JP2015054302A - Water treatment apparatus - Google Patents

Water treatment apparatus Download PDF

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JP2015054302A
JP2015054302A JP2013190264A JP2013190264A JP2015054302A JP 2015054302 A JP2015054302 A JP 2015054302A JP 2013190264 A JP2013190264 A JP 2013190264A JP 2013190264 A JP2013190264 A JP 2013190264A JP 2015054302 A JP2015054302 A JP 2015054302A
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ion exchange
treatment
chamber
water
filtration
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JP6196507B2 (en
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雄一 根本
Yuichi Nemoto
雄一 根本
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Maezawa Industries Inc
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  • Water Treatment By Sorption (AREA)
  • Filtering Materials (AREA)
  • Treatment Of Water By Ion Exchange (AREA)
  • Removal Of Specific Substances (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a water treatment apparatus capable of performing continuously the ion exchange treatment by ion exchange resin and the filtration treatment by filtration material while aiming the downsizing and simplification of the apparatus.SOLUTION: The water treatment apparatus is constructed by partitioning the inside of a treatment tank 12 into an ion exchange treatment chamber 15 and a filtration chamber 16 by a partition wall 14 having an overflow section 13. The ion exchange treatment chamber comprises a raw-water inlet portion 18 and an agitator 19 in the lower section, and the filtration chamber comprises a filtration-material layer 20 in the middle section and a treatment-water outlet portion 21 in the lower section. The ion exchange treatment chamber performs the ion exchange treatment during the course of upward flow, and the filtration chamber performs the filtration treatment to the ion exchanged treatment-water entering from the ion exchange treatment chamber during the course of downward flow.

Description

本発明は、水処理装置に関し、詳しくは、イオン交換処理とろ過処理とを含む水処理装置に関する。   The present invention relates to a water treatment device, and more particularly to a water treatment device including an ion exchange treatment and a filtration treatment.

カビ臭などの臭気物質やトリハロメタンの生成原因などとなる溶解性有機成分を含む原水を処理するための水処理装置として、原水に粉末状の活性炭及び粉末状のイオン交換樹脂を同時に混合し、前記臭気物質や溶解性有機成分を活性炭やイオン交換樹脂に吸着させた後、固液分離手段で活性炭及びイオン交換樹脂を固液分離することにより、臭気物質や溶解性有機成分を除去した処理水を得る水処理装置が知られている(例えば、特許文献1参照。)。   As a water treatment device for treating raw water containing soluble organic components that cause generation of odorous substances such as mold odor and trihalomethane, powdered activated carbon and powdered ion exchange resin are mixed simultaneously with raw water, After adsorbing odorous substances and soluble organic components to activated carbon and ion exchange resin, the treated water from which odorous substances and soluble organic components have been removed is obtained by solid-liquid separation of activated carbon and ion exchange resin by solid-liquid separation means. An obtained water treatment apparatus is known (for example, refer to Patent Document 1).

特開2011−230038号公報JP 2011-230038 A

しかし、特許文献1に記載されたような水処理装置では、活性炭及びイオン交換樹脂を混合するための混合槽と、これらを分離するための分離槽とを別個に設けて配管などで接続しているため、初期コストが嵩んだり、広い設置スペースを必要としたりするなどの問題があった。   However, in the water treatment apparatus as described in Patent Document 1, a mixing tank for mixing the activated carbon and the ion exchange resin and a separation tank for separating them are separately provided and connected by piping or the like. Therefore, there are problems such as an increase in initial cost and a need for a large installation space.

そこで本発明は、装置の小型化や簡略化を図りながら、イオン交換樹脂によるイオン交換処理とろ材によるろ過処理とを連続して行うことができる水処理装置を提供することを目的としている。   Then, this invention aims at providing the water treatment apparatus which can perform continuously the ion exchange process by an ion exchange resin, and the filtration process by a filter medium, aiming at size reduction and simplification of an apparatus.

上記目的を達成するため、本発明の水処理装置は、処理槽の内部を、仕切壁によってイオン交換処理室とろ過室とに区画し、前記イオン交換処理室は、該処理室の下部に原水を導入する原水導入部と、原水とイオン交換樹脂とを混合する撹拌機とを備え、前記ろ過室は、中段部に設けられたろ材層と、該ろ材層の下方に設けられた処理水導出部とを備え、前記イオン交換処理室は、上向流にて原水とイオン交換樹脂とを接触させ、前記ろ過室は、イオン交換処理室の上部からろ過室の上部に流入したイオン交換処理水に対して下向流にてろ過処理を行うことを特徴としている。   In order to achieve the above object, the water treatment apparatus of the present invention divides the inside of a treatment tank into an ion exchange treatment chamber and a filtration chamber by a partition wall, and the ion exchange treatment chamber has raw water in the lower part of the treatment chamber. And a stirrer for mixing the raw water and the ion exchange resin, and the filtration chamber is provided with a filter medium layer provided in the middle stage, and a treated water lead provided under the filter medium layer. The ion exchange treatment chamber makes the raw water and the ion exchange resin contact in an upward flow, and the filtration chamber flows from the upper part of the ion exchange treatment chamber into the upper part of the filtration chamber. In contrast, it is characterized in that filtration is performed in a downward flow.

さらに、本発明の水処理装置は、前記仕切壁の上部に、イオン交換処理水をイオン交換処理室からろ過室に流入させる越流部又は通水孔が設けられていること、また、前記ろ材層のろ材が、珪砂、粒状活性炭、アンスラサイト、マンガン砂、接触ろ材の少なくともいずれか1種を含んでいることを特徴としている。   Furthermore, the water treatment apparatus of the present invention is provided with an overflow portion or a water passage hole for allowing ion exchange treated water to flow from the ion exchange treatment chamber into the filtration chamber at the upper portion of the partition wall, and the filter medium. The filter medium of the layer is characterized by containing at least one of quartz sand, granular activated carbon, anthracite, manganese sand, and contact filter medium.

本発明の水処理装置によれば、処理槽の内部を仕切壁によってイオン交換処理室とろ過室とに区画しているので、水処理装置の小型化や簡略化を図りながら、イオン交換樹脂によるイオン交換処理とろ材によるろ過処理とを連続して行うことができる。   According to the water treatment device of the present invention, the interior of the treatment tank is partitioned into an ion exchange treatment chamber and a filtration chamber by a partition wall, so that the water treatment device can be downsized and simplified while using an ion exchange resin. The ion exchange treatment and the filtration treatment with the filter medium can be performed continuously.

本発明の水処理装置の一形態例を示す説明図である。It is explanatory drawing which shows one example of the water treatment apparatus of this invention.

本形態例に示す水処理装置11は、処理槽12の内部を、上部に越流部13を有する仕切壁14により、イオン交換処理室15とろ過室16とに区画し、イオン交換処理室15では、上向流にて原水とイオン交換樹脂とを接触させてイオン交換処理を行い、前記ろ過室16では、下向流にてろ材によるろ過処理を行うように形成されている。   The water treatment apparatus 11 shown in the present embodiment divides the inside of the treatment tank 12 into an ion exchange treatment chamber 15 and a filtration chamber 16 by a partition wall 14 having an overflow portion 13 at the upper portion, and the ion exchange treatment chamber 15. Then, the raw water and the ion exchange resin are brought into contact with each other in an upward flow to perform an ion exchange treatment, and the filtration chamber 16 is configured to perform a filtration treatment with a filter medium in a downward flow.

イオン交換処理室15の下部には、原水導入経路17から供給される原水を槽下部に導入する原水導入部18が設けられるとともに、槽内の原水を撹拌して原水とイオン交換樹脂とを効果的に混合して接触させるための撹拌機19が設けられている。   A lower part of the ion exchange treatment chamber 15 is provided with a raw water introduction part 18 for introducing the raw water supplied from the raw water introduction path 17 into the lower part of the tank, and the raw water in the tank is stirred to effect the raw water and the ion exchange resin. A stirrer 19 is provided for mixing and contacting.

ろ過室16の中段部には、原水の処理目的に応じたろ材を充填したろ材層20が設けられており、ろ材層20の下方には、ろ過処理を行った処理水を導出する処理水導出部21が設けられている。   The middle part of the filtration chamber 16 is provided with a filter medium layer 20 filled with a filter medium in accordance with the purpose of the raw water treatment. Under the filter medium layer 20, a treated water derivation for deriving treated water that has been subjected to the filtration process is provided. A portion 21 is provided.

また、本形態例に示す水処理装置11では、原水の流入量、イオン交換処理室15の断面積及び高さ、撹拌機19の撹拌強度を適宜設定することにより、撹拌機19の撹拌作用が及ばないイオン交換処理室15の上部に、該イオン交換処理室15の上部を上昇する水中から、水より比重が大きなイオン交換樹脂をイオン交換処理室15の下部に向けて沈降させるイオン交換樹脂沈降部22を形成している。   Moreover, in the water treatment apparatus 11 shown in this embodiment, the stirring action of the stirrer 19 is appropriately set by appropriately setting the inflow amount of raw water, the cross-sectional area and height of the ion exchange treatment chamber 15, and the stirring strength of the stirrer 19. Ion exchange resin sedimentation in which an ion exchange resin having a specific gravity greater than that of water is settled toward the lower portion of the ion exchange treatment chamber 15 from the water rising above the ion exchange treatment chamber 15 at the upper portion of the ion exchange treatment chamber 15 that does not reach A portion 22 is formed.

原水は、原水導入部18からイオン交換処理室15の下部に流入し、撹拌機19により撹拌され、イオン交換処理室15内にあらかじめ投入されているイオン交換樹脂と混合、接触する。イオン交換樹脂と接触してイオン交換処理されたイオン交換処理水は、撹拌機19で撹拌された状態でイオン交換処理室15内を上昇し、撹拌力が弱くなったイオン交換処理室15の上部のイオン交換樹脂沈降部22では、所定の速度で上昇するイオン交換処理水の流れに逆らってイオン交換樹脂がイオン交換処理室15の底部に向かって沈降する状態になる。イオン交換処理室15の最上部に上昇したイオン交換処理水は、越流部13を越えてろ過室16の上部に流入し、下向流でろ材層20を通り、所定のろ過処理が行われた後、下部の処理水導出部21から取り出される。   The raw water flows into the lower part of the ion exchange treatment chamber 15 from the raw water introduction part 18, is agitated by the agitator 19, and mixes with and comes into contact with the ion exchange resin previously put in the ion exchange treatment chamber 15. The ion exchange treated water that has been subjected to the ion exchange treatment in contact with the ion exchange resin ascends in the ion exchange treatment chamber 15 while being stirred by the stirrer 19, and the upper portion of the ion exchange treatment chamber 15 in which the stirring force is weakened. In the ion exchange resin sedimentation section 22, the ion exchange resin settles toward the bottom of the ion exchange treatment chamber 15 against the flow of ion exchange treatment water rising at a predetermined speed. The ion exchange treated water that has risen to the uppermost part of the ion exchange treatment chamber 15 passes through the overflow section 13 and flows into the upper portion of the filtration chamber 16, passes through the filter medium layer 20 in a downward flow, and undergoes a predetermined filtration treatment. After that, it is taken out from the lower treated water outlet 21.

このように、通水部として、上部に越流部13を有する仕切壁14を設けて一つの処理槽12をイオン交換処理室15とろ過室16とに区画することにより、色度や有機物などを除去する所定のイオン交換処理と、濁質や金属類の除去といった所定のろ過処理とを一つの処理槽12で行うことができ、水処理装置11の小型化を図ることができる。   Thus, by providing the partition wall 14 having the overflow portion 13 at the upper portion as a water flow portion and partitioning one treatment tank 12 into an ion exchange treatment chamber 15 and a filtration chamber 16, chromaticity, organic matter, etc. A predetermined ion exchange process for removing water and a predetermined filtration process such as removal of turbidity and metals can be performed in one treatment tank 12, and the water treatment apparatus 11 can be downsized.

また、イオン交換処理室15の上部にイオン交換樹脂沈降部22を形成することにより、イオン交換樹脂をイオン交換処理室15から流出させることなくイオン交換処理室15内に保持することができ、新たに流入する原水と接触させることができるので、イオン交換樹脂が備えるイオン交換能力を十分に活用することができる。これにより、イオン交換樹脂の使用量を削減できるとともに、イオン交換樹脂を再生するための薬剤の使用量も削減でき、イオン交換樹脂を再生する際に発生する再生廃液の量も低減することができる。   Moreover, by forming the ion exchange resin sedimentation part 22 in the upper part of the ion exchange treatment chamber 15, the ion exchange resin can be held in the ion exchange treatment chamber 15 without flowing out of the ion exchange treatment chamber 15, Therefore, the ion exchange ability of the ion exchange resin can be fully utilized. Thereby, while being able to reduce the usage-amount of an ion exchange resin, the usage-amount of the chemical | medical agent for reproducing | regenerating an ion exchange resin can also be reduced, and the quantity of the regeneration waste liquid generate | occur | produced when reproducing | regenerating an ion exchange resin can also be reduced. .

一方、ろ過室16では、ろ材層20に用いるろ材として、原水の性状に応じて珪砂、粒状活性炭、アンスラサイト、マンガン砂、接触ろ材などを適宜使用することにより、カビ臭やアンモニア、マンガンなどの除去も行うことができる。   On the other hand, in the filtration chamber 16, as a filter medium used for the filter medium layer 20, silica sand, granular activated carbon, anthracite, manganese sand, contact filter medium, etc. are appropriately used according to the properties of raw water, so that mold odor, ammonia, manganese, etc. Removal can also be performed.

なお、イオン交換能力が低下したイオン交換樹脂は、イオン交換処理室の底部などの適宜な位置から抜き出すことにより、周知の再生方法で再生して再利用することができ、イオン交換処理室へのイオン交換樹脂の投入は、イオン交換処理室の上方から行うことができる。   In addition, the ion exchange resin with reduced ion exchange capacity can be regenerated and reused by a known regeneration method by being extracted from an appropriate position such as the bottom of the ion exchange treatment chamber. The ion exchange resin can be introduced from above the ion exchange treatment chamber.

また、イオン交換樹脂は、一般的に水より比重が大きいので、意識的にイオン交換樹脂沈降部を形成しなくても、越流部を越えてイオン交換処理室から流出するイオン交換樹脂の量は少量であり、越流部を越えてろ過室に流入しても、ろ材層の上に留まるので、処理水と共に処理水導出部から流出することはない。逆に、イオン交換処理室の上部に傾斜板を設けておくことにより、イオン交換樹脂の沈降を促進して越流部までイオン交換樹脂が上昇することを防止できる。   In addition, since ion exchange resin generally has a higher specific gravity than water, the amount of ion exchange resin that flows out of the ion exchange treatment chamber beyond the overflow section without intentionally forming the ion exchange resin sedimentation section. Is small, and even if it flows into the filtration chamber beyond the overflow section, it stays on the filter medium layer and therefore does not flow out from the treated water outlet section together with the treated water. Conversely, by providing an inclined plate in the upper part of the ion exchange treatment chamber, it is possible to prevent the ion exchange resin from rising to the overflow section by promoting the sedimentation of the ion exchange resin.

なお、本形態例では、イオン交換処理水をろ過室に流入させるために仕切壁の上部に越流部を設けたが、仕切壁の上部の適宜な位置に通水孔を設け、図1に矢印Wで示すように、この通水孔からろ過室へイオン交換処理水を流入させるようにしてもよい。   In this embodiment, an overflow portion is provided at the upper part of the partition wall in order to allow the ion exchange treated water to flow into the filtration chamber. However, a water flow hole is provided at an appropriate position on the upper part of the partition wall. As indicated by an arrow W, ion-exchanged water may be allowed to flow into the filtration chamber from this water passage hole.

11…水処理装置、12…処理槽、13…越流部、14…仕切壁、15…イオン交換処理室、16…ろ過室、17…原水導入経路、18…原水導入部、19…撹拌機、20…ろ材層、21…処理水導出部、22…イオン交換樹脂沈降部   DESCRIPTION OF SYMBOLS 11 ... Water treatment apparatus, 12 ... Treatment tank, 13 ... Overflow part, 14 ... Partition wall, 15 ... Ion exchange treatment room, 16 ... Filtration room, 17 ... Raw water introduction path, 18 ... Raw water introduction part, 19 ... Stirrer , 20 ... filter medium layer, 21 ... treated water lead-out part, 22 ... ion exchange resin sedimentation part

Claims (3)

処理槽の内部を、仕切壁によってイオン交換処理室とろ過室とに区画し、前記イオン交換処理室は、該処理室の下部に原水を導入する原水導入部と、原水とイオン交換樹脂とを混合する撹拌機とを備え、前記ろ過室は、中段部に設けられたろ材層と、該ろ材層の下方に設けられた処理水導出部とを備え、前記イオン交換処理室は、上向流にて原水とイオン交換樹脂とを接触させ、前記ろ過室は、イオン交換処理室の上部からろ過室の上部に流入したイオン交換処理水に対して下向流にてろ過処理を行うことを特徴とする水処理装置。   The interior of the treatment tank is partitioned into an ion exchange treatment chamber and a filtration chamber by a partition wall, and the ion exchange treatment chamber comprises a raw water introduction portion for introducing raw water into a lower portion of the treatment chamber, and raw water and an ion exchange resin. The filter chamber is provided with a filter medium layer provided in a middle stage part, and a treated water outlet part provided below the filter medium layer, and the ion exchange process chamber is an upward flow The raw water and the ion exchange resin are brought into contact with each other, and the filtration chamber performs a down-flow filtration process on the ion exchange treated water that has flowed into the upper portion of the filtration chamber from the upper portion of the ion exchange treatment chamber. Water treatment equipment. 前記仕切壁の上部に、イオン交換処理水をイオン交換処理室からろ過室に流入させる越流部又は通水孔が設けられていることを特徴とする請求項1記載の水処理装置。   The water treatment device according to claim 1, wherein an overflow portion or a water passage hole for allowing ion exchange treated water to flow from the ion exchange treatment chamber into the filtration chamber is provided at an upper portion of the partition wall. 前記ろ材層のろ材が、珪砂、粒状活性炭、アンスラサイト、マンガン砂、接触ろ材の少なくともいずれか1種を含んでいることを特徴とする請求項1又は2記載の水処理装置。   The water treatment device according to claim 1 or 2, wherein the filter medium in the filter medium layer contains at least one of silica sand, granular activated carbon, anthracite, manganese sand, and contact filter medium.
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KR20180040947A (en) * 2016-10-13 2018-04-23 주식회사유진케임텍 System for Waste water treatment and recycling by ion removal

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JPH09276861A (en) * 1996-04-12 1997-10-28 San Medical Kosan:Kk Water purifier fitted with water softener
JPH11197682A (en) * 1998-01-12 1999-07-27 Ebara Corp Granulated material for cleaning environment
JPH11244870A (en) * 1998-03-05 1999-09-14 Nkk Corp Flocculating and settling device for sewage and cleaning method thereof
JP2001137616A (en) * 1999-11-15 2001-05-22 Japan Organo Co Ltd Filter
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JPS547248U (en) * 1977-06-17 1979-01-18
JPH05509256A (en) * 1990-02-12 1993-12-22 ストランド,チャールス,ディー dual chamber water filter
JPH0657493U (en) * 1993-01-06 1994-08-09 英雄 大城 Ion exchange water purification device
JPH09276861A (en) * 1996-04-12 1997-10-28 San Medical Kosan:Kk Water purifier fitted with water softener
JPH11197682A (en) * 1998-01-12 1999-07-27 Ebara Corp Granulated material for cleaning environment
JPH11244870A (en) * 1998-03-05 1999-09-14 Nkk Corp Flocculating and settling device for sewage and cleaning method thereof
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180040947A (en) * 2016-10-13 2018-04-23 주식회사유진케임텍 System for Waste water treatment and recycling by ion removal
KR101889291B1 (en) * 2016-10-13 2018-08-21 주식회사 유진케임텍 System for Waste water treatment and recycling by ion removal

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