A is good, the treated water (produced water) is returned to the pipe 3 instead of the pipe 1 and used together with the produced water from the water treatment facility 2. Water is sent to point 4.

図2a,図2bのその他の構成は図1と同じである。この図2a,図2bは、ユースポイント4の流出水の清浄度が比較的高い場合に採用される。 Other configurations of FIGS. 2a and 2b are the same as those of FIG. 2a and 2b are adopted when the cleanliness of the effluent of use point 4 is relatively high.

ユースポイント流出水の清浄度が低い場合には、図3a,3bの通り、排水処理設備6の処理水の一部を配管7から配管10を介して予備水処理設備2Aの入口側に送水する。予備水処理設備2Aの処理水(生産水)の水質が低いときには、図3aの通り、該処理水を配管1に返送し、水質が良好であるときには、図3bの通り、該処理水を配管3に返送する。 Use point When the cleanliness of the effluent is low, as shown in FIGS. 3a and 3b, a part of the treated water of the wastewater treatment equipment 6 is sent from the pipe 7 to the inlet side of the reserve water treatment equipment 2A via the pipe 10. .. When the quality of the treated water (produced water) of the reserve water treatment facility 2A is low, the treated water is returned to the pipe 1 as shown in FIG. 3a, and when the water quality is good, the treated water is piped as shown in FIG. 3b. Return to 3.

図3a,3bのその他の構成は図2a,2bと同一である。 Other configurations of FIGS. 3a and 3b are the same as those of FIGS. 2a and 2b.

図4,5は、原水の取水が制限され、原水の流量が少なくなったために、排水回収量を多くした場合の例を示している。例えば、通常は原水の取水許容量の70%を取水していたが、渇水による取水制限により取水許容量の50%に制限された場合、不足分の20%を排水回収水で補う。図4,5では、排水回収量を多くしたので、回収排水の一部を予備水処理設備2Aで処理し、残部を配管1に返送している。 FIGS. 4 and 5 show an example in which the amount of wastewater recovered is increased because the intake of raw water is restricted and the flow rate of raw water is reduced. For example, normally 70% of the permissible amount of raw water is taken in, but when the water intake is restricted to 50% due to drought, 20% of the shortfall is supplemented with wastewater recovered water. In FIGS. 4 and 5, since the amount of wastewater recovered was increased, a part of the recovered wastewater was treated by the reserve water treatment facility 2A, and the rest was returned to the pipe 1.

すなわち、図4aは、図2bにおいて、配管5から配管10に分岐させたユースポイント流出水の一部を予備水処理設備2Aで処理し、残部を、配管10から分岐した配管12を介して配管1に返送する。この場合、予備水処理設備2Aの処理水(生産水)の水質が良好であるときには、該処理水(生産水)を配管11によって配管3に返送する。図4aのその他の構成は図2bと同一である。 That is, in FIG. 4a, in FIG. 2b, a part of the use point outflow water branched from the pipe 5 to the pipe 10 is treated by the reserve water treatment facility 2A, and the rest is piped through the pipe 12 branched from the pipe 10. Return to 1. In this case, when the quality of the treated water (produced water) of the reserve water treatment facility 2A is good, the treated water (produced water) is returned to the pipe 3 by the pipe 11. Other configurations of FIG. 4a are the same as those of FIG. 2b.

図4bは、図4aにおいて、予備水処理設備2Aからの処理水の水質が劣る場合である。この場合は、予備水処理設備2Aの処理水を配管11によって分岐配管12からのユースポイント流出水と合流させ、合流配管13を介して配管1に返送する。図4bのその他の構成は図4aと同一である。 FIG. 4b shows a case where the quality of the treated water from the reserve water treatment facility 2A is inferior in FIG. 4a. In this case, the treated water of the reserve water treatment facility 2A is merged with the use point outflow water from the branch pipe 12 by the pipe 11, and is returned to the pipe 1 via the merging pipe 13. Other configurations of FIG. 4b are the same as those of FIG. 4a.

図4a,4bでは、ユースポイント4の流出水の水質が比較的良好であるので、ユースポイント流出水を予備水処理設備2Aに送水しているが、ユースポイント流出水の水質が比較的劣る場合には、図5a,5bの通り、排水処理設備6の処理水の一部を配管7から配管10に分岐させる。図5aのその他の構成は図4aと同一であり、図5bのその他の構成は図4bと同一である。 In FIGS. 4a and 4b, since the quality of the effluent of use point 4 is relatively good, the effluent of use point is sent to the reserve water treatment facility 2A, but the quality of the effluent of use point is relatively inferior. As shown in FIGS. 5a and 5b, a part of the treated water of the wastewater treatment facility 6 is branched from the pipe 7 to the pipe 10. The other configurations of FIG. 5a are the same as those of FIG. 4a, and the other configurations of FIG. 5b are the same as those of FIG. 4b.

図6は、排水処理設備6に不調が生じたために、ユースポイント4の流出水の一部を配管10に分岐させて予備水処理設備2Aに供給するようにしたものである。図6aのその他の構成は図4aと同一であり、図6bのその他の構成は図4bと同一である。 FIG. 6 shows that a part of the effluent from the use point 4 is branched into the pipe 10 and supplied to the reserve water treatment facility 2A due to a malfunction in the wastewater treatment facility 6. The other configurations of FIG. 6a are the same as those of FIG. 4a, and the other configurations of FIG. 6b are the same as those of FIG. 4b.

上記図1〜6では、用水処理設備2は単独で設置されているが、用水処理設備2と並列に、それと同一構成の用水処理設備を設置してもよい。 In FIGS. 1 to 6 above, the water treatment facility 2 is installed independently, but a water treatment facility having the same configuration as the water treatment facility 2 may be installed in parallel with the water treatment facility 2.

図7は、図1での運転中に、ユースポイント4での水需要量が増大した場合に、用水処理の処理水(生産水)の水量を確保する例を示している。
図7では、原水の一部を配管1から配管12を通じて予備水処理設備2Aの入口側に供給し、その処理水(生産水)を配管13を通じて配管3に返送し、用水処理設備2からの生産水と共に、ユースポイント4に送水する。
図7のその他の構成は図1と同じである。
なお図7は、原水水質が悪化した場合、特に豪雨などで濁度が上昇した場合に、用水処理設備の1台あたりの負荷を下げるためにも適用することができる。
FIG. 7 shows an example of securing the amount of treated water (produced water) for irrigation treatment when the amount of water demand at use point 4 increases during the operation of FIG.
In FIG. 7, a part of the raw water is supplied from the pipe 1 to the inlet side of the reserve water treatment equipment 2A through the pipe 12, and the treated water (produced water) is returned to the pipe 3 through the pipe 13 from the water treatment equipment 2. It is sent to use point 4 together with the produced water.
Other configurations of FIG. 7 are the same as those of FIG.
Note that FIG. 7 can also be applied to reduce the load per unit of the irrigation water treatment equipment when the quality of raw water deteriorates, especially when the turbidity increases due to heavy rain or the like.

図8は、原水水質が悪化した場合、特に河川の渇水で海水が河川に逆流してイオン強度が上昇した場合や、井戸に地表の落ち葉由来の腐植物質が流れ込むなどしてTOCが上昇した場合に、用水処理の処理水の水質を確保する例を示している。
図8では、原水の少なくとも一部を配管1から配管12を通じて予備水処理設備2Aの入口側に供給し、その処理水を配管14を通じて配管1の上記分岐点と用水処理設備2の入口側の間に返送する。
図8のその他の構成は図1と同じである。
原水負荷が高い場合ほど、予備水処理設備2Aへの流量比を高くすることが望ましい。
FIG. 8 shows the case where the raw water quality deteriorates, especially when the seawater flows back into the river due to the drought of the river and the ionic strength increases, or when the humus derived from the fallen leaves on the ground surface flows into the well and the TOC increases. Shows an example of ensuring the quality of treated water for water treatment.
In FIG. 8, at least a part of the raw water is supplied from the pipe 1 to the inlet side of the reserve water treatment facility 2A through the pipe 12, and the treated water is supplied through the pipe 14 to the branch point of the pipe 1 and the inlet side of the irrigation water treatment facility 2. I will return it in the meantime.
Other configurations of FIG. 8 are the same as those of FIG.
It is desirable that the higher the raw water load, the higher the flow rate ratio to the reserve water treatment facility 2A.

なお、本発明では、用水処理設備2の前段で原水を前処理してもよい。 In the present invention, the raw water may be pretreated in the front stage of the water treatment facility 2.

本発明は、上記実施の形態に限定されるものではなく、さらに他の態様とされてもよい。 The present invention is not limited to the above-described embodiment, and may be further used.

2 用水処理設備
2A 予備水処理設備
4 ユースポイント
6 排水処理設備
2 Water treatment equipment 2A Reserve water treatment equipment 4 Use points 6 Wastewater treatment equipment

Claims (8)

原水を処理する用水処理設備を備えた主系列を有する水処理システムにおいて、
該用水処理設備と略同一構成の予備水処理設備を備えており、
該予備水処理設備が該主系列に組み込み可能となっていることを特徴とする水処理システム。
In a water treatment system with a main sequence equipped with water treatment equipment for treating raw water
It is equipped with a reserve water treatment facility that has substantially the same configuration as the water treatment facility.
A water treatment system characterized in that the reserve water treatment equipment can be incorporated into the main sequence.
前記用水処理設備及び予備水処理設備は、少なくとも、凝集装置、除濁装置及び脱塩装置を有することを特徴とする請求項1の水処理システム。 The water treatment system according to claim 1, wherein the water treatment equipment and the reserve water treatment equipment include at least a coagulation device, a decontamination device, and a desalination device. 前記主系列は、第1配管によって原水が供給される前記用水処理設備と、該用水処理設備からの処理水が第2配管によって供給されるユースポイントと、該ユースポイントからの排出水が第3配管によって供給される排水処理設備と、該排水処理設備の流出水を流すための第4配管とを備えていることを特徴とする請求項1又は2の水処理システム。 In the main series, the irrigation water treatment facility to which raw water is supplied by the first pipe, the use point to which the treated water from the irrigation water treatment facility is supplied by the second pipe, and the discharge water from the use point are the third. The water treatment system according to claim 1 or 2, further comprising a wastewater treatment facility supplied by a pipe and a fourth pipe for flowing outflow water of the wastewater treatment facility. 前記第1、第2、第3及び第4配管に、それぞれ、配管接続部が設けられていることを特徴とする請求項3の水処理システム。 The water treatment system according to claim 3, wherein each of the first, second, third, and fourth pipes is provided with a pipe connection portion. 請求項3又は4の水処理システムを用いる水処理方法であって、
前記ユースポイントからの排出水の一部を前記予備水処理設備にて処理し、該予備水処理設備の処理水を前記用水処理設備又はユースポイントに返送することを特徴とする水処理方法。
A water treatment method using the water treatment system according to claim 3 or 4.
A water treatment method characterized in that a part of the discharged water from the use point is treated by the reserve water treatment facility, and the treated water of the reserve water treatment facility is returned to the water treatment facility or the use point.
請求項3又は4の水処理システムを用いる水処理方法であって、
前記排水処理設備からの排出水の一部を前記予備水処理設備にて処理し、該予備水処理設備の処理水を前記用水処理設備又はユースポイントに返送することを特徴とする水処理方法。
A water treatment method using the water treatment system according to claim 3 or 4.
A water treatment method characterized in that a part of the discharged water from the wastewater treatment facility is treated by the reserve water treatment facility, and the treated water of the reserve water treatment facility is returned to the water treatment facility or a use point.
請求項3又は4の水処理システムを用いる水処理方法であって、
前記ユースポイントからの排出水の一部を分岐させ、この分岐させた水の一部を前記用水処理設備に返送し、分岐させた水の残部を前記予備水処理設備にて処理し、該予備水処理設備の処理水を前記用水処理設備又はユースポイントに返送することを特徴とする水処理方法。
A water treatment method using the water treatment system according to claim 3 or 4.
A part of the discharged water from the use point is branched, a part of the branched water is returned to the water treatment facility, and the rest of the branched water is treated by the reserve water treatment facility to prepare the reserve. A water treatment method characterized in that the treated water of a water treatment facility is returned to the water treatment facility or a point of use.
請求項3又は4の水処理システムを用いる水処理方法であって、
前記排水処理設備からの排出水の一部を分岐させ、この分岐させた水の一部を前記用水処理設備に返送し、分岐させた水の残部を前記予備水処理設備にて処理し、該予備水処理設備の処理水を前記用水処理設備又はユースポイントに返送することを特徴とする水処理方法。
A water treatment method using the water treatment system according to claim 3 or 4.
A part of the discharged water from the wastewater treatment facility is branched, a part of the branched water is returned to the water treatment facility, and the rest of the branched water is treated by the reserve water treatment facility. A water treatment method characterized in that the treated water of the reserve water treatment facility is returned to the water treatment facility or the point of use.
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