JPH0375203B2 - - Google Patents

Info

Publication number
JPH0375203B2
JPH0375203B2 JP58035910A JP3591083A JPH0375203B2 JP H0375203 B2 JPH0375203 B2 JP H0375203B2 JP 58035910 A JP58035910 A JP 58035910A JP 3591083 A JP3591083 A JP 3591083A JP H0375203 B2 JPH0375203 B2 JP H0375203B2
Authority
JP
Japan
Prior art keywords
tank
liquid
dialysis
electrodialysis
desalination
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.)
Expired - Lifetime
Application number
JP58035910A
Other languages
Japanese (ja)
Other versions
JPS59162907A (en
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 filed Critical
Priority to JP58035910A priority Critical patent/JPS59162907A/en
Publication of JPS59162907A publication Critical patent/JPS59162907A/en
Publication of JPH0375203B2 publication Critical patent/JPH0375203B2/ja
Granted legal-status Critical Current

Links

Classifications

    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124—Water desalination

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Description

【発明の詳細な説明】 本発明は、電気透析装置に於て処理液と未処理
液の混合による透析効率低下を防止するための成
層形脱塩水タンクを設けてなる電気透析海水淡水
化装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an electrodialysis seawater desalination apparatus equipped with a stratified desalination water tank for preventing a decrease in dialysis efficiency due to mixing of treated liquid and untreated liquid in the electrodialysis apparatus. .

図1に従来技術からなる電気透析装置の系統を
示す。前記装置は、電気透析槽1、脱塩液循環タ
ンク2、濃縮液循環タンク3、脱塩液循環ポンプ
4、濃縮液循環ポンプ5、配管6、循環弁7、回
収弁8、補給弁9、及び直流電源10等で構成さ
れる。
FIG. 1 shows a system of an electrodialysis apparatus according to the prior art. The device includes an electrodialysis tank 1, a desalinated liquid circulation tank 2, a concentrated liquid circulation tank 3, a desalted liquid circulation pump 4, a concentrated liquid circulation pump 5, piping 6, a circulation valve 7, a recovery valve 8, a replenishment valve 9, and a DC power supply 10, etc.

脱塩液及び濃縮液はそれぞれタンク2,3内へ
所定量の原液が補給されたのち、各ポンプ4,5
で配管6及び循環弁7を経て電気透析槽1内を循
環され脱塩液が所定の濃度になるまで循環処理さ
れる。
After a predetermined amount of the desalted solution and concentrated solution are replenished into tanks 2 and 3, each pump 4 and 5
The desalted solution is circulated through the electrodialysis tank 1 via the piping 6 and the circulation valve 7 until it reaches a predetermined concentration.

所定の濃度に処理された循環液は透析装置を停
止して脱塩液、濃縮液ともに各々回収弁8を経て
回収される。
After the circulating fluid has been treated to a predetermined concentration, the dialyzer is stopped, and both the desalinated fluid and the concentrated fluid are collected through the collection valves 8.

回収が完了すると回収弁8を閉じて各タンク
2,3内へ補給弁9より原水がタンク内へ補給さ
れ再び循環処理され順次これを繰返す。ここで直
流電源は液の回収時及び補給時は停止される。
When the recovery is completed, the recovery valve 8 is closed, and raw water is replenished into each tank 2, 3 from the replenishment valve 9, and the process is repeated again in order. Here, the DC power source is stopped during liquid recovery and replenishment.

このように従来技術の電気透析装置は回分式循
環処理を行つて原水を脱塩しているが脱塩液タン
クは開放形の混合槽であるため当該タンク内では
塩濃度の低い透析槽出口の処理液と当該タンク内
に残留している未処理液とが混合する。従つて混
合液は未処理液より塩濃度が低下するため電気透
析槽内で、通電抵抗が大きく透析に要する電気エ
ネルギーは塩濃度が低下しない場合に比べ大きく
なり処理コストは増大する。
In this way, conventional electrodialysis equipment desalinates raw water by performing batch circulation processing, but since the desalination liquid tank is an open mixing tank, the dialysis tank outlet, which has a low salt concentration, is The treated liquid and the untreated liquid remaining in the tank are mixed. Therefore, since the salt concentration of the mixed solution is lower than that of the untreated solution, there is a large electrical resistance in the electrodialysis tank, and the electrical energy required for dialysis is greater than when the salt concentration is not reduced, resulting in an increase in processing costs.

つまり、電気透析法による脱塩の場合は、電流
値は塩濃度変化幅に比例するため所定濃度へする
ための電流値は一定であり、一方通電抵抗値は塩
濃度が低い程大きくなる。従つて、塩濃度が低い
程消費電力は多くなる。
That is, in the case of desalting by electrodialysis, the current value is proportional to the width of change in salt concentration, so the current value for reaching a predetermined concentration is constant, while the current flow resistance value increases as the salt concentration decreases. Therefore, the lower the salt concentration, the higher the power consumption.

尚、処理液の回収時及び補給時に於ては直流電
源を停止するので脱塩操作は出来ず、処理能力
(稼動率)が低下している。この為、設備(透析
膜面積、直流電源容量等)当りの処理能力は小さ
くなる。
In addition, since the DC power source is stopped when recovering and replenishing the processing liquid, desalination operations are not possible, and the processing capacity (operating rate) is reduced. For this reason, the processing capacity per piece of equipment (dialysis membrane area, DC power supply capacity, etc.) becomes smaller.

本発明の目的は前記した従来技術の欠点をなく
し、脱塩液タンク内で透析槽出口の塩濃度の低く
なつた処理液と当該タンク内に残留する塩濃度の
高い未処理液とが混合して透析槽に供給される脱
塩液の塩濃度が低下しない様にする事により、透
析槽内での電気抵抗を低減させ透析に要する電気
エネルギーを低減し得る電気透析海水淡水化装置
を提供するにある。
The purpose of the present invention is to eliminate the drawbacks of the prior art as described above, and to mix the treated solution with a low salt concentration at the outlet of a dialysis tank with the untreated solution with a high salt concentration remaining in the desalination tank. To provide an electrodialysis seawater desalination device capable of reducing electrical resistance in a dialysis tank and reducing electrical energy required for dialysis by preventing the salt concentration of a desalinated solution supplied to the dialysis tank from decreasing. It is in.

すなわち、本発明は、電気透析装置の脱塩液タ
ンク2の内部に整流板12を設け、液成層形タン
ク11とし、電気透析槽1からの処理液と未処理
液との混合を防止しながら未処理液を順次電気透
析槽へ供給することを特徴とする電気透析装置、
である。
That is, the present invention provides a rectifying plate 12 inside the desalinated liquid tank 2 of an electrodialysis apparatus to form a liquid stratification type tank 11, and prevents the treated liquid from the electrodialysis tank 1 from mixing with the untreated liquid. An electrodialysis device characterized by sequentially supplying untreated liquid to an electrodialysis tank,
It is.

要するに本発明は、脱塩液タンク内で電気透析
槽出口の処理脱塩液と、タンク内の残留する未処
理液が混合しない様にタンク内に整流板12を設
け液成層形タンク11とした電気透析装置であ
る。
In short, the present invention provides a liquid stratification type tank 11 with a rectifier plate 12 installed in the tank so that the treated desalinated liquid at the outlet of the electrodialyzer and the untreated liquid remaining in the tank do not mix in the desalted liquid tank. It is an electrodialysis device.

図2に本発明による電気透析装置の脱塩液タン
クを成層形とする場合の一実施例を示す。図1に
於る透析装置中の脱塩液タンク2の替りに図2の
成層形タンク11を設けることにより配管6によ
り透析層より当該タンクに戻つてくる処理液は当
該タンクに流入し、整流板12に添つてタンク入
口部(本図では上側)より整流されてタンク出口
に流れるので、タンク内に残留する未処理液(本
図では下側の液)と混合することなく脱塩液循環
ポンプ4により透析槽1へ循環供給される。整流
板12の設置方法は本実施例の他に上下方向等
種々考えられるがいずれもタンク内の液を成層流
(ピストン流とも言う)となるようにすることで
同様の透析システムを実現し得る。このシステム
の優位性につき図3にて説明する。
FIG. 2 shows an embodiment in which the desalted solution tank of the electrodialysis apparatus according to the present invention is of a stratified type. By providing the stratified tank 11 shown in FIG. 2 in place of the desalted solution tank 2 in the dialysis machine shown in FIG. Since the flow is rectified from the tank inlet (upper side in this figure) along the plate 12 and flows to the tank outlet, the desalted liquid is circulated without mixing with the untreated liquid remaining in the tank (lower liquid in this figure). It is circulated and supplied to the dialysis tank 1 by the pump 4. In addition to this embodiment, various methods of installing the rectifying plate 12 can be considered, such as vertically, etc., but in any case, a similar dialysis system can be realized by making the liquid in the tank a stratified flow (also called a piston flow). . The advantages of this system will be explained with reference to FIG.

図3は横軸に脱塩水タンク内の処理液の循環回
数、縦軸に液の塩濃度及び、これに相当する液の
電気抵抗を示している。従来方式は連続的に塩濃
度が低下するため、これに相応して電気抵抗値も
連続的に増加する。この状態を図3の直線で示
す。一方、本発明によれば塩濃度は階段状に低下
するため電気抵抗もそれに相応して階段状に増加
し、この状況を図3の階段上直線で示す。こゝで
大切なことは、従来法の電気抵抗値よりも本発明
による電気抵抗値の方が常に低位にあることであ
る。つまり透析電力消費の低下が可能となる。
In FIG. 3, the horizontal axis shows the number of circulations of the treatment liquid in the desalinated water tank, and the vertical axis shows the salt concentration of the liquid and the corresponding electrical resistance of the liquid. In the conventional method, since the salt concentration continuously decreases, the electrical resistance value also increases continuously. This state is shown by the straight line in FIG. On the other hand, according to the present invention, since the salt concentration decreases in a stepwise manner, the electrical resistance also increases in a corresponding stepwise manner, and this situation is shown by the stepwise straight line in FIG. What is important here is that the electrical resistance value of the present invention is always lower than that of the conventional method. In other words, it is possible to reduce dialysis power consumption.

尚図3に示す循環回数は一例であり、これに限
定されるものでない。実際には成層形タンクの形
状および容積等により定まるものである。
Note that the number of circulations shown in FIG. 3 is an example, and is not limited to this. In reality, it is determined by the shape and volume of the stratified tank.

脱塩液タンク内での処理液の混合を防止する方
法として透析槽を直列に複数基設け、第1の透析
槽出口の処理液を第2の透析槽へ直接(脱塩液タ
ンクを設けず)導入して脱塩処理を行う。更に第
3第4と必要な脱塩量に応じて直列に脱塩処理を
行ういわゆる一過処理システムがある。一過処理
システムについては既に従来の混合形の脱塩液タ
ンクを用いる透析システムの欠点を補う方法とし
て提案され公知である。本発明はこの一過処理シ
ステムと同様の効果を単一の透析槽のみで発揮し
得るものである。
As a method to prevent mixing of the treatment liquid in the desalination tank, multiple dialysis tanks are installed in series, and the treatment liquid at the outlet of the first dialysis tank is directly transferred to the second dialysis tank (without the desalination tank). ) and perform desalination treatment. Furthermore, there is a so-called one-time treatment system that performs desalination treatment in series with a third and fourth according to the required amount of desalination. A transient treatment system has already been proposed and known as a method of compensating for the drawbacks of a conventional dialysis system using a mixed type desalted liquid tank. The present invention can achieve the same effects as this transient treatment system using only a single dialysis tank.

本発明の効果として次の3つが挙げられる。 The following three effects can be mentioned as effects of the present invention.

1 従来の透析システムに於る脱塩処理液の脱塩
液タンク内に於る未処理液との混合による濃度
低下を防止し得る。
1. It is possible to prevent concentration reduction due to mixing of the desalted solution with the untreated solution in the desalted solution tank in the conventional dialysis system.

2 従つて透析電気抵抗の増加が低く抑えられる
ため電力消費量が節減される。
2. Therefore, the increase in dialysis electrical resistance is suppressed to a low level, resulting in a reduction in power consumption.

3 一過処理システムと同様の効果を単一の透析
槽をもつて達成されるので設備がコンパクトに
構成出来る。
3. Since the same effects as the one-time treatment system can be achieved using a single dialysis tank, the equipment can be configured compactly.

【図面の簡単な説明】[Brief explanation of drawings]

図1は従来方式による回分式電気透析装置の系
統図を示す。図2は本発明による液成層形タンク
の一実施例を示する断面図を示す。図3には従来
方式と本発明からなる透析装置の透析槽内の液濃
度、電気抵抗と循環回収との関係図表を示す。 1…透析槽、2…脱塩液タンク、3…濃縮液タ
ンク、4…脱塩液循環ポンプ、5…濃縮液循環ポ
ンプ、6…配管、7…循環弁、8…回収弁、9…
補給弁、10…直流源、11…成層形タンク、1
2…整流板。
FIG. 1 shows a system diagram of a conventional batch type electrodialysis apparatus. FIG. 2 shows a cross-sectional view of an embodiment of a liquid stratification type tank according to the present invention. FIG. 3 shows a graph showing the relationship between the concentration of liquid in the dialysis tank, electrical resistance, and circulation recovery in the conventional dialysis apparatus and the dialysis apparatus according to the present invention. 1... Dialysis tank, 2... Desalinated liquid tank, 3... Concentrated liquid tank, 4... Desalted liquid circulation pump, 5... Concentrated liquid circulation pump, 6... Piping, 7... Circulation valve, 8... Recovery valve, 9...
Supply valve, 10... DC source, 11... Stratified tank, 1
2... Rectifier plate.

Claims (1)

【特許請求の範囲】[Claims] 1 電気透析装置の脱塩液タンク2の内部に整流
板12を設け、液成層形タンク11とし、電気透
析槽1からの処理液と未処理液との混合を防止し
ながら未処理液を順次電気透析槽へ供給すること
を特徴とする電気透析装置。
1. A rectifying plate 12 is provided inside the desalination liquid tank 2 of the electrodialysis machine to form a liquid stratification type tank 11, and the untreated liquid is sequentially transferred from the electrodialysis tank 1 while preventing the treated liquid from mixing with the untreated liquid. An electrodialysis device that supplies electricity to an electrodialysis tank.
JP58035910A 1983-03-07 1983-03-07 Electrodyalitic apparatus Granted JPS59162907A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58035910A JPS59162907A (en) 1983-03-07 1983-03-07 Electrodyalitic apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58035910A JPS59162907A (en) 1983-03-07 1983-03-07 Electrodyalitic apparatus

Publications (2)

Publication Number Publication Date
JPS59162907A JPS59162907A (en) 1984-09-13
JPH0375203B2 true JPH0375203B2 (en) 1991-11-29

Family

ID=12455180

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58035910A Granted JPS59162907A (en) 1983-03-07 1983-03-07 Electrodyalitic apparatus

Country Status (1)

Country Link
JP (1) JPS59162907A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6164304U (en) * 1984-10-04 1986-05-01

Also Published As

Publication number Publication date
JPS59162907A (en) 1984-09-13

Similar Documents

Publication Publication Date Title
Lambert et al. Separation of sodium ions from trivalent chromium by electrodialysis using monovalent cation selective membranes
CN107240432B (en) Nuclear power plant radioactive waste liquid treatment process method
MXPA06005386A (en) Water treatment system and method
US6835295B1 (en) Electrowinning cell incorporating metal ion filtration apparatus
CN1388069A (en) Water treatment facilities
US4306946A (en) Process for acid recovery from waste water
CN116693106B (en) A wastewater treatment system based on dialysis-denitrification
TW201904878A (en) Control method and design method of electric deionization device
KR102351744B1 (en) Electrochemical System Using Concentrate Recirculation in Periodic Batch Mode
JP3900666B2 (en) Deionized water production method
US7108772B2 (en) Device and process for electrodialysis of ultrafiltration premeate of electrocoat paint
JPS6336893A (en) Method for operating desalination apparatus by means of electrodialysis
JPS59162907A (en) Electrodyalitic apparatus
CN115818887B (en) Method for adjusting quality of cooling water in camera rotor and intelligent treatment device
CN216149444U (en) Equipment for removing perchlorate in emulsion
CN213112890U (en) Ultrapure water system
CN212222621U (en) Circulating filtering system
WO2022202305A1 (en) Method for controlling electrodeionization device
CN223737774U (en) Liquid desalination system
CN218025720U (en) Automatic adjust electric desalting device
CN206173117U (en) Cyclic utilization raw water purifier
CN219652760U (en) Energy-saving EDI circulation system
CN214270324U (en) Water treatment system
CN201665598U (en) Power station water treatment system with multiple hydration and one water
JPH1110161A (en) Electrodialysis method