JPS5936506A - Method for controlling operation of electrodialysis type water producing equipment - Google Patents

Method for controlling operation of electrodialysis type water producing equipment

Info

Publication number
JPS5936506A
JPS5936506A JP14477082A JP14477082A JPS5936506A JP S5936506 A JPS5936506 A JP S5936506A JP 14477082 A JP14477082 A JP 14477082A JP 14477082 A JP14477082 A JP 14477082A JP S5936506 A JPS5936506 A JP S5936506A
Authority
JP
Japan
Prior art keywords
current
voltage
controlling
current value
time
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
JP14477082A
Other languages
Japanese (ja)
Inventor
Tetsuyoshi Ishida
哲義 石田
Kenji Shibata
芝田 健二
Kunio Okiura
沖浦 邦夫
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP14477082A priority Critical patent/JPS5936506A/en
Publication of JPS5936506A publication Critical patent/JPS5936506A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To control voltage by operating a titled device at a fixed current value untill the concentration of salt of a desalted water attains a prescribed value, at the time of starting-up an electric power supply, and measuring the electric conductivity of a produced water in the same manner as in an conventional method of operation control, except said start-up. CONSTITUTION:A circuit having a voltage-current controlling switch 6 and a constant current device 10 are installed between a rectifier 2 and an ammeter 4, and the switch 6 is changed to the current controlling side at the time of power supply, and an impressing current value is set to the current in normal operation or the current close to it perform the operation of a fixed current value. The electric conductivity of a produced desalted water falls with the lapse of power supplying time, but when said conductivity attains the electric conductivity in normal operation or the value close to it, the switch 6 is changed to the voltage controlling side to shift the operation to the voltage controlling one. By this operation, an excessive flow of electric current such as in the case of conventional method is prevented because the control at the time of start-up is switched to the constant current control.

Description

【発明の詳細な説明】 本発明は、電気透析式造水装置の運転制御方法に関し、
特に整流器の容量の小さい電気透析式造水装置の運転制
御方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the operation of an electrodialysis water generator,
In particular, the present invention relates to a method of controlling the operation of an electrodialysis water generator with a small rectifier capacity.

電気透析式造水装置は、一端に陽極、他端に陰極を配置
し、これらの電極間に陰イオン交換膜および陽イオン交
換膜を交互に多数挾持した構造を(1) 有している。この両極間に電圧を加えると、陽イオンは
陰極へ、陰イオンは陽極へ電気泳動する結果、両極間に
多数の脱塩室と濃縮室が形成され、との脱塩室から液を
取り出せば脱塩水が得られる。
The electrodialysis fresh water generator has a structure (1) in which an anode is disposed at one end, a cathode is disposed at the other end, and a large number of anion exchange membranes and cation exchange membranes are alternately sandwiched between these electrodes. When a voltage is applied between these two electrodes, cations migrate to the cathode and anions to the anode, resulting in the formation of numerous demineralization chambers and concentration chambers between the two electrodes. Demineralized water is obtained.

従来、−過大の脱塩処理を行なう装置においては、透析
室へ入る電解液が出口で所定の塩濃度となるようにする
必要があり、このため長い液流路を有する構造とする必
要があり、一般に海水から500Fの脱塩水をつくる条
件では10m以上の流路が必要とされている。
Conventionally, in devices that perform excessive desalination processing, it is necessary to ensure that the electrolytic solution entering the dialysis chamber has a predetermined salt concentration at the outlet, and for this reason, it is necessary to have a structure with a long liquid flow path. Generally, a flow path of 10 m or more is required to produce desalinated water at 500 F from seawater.

このような−過大の脱塩処理を行なう電気透析式造水装
置において、脱塩水の純度を保持する方法としては、生
成脱塩水の電導度を測定し、これにより電圧を制御する
方法が行左われている。第1図は、このような従来の一
過式の脱塩処理を行なう電気透析式造水装置の運転制御
方法を示す流れ図である。この電気透析式造水装置では
、電解液7が透析槽1に導入され、電気透析されて脱塩
水8および濃縮水9が取り出される。この脱塩水8の電
導度を電導変針5て測定し、Jこれにより電(2) 圧が制御される。、図中2は整流器−3,ケミ圧計、。
In such an electrodialysis water production system that performs excessive desalination processing, the most common method for maintaining the purity of desalinated water is to measure the electrical conductivity of the produced desalinated water and control the voltage accordingly. It is being said. FIG. 1 is a flowchart showing a method for controlling the operation of an electrodialysis water generating apparatus that performs such a conventional one-time desalination process. In this electrodialysis water generator, an electrolytic solution 7 is introduced into a dialysis tank 1, electrodialyzed, and demineralized water 8 and concentrated water 9 are taken out. The conductivity of this demineralized water 8 is measured by the conductivity change needle 5, and the electric pressure (2) is thereby controlled. , 2 in the figure is a rectifier 3, and a chemical pressure gauge.

番は電流計を示す。The number indicates the ammeter.

しかしながら、この造水装置の通電開始時には透析槽内
の脱塩水の濃度が高いため、定常状態と比較して多量の
電気が流れ、例えば海水から500Pの脱塩水をつくる
条件では、約3倍の電気が流れる。このため、従来の造
水装置では、整流器の容量を定常運転時に必要外容量よ
シ極端に大きくする必要があり、その結果、定常運転時
においては整流器を低負荷で運転することになるため、
電力効率が低いという欠点があった。
However, since the concentration of desalinated water in the dialysis tank is high when the water generator starts energizing, a large amount of electricity flows compared to the steady state. Electricity flows. For this reason, in conventional fresh water generation equipment, the capacity of the rectifier must be made extremely larger than the unnecessary capacity during steady operation, and as a result, the rectifier is operated at a low load during steady operation.
The drawback was low power efficiency.

まだ、従来の造水装置においては、生成脱塩水の電導度
の測定個所が透析槽から遠く離れていると、透析槽内の
脱塩状態の応答が遅くなることから、装置を誤操作する
可能性があった。例えば、透析槽内で十分脱塩処理が進
行しているにもかかわらず、生成脱塩水の電導度指示計
が高い電導度を指示するような場合には、誤って多量の
電流を流し、透析膜の寿命を短縮させるトラブルが生じ
る可能性があった。
However, in conventional water production equipment, if the point where the conductivity of the produced desalinated water is measured is far away from the dialysis tank, the response to the desalination state in the dialysis tank will be slow, leading to the possibility of incorrect operation of the equipment. was there. For example, if the conductivity indicator of the produced desalinated water indicates a high conductivity even though the desalination process is sufficiently progressing in the dialysis tank, a large amount of current may be applied by mistake and the dialysis There was a possibility that problems would occur that would shorten the life of the membrane.

(3) 本発明の目的は、上記の従来技術の欠点を除去し、整流
器の容量を小さクシ、かつ誤動作の少ない電気透析式造
水装置の運転制御方法を提供することにある。
(3) It is an object of the present invention to provide a method for controlling the operation of an electrodialysis water generating apparatus, which eliminates the drawbacks of the above-mentioned conventional techniques, reduces the capacity of the rectifier, and reduces malfunctions.

本発明は、通電開始時に脱塩水の塩濃度が所定の値また
はほぼ所定の値に達するまで一定電流値で運転を行ない
、通電開始時以外は従来の運転制御方法と同様に、生成
水の電導度を測定して電圧を制御するものである。
The present invention operates at a constant current value until the salt concentration of desalinated water reaches a predetermined value or almost a predetermined value at the start of energization. It measures the temperature and controls the voltage.

以下、本発明を図面によりさらに詳細に説明する。第2
図は、本発明の電気透析式造水装置の運転制御方法の一
実施例を示す系統図である。第1図の従来装置と異なる
点は、整流器2と電流計4の間に電圧電流制御切換器6
および定電流装置10を有する回路を設けたことである
。通電開始時には電流〜電流制御切換器6を電流制御側
に切り換え、印加電流値を定常運転時の電流値またはと
の近傍の電流値に設定し、一定電流値運転を行なう。通
電時間の経過にしたがい、生成脱塩水の電導度が低下し
てくるが、この脱塩水の電導度が定(4) 常運転時の電導度またはこの近傍の値に達した時点で、
前記電圧−電流切換器6を電圧制御側に切り換え、従来
方法と同様々電圧制御運転に移行する。このような運転
方法によれば、通電開始時に定電流制御に切換えるので
、従来方法のように極端に多くの電流が流れることなく
、従って整流器の容量は起動時においても定常運転時の
容量と同程度でよく、装置上きわめて有利となる。また
、本発明方法では、整流器が定常運転時において全負荷
に近い状態で使用されるため、電力効率が高くなシ、運
転上から経済的である。さらに本発明の方法では、起動
時に定電流制御を行ない、整流器が小容量化したことに
よシ、透析槽内の脱塩状態の応答が遅いために誤って多
量の電流を流すような誤操作がなくカリ、透析膜の寿命
を短縮させることがなくなる。
Hereinafter, the present invention will be explained in more detail with reference to the drawings. Second
The figure is a system diagram showing one embodiment of the method for controlling the operation of an electrodialysis fresh water generating apparatus according to the present invention. The difference from the conventional device shown in FIG.
and a circuit having the constant current device 10 is provided. At the start of energization, the current-current control switch 6 is switched to the current control side, and the applied current value is set to the current value during steady operation or a current value in the vicinity thereof, thereby performing constant current value operation. As the energization time passes, the conductivity of the produced desalinated water decreases, but the conductivity of this desalinated water remains constant (4).When the conductivity of the desalinated water reaches the value during normal operation or a value close to this,
The voltage-current switch 6 is switched to the voltage control side, and the operation is shifted to voltage control as in the conventional method. According to this operating method, since the switch is made to constant current control at the start of energization, an extremely large amount of current does not flow as in the conventional method, and therefore the capacity of the rectifier remains the same as the capacity during steady operation even at startup. This is extremely advantageous for the device. Further, in the method of the present invention, since the rectifier is used under a state close to full load during steady operation, the power efficiency is high and it is economical from an operational point of view. Furthermore, in the method of the present invention, constant current control is performed at startup, and due to the small capacity of the rectifier, the response of the desalination state in the dialysis tank is slow, which prevents erroneous operations such as accidentally flowing a large amount of current. There is no need for potash to shorten the life of the dialysis membrane.

以上、本発明によれば、整流器の容量を小さくすること
ができ、装置上および運転上からも効率のよい電気透析
式造水装置の運転を行なうことができる。
As described above, according to the present invention, the capacity of the rectifier can be reduced, and the electrodialysis water generation apparatus can be operated efficiently both in terms of equipment and operation.

(5)(5)

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

第1図は従来の電気透析式造水装置の運転制御方法を示
す装置系統図、第2図は、本発明の電気透析式造水装置
の運転制御方法の実施例を示す系統図である。 1・・・・・・透析槽、2・・・・・・整流器、5・・
・・・・電導度肝、6・・・−・・電圧−電流制御切換
器、8・・・・・・脱塩水、10・・・・・・定電流装
置。 代理人 弁理士 川 北 武 長 (6)
FIG. 1 is a system diagram showing a conventional method for controlling the operation of an electrodialysis water generating apparatus, and FIG. 2 is a system diagram showing an embodiment of the method for controlling the operation of an electrodialysis water generating apparatus according to the present invention. 1... Dialysis tank, 2... Rectifier, 5...
. . . Conductivity scale, 6 . . . Voltage-current control switch, 8 . . . Desalinated water, 10 . Agent Patent Attorney Takeshi Kawakita (6)

Claims (1)

【特許請求の範囲】[Claims] (1)陽極と陰極との間に陰イオン交換膜および陽イオ
ン交換膜を交互に配置した電気透析式造水装置の運転制
御方法において、通電開始時に一定電流値運転を行なう
ことを特徴とする電気透析式造水装置の運転制御方法。 (2、特許請求の範囲第1項において、前記一定電流値
が定常運転時の電流値寸たはその近傍の電流値であるこ
とを特徴とする電気透析式造水装置の運転制御方法。
(1) A method for controlling the operation of an electrodialysis water generator in which anion exchange membranes and cation exchange membranes are alternately arranged between an anode and a cathode, characterized by performing constant current value operation at the start of energization. Operation control method for electrodialysis water generation equipment. (2. The method for controlling the operation of an electrodialysis water generating apparatus according to claim 1, wherein the constant current value is a current value during steady operation or a current value in the vicinity thereof.
JP14477082A 1982-08-23 1982-08-23 Method for controlling operation of electrodialysis type water producing equipment Pending JPS5936506A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14477082A JPS5936506A (en) 1982-08-23 1982-08-23 Method for controlling operation of electrodialysis type water producing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14477082A JPS5936506A (en) 1982-08-23 1982-08-23 Method for controlling operation of electrodialysis type water producing equipment

Publications (1)

Publication Number Publication Date
JPS5936506A true JPS5936506A (en) 1984-02-28

Family

ID=15370009

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14477082A Pending JPS5936506A (en) 1982-08-23 1982-08-23 Method for controlling operation of electrodialysis type water producing equipment

Country Status (1)

Country Link
JP (1) JPS5936506A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01102049A (en) * 1987-10-14 1989-04-19 Chlorine Eng Corp Ltd Production of amino acid
KR100489310B1 (en) * 1997-06-30 2005-09-15 주식회사 포스코 Current control method by electric conductivity tracking formula of electrodialysis process for cold rolled water recycle
JP2009220062A (en) * 2008-03-18 2009-10-01 Fuji Electric Holdings Co Ltd Water treatment system

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS516880A (en) * 1974-07-08 1976-01-20 Organo Kk

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS516880A (en) * 1974-07-08 1976-01-20 Organo Kk

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01102049A (en) * 1987-10-14 1989-04-19 Chlorine Eng Corp Ltd Production of amino acid
JPH0830048B2 (en) * 1987-10-14 1996-03-27 クロリンエンジニアズ株式会社 Amino acid production method
KR100489310B1 (en) * 1997-06-30 2005-09-15 주식회사 포스코 Current control method by electric conductivity tracking formula of electrodialysis process for cold rolled water recycle
JP2009220062A (en) * 2008-03-18 2009-10-01 Fuji Electric Holdings Co Ltd Water treatment system

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