JP2009274006A - Wastewater treatment apparatus - Google Patents

Wastewater treatment apparatus Download PDF

Info

Publication number
JP2009274006A
JP2009274006A JP2008127229A JP2008127229A JP2009274006A JP 2009274006 A JP2009274006 A JP 2009274006A JP 2008127229 A JP2008127229 A JP 2008127229A JP 2008127229 A JP2008127229 A JP 2008127229A JP 2009274006 A JP2009274006 A JP 2009274006A
Authority
JP
Japan
Prior art keywords
water
stage
reverse osmosis
concentrated
osmosis 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.)
Pending
Application number
JP2008127229A
Other languages
Japanese (ja)
Inventor
Atsuyuki Manabe
敦行 真鍋
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.)
Miura Co Ltd
Original Assignee
Miura Co Ltd
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 Miura Co Ltd filed Critical Miura Co Ltd
Priority to JP2008127229A priority Critical patent/JP2009274006A/en
Publication of JP2009274006A publication Critical patent/JP2009274006A/en
Pending legal-status Critical Current

Links

Images

Abstract

<P>PROBLEM TO BE SOLVED: To provide a wastewater treatment apparatus which lowers a concentration of IPA of a water to be treated such as a cleaning wastewater to a lower concentration by using a reverse osmosis membrane apparatus and also reduces a volume of the wastewater. <P>SOLUTION: The waste water treatment apparatus includes a tank 1 for the water to be treated for storing the water to be treated, a first reverse osmosis membrane apparatus 10a which treats the water to be treated supplied from the tank 1 for the water to be treated and discharges it as a first step permeated water in which an impurity in the water to be treated is removed and the first step concentrated water in which the impurity is concentrated, a second reverse osmosis membrane apparatus 10b which receives the first step concentrated water and discharges it as a second-step permeated water in which the impurity in the first step concentrated water is removed and a second step concentrated water in which the impurity is concentrated, and a permeated-water recovering line 3 which recovers the second step permeated water into the tank 1 for the water to be treated. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、廃水処理装置に関し、特に、逆浸透膜装置を用いてイソプロピルアルコール(以下、IPAと称す)を含む洗浄廃水を処理する廃水処理装置に関する。   The present invention relates to a wastewater treatment apparatus, and more particularly to a wastewater treatment apparatus that treats cleaning wastewater containing isopropyl alcohol (hereinafter referred to as IPA) using a reverse osmosis membrane device.

近年、半導体製造におけるウェット洗浄プロセスにおける乾燥工程では、IPAが広く利用されており、使用されたIPAは、半導体ウエハのリンス廃水および半導体ウエハ上から除去された水分とともに洗浄廃水として排出されている。このIPAを含有する洗浄廃水に対しては、蒸留法によりIPAを回収することが行われているが、この方法は加熱エネルギーを必要とするため、洗浄廃水の量が増えるとそれだけコストがかる。そのため、蒸留を行う前に、逆浸透膜装置を用いた廃水処理装置においてIPAを含有する洗浄廃水を処理することが検討されている。   In recent years, IPA is widely used in a drying process in a wet cleaning process in semiconductor manufacturing, and the used IPA is discharged as cleaning waste water together with rinse waste water of the semiconductor wafer and moisture removed from the semiconductor wafer. With respect to the washing wastewater containing IPA, IPA is recovered by a distillation method. However, since this method requires heating energy, the cost increases as the amount of washing wastewater increases. For this reason, it has been studied to treat washing wastewater containing IPA in a wastewater treatment apparatus using a reverse osmosis membrane device before distillation.

逆浸透膜装置は、溶媒は通すが溶質は透過させないという逆浸透膜の性質を利用して、被処理水の浸透圧より高い圧力をかけて、溶媒としての水だけを選択的に透過採取する装置である。この逆浸透膜装置を用いて、被処理水中の不純物等を除去するとともに、この逆浸透膜部の下流側に溶存気体を脱気する膜式脱気部を備えた純水製造装置がある(例えば、特許文献1参照)。   The reverse osmosis membrane device selectively permeates and collects only water as a solvent by applying a pressure higher than the osmotic pressure of the water to be treated, utilizing the property of the reverse osmosis membrane that allows the solvent to pass but does not allow the solute to permeate. Device. Using this reverse osmosis membrane device, there is a pure water production apparatus equipped with a membrane-type deaeration unit that removes impurities and the like in treated water and degassed dissolved gas downstream of the reverse osmosis membrane unit ( For example, see Patent Document 1).

特開2004−160379号公報JP 2004-160379 A

しかしながら、特許文献1に記載されているような純水製造装置では、IPAの低濃度に低下させた純水を得ることは困難であるとともに、逆浸透膜部から排出される、IPAが濃縮された濃縮水の量が多く、蒸留する場合コストがかかるという問題があった。   However, in the pure water production apparatus as described in Patent Document 1, it is difficult to obtain pure water reduced to a low concentration of IPA, and IPA discharged from the reverse osmosis membrane portion is concentrated. In addition, there is a problem that the amount of the concentrated water is large and the cost is high when distilling.

そこで、逆浸透膜装置を用いて、洗浄廃水等の被処理水のIPAを低濃度に低下させるとともに、廃水の容積を減らす(減容化)ことを達成することが求められている。以上のことが本発明の課題である。   Therefore, it is required to use a reverse osmosis membrane device to reduce IPA to be treated such as washing wastewater to a low concentration and to reduce the volume of wastewater (volume reduction). The above is the subject of the present invention.

本発明は、このような課題に鑑みてなされたものであり、逆浸透膜装置を用いて、濃縮廃水の容積を減らす(減容化)を達成することを第1の目的とする。
また、逆浸透膜装置を用いて、被処理水のIPA等の不純物を低濃度に低下させることを第2の目的とする。
This invention is made | formed in view of such a subject, and makes it the 1st objective to reduce the volume (volume reduction) of concentrated wastewater using a reverse osmosis membrane apparatus.
A second object is to reduce impurities such as IPA of water to be treated to a low concentration using a reverse osmosis membrane device.

本発明者は、逆浸透膜装置により複数段処理を行うことにより、減容化および被処理水の不純物を低濃度に低下させ得ることを見出し、これに基づいて、以下のような新たな廃水処理装置を発明するに至った。   The present inventor has found that by performing a multi-stage treatment with a reverse osmosis membrane device, volume reduction and impurities in water to be treated can be reduced to a low concentration, and based on this, the following new waste water is obtained. It came to invent a processing apparatus.

(1) 被処理水を貯留する被処理水タンクと、前記被処理水タンクから供給される被処理水を処理し、該被処理水中の不純物が除去された第1段透過水ならびに不純物が濃縮された第1段濃縮水として排出する第1の逆浸透膜装置と、前記第1段濃縮水が供給され、該第1段濃縮水中の不純物が除去された第2段透過水ならびに不純物が濃縮された第2段濃縮水として排出する第2の逆浸透膜装置と、前記第2段透過水を前記被処理水タンクに回収する透過水回収ラインと、を備え、前記第1段透過水を採取するようにしたことを特徴とする廃水処理装置。   (1) A treated water tank for storing treated water and treated water supplied from the treated water tank, and the first-stage permeated water and impurities removed from the treated water are concentrated. The first reverse osmosis membrane device that discharges as the first-stage concentrated water, the second-stage permeated water from which the first-stage concentrated water is supplied, and the impurities in the first-stage concentrated water are removed, and the impurities are concentrated. A second reverse osmosis membrane device that discharges as the second-stage concentrated water, and a permeate recovery line that recovers the second-stage permeate to the treated water tank. A wastewater treatment apparatus characterized by being collected.

(2) 被処理水を貯留する被処理水タンクと、前記被処理水タンクから供給される被処理水を処理し、該被処理水中の不純物が除去された第1段透過水ならびに不純物が濃縮された第1段濃縮水として排出する第1の逆浸透膜装置と、前記第1段濃縮水が供給され、該第1段濃縮水中の不純物が除去された第2段透過水ならびに不純物が濃縮された第2段濃縮水として排出する第2の逆浸透膜装置と、前記第1段透過水が供給され、該第1段透過水中の不純物が除去された第3段透過水ならびに不純物が濃縮された第3段濃縮水として排出する第3の逆浸透膜装置と、前記第2段透過水を前記被処理水タンクに回収する透過水回収ラインと、前記第3段濃縮水を前記被処理水タンクに回収する濃縮水回収ラインと、を備え、前記第3段透過水を採取するようにしたことを特徴とする廃水処理装置。   (2) A treated water tank for storing treated water and treated water supplied from the treated water tank, and the first-stage permeated water and impurities removed from the treated water are concentrated. The first reverse osmosis membrane device that discharges as the first-stage concentrated water, the second-stage permeated water from which the first-stage concentrated water is supplied, and the impurities in the first-stage concentrated water are removed, and the impurities are concentrated. The second reverse osmosis membrane device that discharges as the second-stage concentrated water, and the third-stage permeated water from which the first-stage permeated water is supplied and impurities in the first-stage permeated water are removed and the impurities are concentrated. A third reverse osmosis membrane device that discharges as the third-stage concentrated water, a permeate recovery line that recovers the second-stage permeate to the treated water tank, and the third-stage concentrated water to be treated A concentrated water recovery line for recovery in a water tank, and the third stage permeation Waste water treatment apparatus is characterized in that so as to collect.

(3) 前記第1の逆浸透膜装置と前記第2の逆浸透膜装置との間の濃縮水給水ラインに、濃縮水を貯留する濃縮水タンクを設けたことを特徴とする(1)又は(2)記載の廃水処理装置。   (3) A concentrated water tank for storing concentrated water is provided in the concentrated water supply line between the first reverse osmosis membrane device and the second reverse osmosis membrane device (1) or (2) The waste water treatment apparatus as described.

(4) 前記第1の逆浸透膜装置と前記第3の逆浸透膜装置との間の透過水給水ラインに、透過水を貯留する透過水タンクを設けたことを特徴とする(2)記載の廃水処理装置。   (4) The permeated water tank for storing permeated water is provided in the permeated water supply line between the first reverse osmosis membrane device and the third reverse osmosis membrane device (2). Wastewater treatment equipment.

本発明(1)によれば、逆浸透膜装置を用いて、濃縮廃水の容積を減らす(減容化)を達成することができる。
本発明(2)によれば、逆浸透膜装置を用いて、被処理水のIPA等の不純物を低濃度に低下させるとことができる。
According to the present invention (1), the volume of concentrated waste water can be reduced (volume reduction) using a reverse osmosis membrane device.
According to the present invention (2), the reverse osmosis membrane device can be used to reduce impurities such as IPA to be treated to a low concentration.

以下、本発明の実施形態について説明する。第1実施形態に係わる廃水処理装置は、被処理水を貯留する被処理水タンクから供給される被処理水を処理する第1の逆浸透膜装置を備えている。第1の逆浸透膜装置により被処理水を処理し、被処理水中の不純物が除去された第1段透過水ならびに不純物が濃縮された第1段濃縮水を排出する。排出された第1段濃縮水は第2の逆浸透膜装置に供給され、第2の逆浸透膜装置において処理され、第1段濃縮水中の不純物が除去された第2段透過水ならびに不純物が濃縮された第2段濃縮水として排出する。そして、第2段透過水を透過水回収ラインを介して被処理水タンクに回収し、第1段透過水を採取する。   Hereinafter, embodiments of the present invention will be described. The wastewater treatment apparatus according to the first embodiment includes a first reverse osmosis membrane device that treats water to be treated supplied from a water tank to be treated that stores the water to be treated. The treated water is treated by the first reverse osmosis membrane device, and the first-stage permeated water from which impurities in the treated water are removed and the first-stage concentrated water from which impurities are concentrated are discharged. The discharged first-stage concentrated water is supplied to the second reverse osmosis membrane device, processed in the second reverse osmosis membrane device, and the second-stage permeated water from which impurities in the first-stage concentrated water are removed and impurities are removed. Drain as concentrated second stage concentrated water. Then, the second-stage permeated water is collected in the water tank to be treated through the permeated water collection line, and the first-stage permeated water is collected.

以下、本発明の実施形態について図面を参照して説明する。   Embodiments of the present invention will be described below with reference to the drawings.

図1は、本発明の第1実施形態による廃水処理装置のシステム構成図である。   FIG. 1 is a system configuration diagram of a wastewater treatment apparatus according to a first embodiment of the present invention.

図1に示すように、第1実施形態の廃水処理装置は、被処理水を貯留する被処理水タンク1と、この被処理水タンク1から供給される被処理水を処理する第1の逆浸透膜装置10aと、第1の逆浸透膜装置10aから排出される第1段濃縮水を貯留する濃縮水タンク2と、この濃縮水タンク2から供給される濃縮水を処理する第2の逆浸透膜装置10bと、第2の逆浸透膜装置10bから排出される第2段透過水を被処理水タンク1に回収する透過水回収ライン3と、を備えている。   As shown in FIG. 1, the wastewater treatment apparatus of the first embodiment includes a treated water tank 1 that stores treated water and a first reverse that treats treated water supplied from the treated water tank 1. The osmosis membrane device 10a, the concentrated water tank 2 for storing the first-stage concentrated water discharged from the first reverse osmosis membrane device 10a, and the second reverse for processing the concentrated water supplied from the concentrated water tank 2 The osmosis membrane device 10b and the permeable water recovery line 3 for recovering the second-stage permeable water discharged from the second reverse osmosis membrane device 10b to the water tank 1 to be treated are provided.

逆浸透膜装置10a、10bは、溶媒は通すが溶質は透過させないという性質の逆浸透膜(RO)を利用して、イソプロピルアルコール(以下、IPAと称す)等の不純物を含んだ被処理水の浸透圧より高い圧力をかけて、溶媒としての水だけを選択的に透過採取するものである。図1に示すように、逆浸透膜装置10a、10bは、逆浸透膜又はナノろ過膜(いずれも図示せず)を多数備えた筒状の逆浸透膜モジュール(以下、ROモジュールと称す)11と、このROモジュール11の上流側に設けられた被処理水ライン12と、この被処理水ライン12に設けられた、被処理水を加圧するためのポンプ13と、ROモジュール11の下流側に設けられた、不純物が除かれた処理水を供給するRO処理水ライン(透過水ライン)14と、ROモジュール11の下流側に設けられた、不純物が濃縮された濃縮水を排水する濃縮水ライン15とにより構成されている。   The reverse osmosis membrane devices 10a and 10b use a reverse osmosis membrane (RO) having a property of allowing a solvent to pass but not allowing a solute to pass through, so that water to be treated containing impurities such as isopropyl alcohol (hereinafter referred to as IPA) is used. By applying a pressure higher than the osmotic pressure, only water as a solvent is selectively permeated and collected. As shown in FIG. 1, a reverse osmosis membrane device 10a, 10b is a cylindrical reverse osmosis membrane module (hereinafter referred to as RO module) 11 provided with a number of reverse osmosis membranes or nanofiltration membranes (both not shown). A treated water line 12 provided upstream of the RO module 11, a pump 13 provided in the treated water line 12 for pressurizing treated water, and a downstream side of the RO module 11. An RO treatment water line (permeate water line) 14 that supplies treated water from which impurities are removed, and a concentrated water line that is provided downstream of the RO module 11 and drains concentrated water enriched with impurities. 15.

被処理水タンク1には、例えば、半導体製造工程におけるウェット洗浄等に使用されたIPAを含有する洗浄廃水等の被処理水が貯留される。被処理水タンクの被処理水は、第1の逆浸透膜装置10aのポンプ13により、被処理水ライン12からROモジュール11に供給され、ROモジュール11において処理された透過水は、透過水ライン14から処理水として採取される。   The treated water tank 1 stores treated water such as cleaning wastewater containing IPA used for wet cleaning or the like in the semiconductor manufacturing process. The treated water in the treated water tank is supplied from the treated water line 12 to the RO module 11 by the pump 13 of the first reverse osmosis membrane device 10a, and the permeated water treated in the RO module 11 is the permeated water line. 14 is collected as treated water.

第1の逆浸透膜装置10aのROモジュール11において処理され、不純物が濃縮された濃縮水は、濃縮水ライン15から濃縮水として排出され、濃縮水タンク2に貯留される。濃縮水タンク2に貯留された濃縮水は、第2の逆浸透膜装置10bのポンプ13により、被処理水ライン12から第2の逆浸透膜装置10bのROモジュール11に供給され、ROモジュール11において処理された第2段透過水は、透過水ライン14から透過水回収ライン3を介して被処理水タンク1に回収され、第2の逆浸透膜装置10bのROモジュール11において処理された第2段濃縮水は濃縮水ライン15から排出される。排出された第2段濃縮水は、蒸留等の再処理を行うか又は廃棄される。   The concentrated water that has been processed in the RO module 11 of the first reverse osmosis membrane device 10 a and concentrated in impurities is discharged as concentrated water from the concentrated water line 15 and stored in the concentrated water tank 2. The concentrated water stored in the concentrated water tank 2 is supplied from the treated water line 12 to the RO module 11 of the second reverse osmosis membrane device 10b by the pump 13 of the second reverse osmosis membrane device 10b. The second-stage permeated water treated in step 2 is recovered from the permeated water line 14 to the treated water tank 1 via the permeated water recovery line 3 and processed in the RO module 11 of the second reverse osmosis membrane device 10b. The two-stage concentrated water is discharged from the concentrated water line 15. The discharged second stage concentrated water is subjected to reprocessing such as distillation or discarded.

第1実施形態の廃水処理装置では、第1の逆浸透膜装置10aの第1段濃縮水が第2の逆浸透膜装置10bにおいて処理された後、第2の逆浸透膜装置10bの透過水を被処理水タンク1に回収するので、第1の逆浸透膜装置10aから排出される第1段濃縮水は廃棄することなく第2の逆浸透膜装置10bで再処理され、大部分は透過水回収ライン3を介して被処理水タンク1に回収され、残りは第2段濃縮水として排出される。したがって、第2段濃縮水は第1段濃縮水に比べて容積が大きく減っており、濃縮水の減容化を達成することができる。   In the wastewater treatment apparatus of the first embodiment, the first stage concentrated water of the first reverse osmosis membrane device 10a is treated in the second reverse osmosis membrane device 10b, and then the permeated water of the second reverse osmosis membrane device 10b. Is recovered in the water tank 1 to be treated, so that the first-stage concentrated water discharged from the first reverse osmosis membrane device 10a is reprocessed by the second reverse osmosis membrane device 10b without being discarded, and most of it is permeated. It is recovered in the water tank 1 to be treated via the water recovery line 3 and the rest is discharged as the second stage concentrated water. Therefore, the volume of the second stage concentrated water is greatly reduced as compared with the first stage concentrated water, and the volume reduction of the concentrated water can be achieved.

図2は、本発明の第2実施形態による廃水処理装置のシステム構成図である。   FIG. 2 is a system configuration diagram of the wastewater treatment apparatus according to the second embodiment of the present invention.

図2に示すように、第2実施形態の廃水処理装置は、被処理水を貯留する被処理水タンク1と、この被処理水タンク1から供給される被処理水を処理する第1の逆浸透膜装置10aと、第1の逆浸透膜装置10aから排出される第1段濃縮水を貯留する濃縮水タンク2と、この濃縮水タンク2から供給される濃縮水を処理する第2の逆浸透膜装置10bと、第2の逆浸透膜装置10bから排出される第2段透過水を被処理水タンク1に回収する透過水回収ライン3と、第1の逆浸透膜装置10aの透過水ライン14から排出される第1段透過水を貯留する透過水タンク4と、透過水タンク4から供給される透過水を処理する第3の逆浸透膜装置10cと、第3の逆浸透膜装置10cから排出される第2段濃縮水を被処理水タンク1に回収する濃縮水回収ライン5とにより構成されている。   As shown in FIG. 2, the wastewater treatment apparatus of the second embodiment includes a treated water tank 1 that stores treated water and a first reverse that treats treated water supplied from the treated water tank 1. The osmosis membrane device 10a, the concentrated water tank 2 for storing the first-stage concentrated water discharged from the first reverse osmosis membrane device 10a, and the second reverse for processing the concentrated water supplied from the concentrated water tank 2 The osmosis membrane device 10b, the permeate recovery line 3 for recovering the second stage permeate discharged from the second reverse osmosis membrane device 10b to the treated water tank 1, and the permeate of the first reverse osmosis membrane device 10a A permeated water tank 4 for storing the first-stage permeated water discharged from the line 14, a third reverse osmosis membrane device 10c for treating the permeated water supplied from the permeated water tank 4, and a third reverse osmosis membrane device. The second stage concentrated water discharged from 10c is collected in the treated water tank 1. It is constituted by a Chijimisui recovery line 5.

被処理水タンク1には、例えば、半導体製造工程におけるウェット洗浄等に使用されたIPAを含有する洗浄廃水等の被処理水が貯留される。被処理水タンクの被処理水は、第1の逆浸透膜装置10aのポンプ13により、被処理水ライン12から第1の逆浸透膜装置10aのROモジュール11に供給され、ROモジュール11において処理された透過水は、透過水ライン14から透過水タンク4に排出され、ROモジュール11において処理された濃縮水タンク2に排出される。濃縮水タンク2に貯留された濃縮水は、第2の逆浸透膜装置10bのポンプ13により、被処理水ライン12から第2の逆浸透膜装置10bのROモジュール11に供給され、ROモジュール11において処理された第2段透過水は、透過水ライン14から透過水回収ライン3を介して被処理水タンク1に回収され、第2の逆浸透膜装置10bのROモジュール11において処理された第2段濃縮水は濃縮水ライン15から排出される。排出された第2段濃縮水は、蒸留等の再処理を行うか又は廃棄される。   The treated water tank 1 stores treated water such as cleaning wastewater containing IPA used for wet cleaning or the like in the semiconductor manufacturing process. The treated water in the treated water tank is supplied from the treated water line 12 to the RO module 11 of the first reverse osmosis membrane device 10 a by the pump 13 of the first reverse osmosis membrane device 10 a and processed in the RO module 11. The permeated water is discharged from the permeated water line 14 to the permeated water tank 4 and discharged to the concentrated water tank 2 processed in the RO module 11. The concentrated water stored in the concentrated water tank 2 is supplied from the treated water line 12 to the RO module 11 of the second reverse osmosis membrane device 10b by the pump 13 of the second reverse osmosis membrane device 10b. The second-stage permeated water treated in step 2 is recovered from the permeated water line 14 to the treated water tank 1 via the permeated water recovery line 3 and processed in the RO module 11 of the second reverse osmosis membrane device 10b. The two-stage concentrated water is discharged from the concentrated water line 15. The discharged second stage concentrated water is subjected to reprocessing such as distillation or discarded.

透過水タンク4に貯留された透過水は、第3の逆浸透膜装置10cのポンプ13により第3の逆浸透膜装置10cのROモジュール11に供給される。第3の逆浸透膜装置10cのROモジュール11により処理された透過水は透過水ライン14から採取され、不純物が濃縮された第2段濃縮水は濃縮水回収ライン5を介して被処理水タンク1に回収される。   The permeated water stored in the permeated water tank 4 is supplied to the RO module 11 of the third reverse osmosis membrane device 10c by the pump 13 of the third reverse osmosis membrane device 10c. The permeated water treated by the RO module 11 of the third reverse osmosis membrane device 10 c is collected from the permeated water line 14, and the second stage concentrated water enriched with impurities is treated water tank via the concentrated water recovery line 5. 1 recovered.

第2実施形態の廃水処理装置では、第1実施形態と同様に、第1の逆浸透膜装置10aの第1段濃縮水が第2の逆浸透膜装置10bにおいて処理された後、第2の逆浸透膜装置10bの透過水を被処理水タンク1に回収するので、第1の逆浸透膜装置10aから排出される第1段濃縮水は廃棄することなく第2の逆浸透膜装置10bで再処理され、大部分は透過水回収ライン3を介して被処理水タンク1に回収され、残りは第2段濃縮水として排出される。したがって、第2段濃縮水は第1段濃縮水に比べて容積が大きく減っており、濃縮水の減容化を達成することができる。   In the wastewater treatment apparatus of the second embodiment, after the first-stage concentrated water of the first reverse osmosis membrane device 10a is treated in the second reverse osmosis membrane device 10b, the second Since the permeated water of the reverse osmosis membrane device 10b is collected in the water tank 1 to be treated, the first-stage concentrated water discharged from the first reverse osmosis membrane device 10a is not discarded but is discarded by the second reverse osmosis membrane device 10b. Reprocessing is performed, and most of the water is recovered in the water tank 1 to be treated through the permeate recovery line 3, and the rest is discharged as second-stage concentrated water. Therefore, the volume of the second stage concentrated water is greatly reduced as compared with the first stage concentrated water, and the volume reduction of the concentrated water can be achieved.

さらに第2実施形態では、第1の逆浸透膜装置10aから排出される第1段透過水を第3の逆浸透膜装置10cにおいて再度処理し、第3の逆浸透膜装置10cから排出される第2段透過水を採取するので、第2段透過水は第1段透過水に比べてIPA等の不純物が低濃度化される。このように、第2実施形態では、第1実施形態と同様に減容化が達成できるとともに、採取した透過水はより不純物が低濃度化されているので、洗浄水として再利用することも可能である。   Furthermore, in 2nd Embodiment, the 1st stage permeate discharged | emitted from the 1st reverse osmosis membrane apparatus 10a is processed again in the 3rd reverse osmosis membrane apparatus 10c, and is discharged | emitted from the 3rd reverse osmosis membrane apparatus 10c. Since the second-stage permeate is collected, impurities such as IPA are reduced in the second-stage permeate compared to the first-stage permeate. As described above, in the second embodiment, volume reduction can be achieved in the same manner as in the first embodiment, and the collected permeated water has a lower concentration of impurities, and can be reused as washing water. It is.

なお、第1、第2実施形態における濃縮水タンク2および透過水タンク4は、ROモジュール11に膜つまり等が生じて処理水の排出量が少なくなった場合の緩衝機能を果たすことができる。但し、第1、第2実施形態における濃縮水タンク2および透過水タンク4は、なくても実施は可能である。   Note that the concentrated water tank 2 and the permeated water tank 4 in the first and second embodiments can perform a buffering function when a membrane or the like is generated in the RO module 11 and the discharge amount of the treated water is reduced. However, the concentrated water tank 2 and the permeated water tank 4 in the first and second embodiments can be implemented without them.

以上、説明したように、本発明の実施形態によれば、第1の逆浸透膜装置の第1段濃縮水が第2の逆浸透膜装置において処理された後、第2の逆浸透膜装置の透過水を被処理タンクに回収するので、第1の逆浸透膜装置から排出される第1段濃縮水は廃棄することなく第2の逆浸透膜装置で再処理され、大部分は回収ラインを介して被処理タンクに回収され、残りは第2段濃縮水として排出される。したがって、第2段濃縮水は第1段濃縮水に比べて容積が大きく減っており、濃縮水の減容化を達成することができる。したがって、排出された濃縮水を従来よりも少ない加熱エネルギーで蒸留することが可能になり、IPAの回収コストの節減を図ることができる。   As described above, according to the embodiment of the present invention, after the first-stage concentrated water of the first reverse osmosis membrane device is processed in the second reverse osmosis membrane device, the second reverse osmosis membrane device. Is recovered in the tank to be treated, so that the first-stage concentrated water discharged from the first reverse osmosis membrane device is reprocessed by the second reverse osmosis membrane device without being discarded, and most of the recovered water is recovered in the recovery line. And the rest is discharged as second-stage concentrated water. Therefore, the volume of the second stage concentrated water is greatly reduced as compared with the first stage concentrated water, and the volume reduction of the concentrated water can be achieved. Accordingly, the discharged concentrated water can be distilled with less heating energy than before, and the IPA recovery cost can be reduced.

また、本発明の実施形態によれば、第1の逆浸透膜装置から排出される第1段透過水を第3の逆浸透膜装置において再度処理し、第3の逆浸透膜装置から排出される第2段透過水を採取するので、第2段透過水は第1段透過水に比べてIPA等の不純物が低濃度化される。このように、第2実施形態では、第1実施形態と同様に減容化が達成できるとともに、採取した透過水はより低濃度化されているので、洗浄水として再利用することも可能である。   In addition, according to the embodiment of the present invention, the first-stage permeated water discharged from the first reverse osmosis membrane device is processed again in the third reverse osmosis membrane device and discharged from the third reverse osmosis membrane device. Since the second-stage permeated water is collected, impurities such as IPA are lower in the second-stage permeated water than in the first-stage permeated water. As described above, in the second embodiment, volume reduction can be achieved in the same manner as in the first embodiment, and the collected permeated water is further reduced in concentration, so that it can be reused as washing water. .

また、本発明の実施形態によれば、第1の逆浸透膜装置と第2の逆浸透膜装置との間の濃縮水ラインに、濃縮水を貯留する濃縮水タンクを設けたので、ROモジュールに膜つまり等が生じて濃縮水の排出量が少なくなった場合の緩衝機能を果たすことができる。   Further, according to the embodiment of the present invention, the concentrated water tank for storing the concentrated water is provided in the concentrated water line between the first reverse osmosis membrane device and the second reverse osmosis membrane device. It is possible to perform a buffering function when a membrane clogging or the like occurs on the surface and the discharge amount of concentrated water decreases.

また、本発明の実施形態によれば、第1の逆浸透膜装置と第3の逆浸透膜装置との間の透過水給水ラインに、透過水を貯留する透過水タンクを設けたので、ROモジュールに膜つまり等が生じて透過水の排出量が少なくなった場合の緩衝機能を果たすことができる。   Moreover, according to the embodiment of the present invention, since the permeated water supply line between the first reverse osmosis membrane device and the third reverse osmosis membrane device is provided with the permeated water tank for storing permeated water, RO It is possible to perform a buffer function when a membrane or the like is generated in the module and the discharge amount of permeated water is reduced.

以上、本発明の実施形態を説明したが、具体例を例示したに過ぎず、特に本発明を限定するものではなく、第1の逆浸透膜装置10a、第2の逆浸透膜装置10b、第3の逆浸透膜装置10c、透過水回収ライン3、濃縮水回収ライン5、濃縮水タンク2、透過水タンク4等の具体的構成および配置は適宜設計変更可能である。特に、逆浸透膜装置の配置個数は、任意の複数段で構成することが可能であり、上記実施形態の配置個数は一例に過ぎない。また、上記の実施形態に記載された効果は、本発明から生じる最も好適な効果を列挙したに過ぎず、本発明による効果は、本発明の実施形態に記載されたものに限定されるものではない。   As mentioned above, although embodiment of this invention was described, it only showed the specific example and does not limit this invention in particular, The 1st reverse osmosis membrane apparatus 10a, the 2nd reverse osmosis membrane apparatus 10b, The specific configurations and arrangements of the reverse osmosis membrane device 10c, the permeated water recovery line 3, the concentrated water recovery line 5, the concentrated water tank 2, the permeated water tank 4 and the like can be appropriately changed. In particular, the number of reverse osmosis membrane devices can be configured in an arbitrary plurality of stages, and the number of arrangements in the above embodiment is merely an example. In addition, the effects described in the above-described embodiment only list the most preferable effects resulting from the present invention, and the effects according to the present invention are not limited to those described in the embodiments of the present invention. Absent.

本発明の第1実施形態の廃水処理装置のシステム構成図である。1 is a system configuration diagram of a wastewater treatment apparatus according to a first embodiment of the present invention. 本発明の第2実施形態の廃水処理装置のシステム構成図である。It is a system block diagram of the waste water treatment apparatus of 2nd Embodiment of this invention.

符号の説明Explanation of symbols

1 被処理水タンク
2 濃縮水タンク
4 透過水タンク
5 透過水回収ライン
10a 第1の逆浸透膜装置
10b 第2の逆浸透膜装置
10c 第3の逆浸透膜装置
DESCRIPTION OF SYMBOLS 1 Treated water tank 2 Concentrated water tank 4 Permeated water tank 5 Permeated water collection | recovery line 10a 1st reverse osmosis membrane apparatus 10b 2nd reverse osmosis membrane apparatus 10c 3rd reverse osmosis membrane apparatus

Claims (4)

被処理水を貯留する被処理水タンクと、
前記被処理水タンクから供給される被処理水を処理し、該被処理水中の不純物が除去された第1段透過水ならびに不純物が濃縮された第1段濃縮水として排出する第1の逆浸透膜装置と、
前記第1段濃縮水が供給され、該第1段濃縮水中の不純物が除去された第2段透過水ならびに不純物が濃縮された第2段濃縮水として排出する第2の逆浸透膜装置と、
前記第2段透過水を前記被処理水タンクに回収する透過水回収ラインと、を備え、
前記第1段透過水を採取するようにしたことを特徴とする廃水処理装置。
A treated water tank for storing treated water;
1st reverse osmosis which processes the to-be-processed water supplied from the to-be-processed water tank, and discharge | releases as 1st stage permeated water from which the impurities in this to-be-processed water were removed, and 1st stage concentrated water with which the impurities were concentrated A membrane device;
A second reverse osmosis membrane device that is supplied with the first-stage concentrated water and discharges the second-stage permeated water from which impurities in the first-stage concentrated water are removed and the second-stage concentrated water in which impurities are concentrated;
A permeate recovery line for recovering the second stage permeate to the treated water tank,
A wastewater treatment apparatus characterized in that the first-stage permeate is collected.
被処理水を貯留する被処理水タンクと、
前記被処理水タンクから供給される被処理水を処理し、該被処理水中の不純物が除去された第1段透過水ならびに不純物が濃縮された第1段濃縮水として排出する第1の逆浸透膜装置と、
前記第1段濃縮水が供給され、該第1段濃縮水中の不純物が除去された第2段透過水ならびに不純物が濃縮された第2段濃縮水として排出する第2の逆浸透膜装置と、
前記第1段透過水が供給され、該第1段透過水中の不純物が除去された第3段透過水ならびに不純物が濃縮された第3段濃縮水として排出する第3の逆浸透膜装置と、
前記第2段透過水を前記被処理水タンクに回収する透過水回収ラインと、
前記第3段濃縮水を前記被処理水タンクに回収する濃縮水回収ラインと、を備え、
前記第3段透過水を採取するようにしたことを特徴とする廃水処理装置。
A treated water tank for storing treated water;
1st reverse osmosis which processes the to-be-processed water supplied from the to-be-processed water tank, and discharge | releases as 1st stage permeated water from which the impurities in this to-be-processed water were removed, and 1st stage concentrated water with which the impurities were concentrated A membrane device;
A second reverse osmosis membrane device that is supplied with the first-stage concentrated water and discharges the second-stage permeated water from which impurities in the first-stage concentrated water are removed and the second-stage concentrated water in which impurities are concentrated;
A third reverse osmosis membrane device that is supplied with the first-stage permeated water and discharges the third-stage permeated water from which impurities in the first-stage permeated water are removed and the third-stage concentrated water in which impurities are concentrated;
A permeate recovery line for recovering the second stage permeate to the treated water tank;
A concentrated water recovery line for recovering the third stage concentrated water in the treated water tank,
A wastewater treatment apparatus characterized in that the third-stage permeate is collected.
前記第1の逆浸透膜装置と前記第2の逆浸透膜装置との間の濃縮水給水ラインに、濃縮水を貯留する濃縮水タンクを設けたことを特徴とする請求項1又は2記載の廃水処理装置。   The concentrated water tank which stores concentrated water in the concentrated water supply line between the said 1st reverse osmosis membrane apparatus and the said 2nd reverse osmosis membrane apparatus was provided. Waste water treatment equipment. 前記第1の逆浸透膜装置と前記第3の逆浸透膜装置との間の透過水給水ラインに、透過水を貯留する透過水タンクを設けたことを特徴とする請求項2記載の廃水処理装置。   The wastewater treatment according to claim 2, wherein a permeate tank for storing permeate is provided in a permeate water supply line between the first reverse osmosis membrane device and the third reverse osmosis membrane device. apparatus.
JP2008127229A 2008-05-14 2008-05-14 Wastewater treatment apparatus Pending JP2009274006A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2008127229A JP2009274006A (en) 2008-05-14 2008-05-14 Wastewater treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2008127229A JP2009274006A (en) 2008-05-14 2008-05-14 Wastewater treatment apparatus

Publications (1)

Publication Number Publication Date
JP2009274006A true JP2009274006A (en) 2009-11-26

Family

ID=41439921

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2008127229A Pending JP2009274006A (en) 2008-05-14 2008-05-14 Wastewater treatment apparatus

Country Status (1)

Country Link
JP (1) JP2009274006A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20150040455A (en) * 2013-10-07 2015-04-15 (주)에어레인 Combined membrane separation process for concentration of IPA and treatment of wastewater from IPA-containing wastewater

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20150040455A (en) * 2013-10-07 2015-04-15 (주)에어레인 Combined membrane separation process for concentration of IPA and treatment of wastewater from IPA-containing wastewater
WO2015053483A1 (en) * 2013-10-07 2015-04-16 (주)에어레인 Combined membrane separation process for concentrating ipa from wastewater containing ipa and treating wastewater
KR101695215B1 (en) * 2013-10-07 2017-01-11 (주)에어레인 Combined membrane separation process for concentration of IPA and treatment of wastewater from IPA-containing wastewater

Similar Documents

Publication Publication Date Title
JP6690197B2 (en) Method and system for treating wastewater containing organic matter
JP6440156B2 (en) Organic solvent purification system and method
KR101398352B1 (en) Thermal desalination
JP2018069198A (en) Concentration method and concentrator
JP2018001110A (en) Processing method of brine, processing method of desalinating salt water, processing system of brine, and processing method of desalinating salt water
JP2007130523A (en) Membrane washing method for water treatment system
US8491795B2 (en) Conversion of seawater to drinking water at room temperature
JP2007000788A (en) Water treatment apparatus using reverse osmosis membrane
JP5900527B2 (en) Treatment method for water containing low molecular weight organic substances
JP6670206B2 (en) Ultrapure water production equipment
JP6088268B2 (en) NMP purification system
JP6415159B2 (en) Organic solvent purification system and method
JP6085155B2 (en) Ammonia-containing wastewater treatment apparatus and ammonia-containing wastewater treatment method
JP5245626B2 (en) Method and apparatus for recovering water-soluble organic solvent having amino group
JP2008080255A (en) Pure water making apparatus
JP2009274006A (en) Wastewater treatment apparatus
JP2012210568A (en) Regeneration apparatus and regeneration method of development waste liquid
JP2004130233A (en) Treatment method for high-concentration solution with reverse osmosis membrane
JP2006212540A (en) Treatment method of chemical-washing waste liquid
JPH10305216A (en) Reverse osmosis membrane device and high concentration solution separation
JP2005046762A (en) Water treatment method and water treatment apparatus
JP6368767B2 (en) Ammonia-containing wastewater treatment apparatus and ammonia-containing wastewater treatment method
JP2012149002A (en) Gas purifier
JP2006218341A (en) Method and apparatus for treating water
JP2002001069A (en) Method for producing pure water

Legal Events

Date Code Title Description
RD03 Notification of appointment of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7423

Effective date: 20091106

RD04 Notification of resignation of power of attorney

Effective date: 20091111

Free format text: JAPANESE INTERMEDIATE CODE: A7424