JPH0341784Y2 - - Google Patents

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Publication number
JPH0341784Y2
JPH0341784Y2 JP1985199331U JP19933185U JPH0341784Y2 JP H0341784 Y2 JPH0341784 Y2 JP H0341784Y2 JP 1985199331 U JP1985199331 U JP 1985199331U JP 19933185 U JP19933185 U JP 19933185U JP H0341784 Y2 JPH0341784 Y2 JP H0341784Y2
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JP
Japan
Prior art keywords
desalination
chamber
solution
sample
pump
Prior art date
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Expired
Application number
JP1985199331U
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Japanese (ja)
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JPS62106602U (en
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Priority to JP1985199331U priority Critical patent/JPH0341784Y2/ja
Publication of JPS62106602U publication Critical patent/JPS62106602U/ja
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Description

【考案の詳細な説明】 産業上の利用分野 本考案は少量の塩水の脱塩を行なう小型電気透
析装置に関する。さらに詳しくは、液体クロマト
グラフイー分取液の如く、含有する有機物の定
性・定量分析精度向上のために試料中の塩分を除
去する場合等の極めて少容量の塩水の脱塩を目的
とする小型脱塩装置を提供するものである。
[Detailed Description of the Invention] Industrial Application Field The present invention relates to a compact electrodialysis device for desalinating small amounts of salt water. More specifically, it is a small-sized product designed for desalting extremely small volumes of salt water, such as when removing salt from samples such as liquid chromatography preparative solutions to improve the accuracy of qualitative and quantitative analysis of contained organic matter. The present invention provides a desalination device.

従来の技術 一般的に工業的に用いられている電気透析シス
テムは、第1に陽極と陰極の間にイオン交換膜及
び室枠を組みこみ、これを両端から締め付けて成
る電気透析槽、第2の電気透析槽に通液するため
のタンク及びポンプ群、第3の電気透析槽に印加
する直流電流を供給する電源部、第4に各種の制
御を行なう制御部から構成される。
BACKGROUND TECHNOLOGY An electrodialysis system that is generally used industrially consists of an electrodialysis tank that first incorporates an ion exchange membrane and a chamber frame between an anode and a cathode and tightens them from both ends; It is composed of a tank and pump group for supplying liquid to the third electrodialysis tank, a power supply unit that supplies direct current to be applied to the third electrodialysis tank, and a fourth control unit that performs various controls.

これら工業的規模の電気透析システムは、処理
すべき液の容量がある程度大きいため、電気透析
槽は多数の膜と室枠とを交互に積層することで装
置当たりの膜面積を大きくしてある。また、処理
すべき液が特定されているために頻繁に電気透析
槽を解体して膜を交換したり、配管内を洗浄した
りする必要はない。
Since these industrial-scale electrodialysis systems have a relatively large volume of liquid to be treated, the electrodialysis tank has a large number of membranes and chamber frames stacked alternately to increase the membrane area per device. Furthermore, since the liquid to be treated is specified, there is no need to frequently dismantle the electrodialysis tank to replace the membrane or clean the inside of the piping.

しかし、液体クロマトグラフイー分取液等の様
に不特定多数の、しかも少量の試料を脱塩しよう
とする場合、透析槽の構造は、電極枠間に陰イオ
ン交換膜又は中性膜、脱塩室枠、陽イオン交換膜
又は中性膜を配置した3室型構造であることが望
ましく、また膜は試料毎に新しいものに簡単に交
換でき、配管も洗浄して前のサンプルが残らない
様にしなければならない。さらには全体の運転も
簡便であり、望ましくは装置全体が小さいことも
重要である。
However, when attempting to desalt an unspecified large number and small amount of samples such as liquid chromatography preparative solutions, the structure of the dialysis tank requires an anion exchange membrane or a neutral membrane between the electrode frames. A three-chamber structure with a salt chamber frame, a cation exchange membrane, or a neutral membrane is preferable, and the membrane can be easily replaced with a new one for each sample, and the piping can be cleaned so that no previous sample remains. You have to do it the same way. Furthermore, it is important that the overall operation is simple and that the entire device is desirably small.

考案が解決しようとする問題点 3室型脱塩セルとしては、従来より、電極枠間
に一対のイオン交換膜又は中性膜を配置し、膜間
に形成される脱塩室に処理すべき試料を満たして
透析する方法が知られている。この場合、脱塩で
きる試料の容量が脱塩室の容量によつて限定さ
れ、且つ脱塩室を回転子等で撹拌する必要がある
ために脱塩室の大きさを充分に小さくできない等
の欠点があるため好ましくない。
Problems that the invention aims to solve Conventionally, a three-chamber desalination cell has a pair of ion exchange membranes or neutral membranes placed between the electrode frames, and a desalination chamber formed between the membranes. A method of filling and dialyzing a sample is known. In this case, the capacity of the sample that can be desalted is limited by the capacity of the desalting chamber, and the desalting chamber must be stirred with a rotor, etc., so the size of the desalting chamber cannot be made sufficiently small. Undesirable because of its drawbacks.

また装置の自動化に関しては、例えば特公昭51
−35472号公報、特開昭50−110982号公報の提案
があるが、いずれも工業的規模の装置においては
有効であつても、極めて少量の試料の脱塩におい
てはいずれも実施で極めて困難である。
Regarding the automation of equipment, for example,
-35472 and Japanese Patent Application Laid-Open No. 110982/1982, both of them are effective in industrial-scale equipment, but they are extremely difficult to implement when desalting a very small amount of sample. be.

本考案の目的は、上記の問題点を解決し、且つ
膜と室枠の交換が容易で、簡単な操作で少量の試
料が脱塩でき、しかもコンパクトな電気脱塩装置
を提供することにある。
The purpose of the present invention is to solve the above-mentioned problems, and to provide a compact electrodesalination device that allows easy replacement of membranes and chamber frames, allows desalination of small amounts of samples with simple operations, and moreover, is compact. .

問題点を解決するための手段 本考案の電気脱塩装置は、少量の試料を脱塩で
きる様に膜面積を0.5cm2以上100cm2以下とし、且つ
透析槽外部のポンプで試料を循環することでは脱
塩室内を攪拌し、しかも、電気透析槽、液の容器
とポンプ、直流電源、制御装置の全てを1つのケ
ースに固定もしくは収納し、さらには電気的制御
により脱塩セル及び配管内の水洗、試料液及び電
極電解液の循環、直流電流の印加、脱塩の終了の
判断と直流電流の停止、試料液の容器への回収の
一連の操作を自動的に行なうことで、小型で、し
かも簡単な操作で試料の脱塩を可能とする。
Means for Solving the Problems The electrodesalination device of the present invention has a membrane area of 0.5 cm 2 or more and 100 cm 2 or less so that a small amount of sample can be desalinated, and the sample is circulated by a pump outside the dialysis tank. In addition, the electrodialysis tank, liquid container and pump, DC power supply, and control device are all fixed or housed in one case, and the desalination cell and piping are controlled electrically. By automatically performing a series of operations such as washing with water, circulating the sample solution and electrode electrolyte, applying direct current, determining the end of desalination, stopping the direct current, and collecting the sample solution into a container, it is compact and Moreover, the sample can be desalted with simple operations.

実施例 本考案の脱塩装置の一例を第1図に示す。電気
透析槽は陽極枠と陰極枠の間に膜と室枠を組み込
み一体化したユニツトを配置して締めこむことに
より構成される。陽極枠又は陰極枠のいずれか一
方は装置のケースに固定され、ボルト・ナツト等
の締め付け具によつて他方の可動の電極枠と互い
に締め付けられる構造となつている。第1図では
ポンプとして、2流路系で、正・逆転可能なチユ
ーブ式ポンプを用いており第2図で良くわかるよ
うに、一方の流路1で脱塩すべき試料を、他方の
流路3で電極電解液をそれぞれ循環する。試料容
器及び電極電解液容器にはそれぞれ液往路用ノズ
ルと復路ノズルが設けられているが、往路側ノズ
ルは容器のできるだけ下部に、復路側ノズルは液
面より上方に取り付けることにより、効率の良い
液循環ができるとともにポンプを逆回転した時、
殆んど全量の液が容器に回収できる様になる。
Example An example of the desalination apparatus of the present invention is shown in FIG. An electrodialysis cell is constructed by placing and tightening an integrated unit that incorporates a membrane and a chamber frame between an anode frame and a cathode frame. Either the anode frame or the cathode frame is fixed to the case of the device, and is configured to be fastened to the other movable electrode frame using fasteners such as bolts and nuts. In Figure 1, a tube type pump with a two-channel system and capable of forward and reverse rotation is used as the pump. Channel 3 circulates the electrode electrolyte respectively. The sample container and the electrode electrolyte container are each equipped with a liquid forward nozzle and a return path nozzle, but the forward path nozzle is installed as low as possible in the container, and the return path nozzle is installed above the liquid level to improve efficiency. When liquid circulation is established and the pump is rotated in reverse,
Almost all of the liquid can now be collected into a container.

電流値表示部は、定電圧の直流電流を透析槽に
印加して脱塩運転する場合の電流値を表示する部
分であり、脱塩の状況を把握することができ、且
つ電流値設定部で脱塩が終了したことを自動的に
判断して脱塩運転を停止させることができる。こ
れは定電圧法で脱塩した場合、試料の塩濃度の低
下に従い電導度が低下するため、オームの法則に
より印加電流が低下することを利用したものであ
る。また直流電源として、定電流を用いた場合
は、脱塩の進行とともに透析槽の電圧が上昇する
ので同様の方法で制御できる。電流値又は電圧値
は、試料の性状や、目的とする脱塩度に対応させ
るために、任意に設定できることが好ましい。
The current value display section is a section that displays the current value when desalination operation is performed by applying a constant voltage DC current to the dialysis tank, and allows you to grasp the desalination status. It is possible to automatically determine that desalination is complete and stop the desalination operation. This takes advantage of the fact that when desalting is carried out by the constant voltage method, the electrical conductivity decreases as the salt concentration of the sample decreases, so the applied current decreases according to Ohm's law. Furthermore, when a constant current is used as the DC power source, the voltage of the dialysis tank increases as desalination progresses, so it can be controlled in a similar manner. It is preferable that the current value or voltage value can be arbitrarily set in order to correspond to the properties of the sample and the desired degree of desalination.

スイツチは自動運転スタートスイツチひとつが
あれば充分だが、機能拡張のため、水洗のみを行
なうためのスイツチや、脱塩のみを行うためのス
イツチを設けてもよい。
A single automatic operation start switch is sufficient, but to expand functionality, a switch for only flushing or a switch for only desalination may be provided.

装置のフロー模式図を第2図に示す。自動運転
スタートスイツチを押すことで、最初に水洗用ラ
イン5で透析槽の脱塩室及び配管内で洗浄され、
次いで試料循環ライン1に切り換わり通電が開始
される。脱塩が終了すると通電が停止し、ポンプ
2,4が逆回転して試料、電極電解液を容器に回
収した後、ポンプ2,4が停止する。脱塩が終了
した時に試料を容器に回収することは、少量の試
料の脱塩においては極めて重要なことである。即
ち、膜を介して脱塩後の試料と電極室液とが長時
間接していると、せつかく脱塩した試料に電極室
液から塩分が拡散したり、逆に試料中の有価成分
の電極室液側に拡散するからである。
A schematic flow diagram of the device is shown in Figure 2. By pressing the automatic operation start switch, the desalination chamber and piping of the dialysis tank are first washed in the water washing line 5,
Next, the sample circulation line 1 is switched and energization is started. When the desalination is completed, the current supply is stopped, and the pumps 2 and 4 rotate in reverse to collect the sample and the electrode electrolyte into the container, and then the pumps 2 and 4 are stopped. Collecting the sample into a container when desalting is completed is extremely important when desalting a small amount of sample. In other words, if the sample after desalination is in contact with the electrode chamber solution for a long time through the membrane, salt from the electrode chamber solution may diffuse into the sample that has been desalted, or conversely, valuable components in the sample may be transferred to the electrode. This is because it diffuses to the room liquid side.

上記の一連の工程が終了した際にブザー等によ
つて報知することもできる。以上の制御は全てタ
イマー、リレー、電磁弁の活用によつて行なわれ
る。
It is also possible to notify by a buzzer or the like when the above series of steps are completed. All of the above controls are performed using timers, relays, and solenoid valves.

本脱塩装置に使用される膜の通電面積は、0.5
cm2以上100cm2以下であり、好ましくは5cm2以下で
ある。またユニツト内の脱塩室の厚みも小さい方
が好ましく、0.2cm2以上1mm以下のものを用いる。
膜面積、脱塩室の厚みを小さくすることは脱塩室
の容積を小さくすることになり、より少量の試料
を脱塩できるため好ましい。また配管の内径や長
さも同じ理由で極力小さくすることが望ましく、
内径0.5mm〜2mm程度のテフロンチユーブ等を用
いる。これらを充分に配慮することで、1ml程度
の極く少量の試料の脱塩も可能となる。
The current carrying area of the membrane used in this desalination equipment is 0.5
It is not less than cm 2 and not more than 100 cm 2 , preferably not more than 5 cm 2 . It is also preferable that the thickness of the demineralization chamber in the unit be as small as possible, with a thickness of 0.2 cm 2 or more and 1 mm or less being used.
Reducing the membrane area and the thickness of the desalting chamber is preferable because it reduces the volume of the desalting chamber and allows a smaller amount of sample to be desalted. It is also desirable to keep the inner diameter and length of the piping as small as possible for the same reason.
Use a Teflon tube or the like with an inner diameter of about 0.5 mm to 2 mm. By taking these into consideration, it becomes possible to desalt a sample as small as 1 ml.

本考案は特に3室型脱塩装置に関するものであ
るが、試料のPHを維持する必要がある場合には脱
塩室をはさんで緩衝室を設け、5室型の脱塩装置
とすることも可能であり、この場合、緩衝室には
特定の塩の水溶液又は緩衝液を満たすか又は循環
する。
This invention specifically relates to a three-chamber type desalting apparatus, but if it is necessary to maintain the pH of the sample, a buffer chamber can be provided across the desalting chamber to create a five-chamber type desalting apparatus. It is also possible, in which case the buffer chamber is filled with or circulated with an aqueous solution of a specific salt or a buffer.

考案の効果 本考案の電気脱塩装置は、全体が極めて小型
で、1ml程度の少量の試料を簡単な操作でしかも
目的に応じて脱塩することが可能である。
Effects of the invention The electrical desalination apparatus of the invention is extremely compact as a whole, and can desalt a small amount of sample of about 1 ml with simple operation and according to the purpose.

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

第1図は本考案の卓上型電気脱塩装置の1実施
例を示す模式図であり、第2図は概略の液フロー
模式図である。 1…試料循環ライン、2,4…ポンプ、3…電
解液循環ライン、5…水洗用ライン。
FIG. 1 is a schematic diagram showing one embodiment of the tabletop electric desalination apparatus of the present invention, and FIG. 2 is a schematic diagram of a liquid flow. 1... Sample circulation line, 2, 4... Pump, 3... Electrolyte circulation line, 5... Water washing line.

Claims (1)

【実用新案登録請求の範囲】 1 陽極枠と陰極枠の間に陰イオン交換膜又は中
性膜、脱塩室枠、陽イオン交換膜又は中性膜を
順次配置して成る該膜の通電面積が0.5cm2以上
100cm2以下の三室型電気透析槽を有する電気脱
塩装置において、脱塩室に給・排液される試料
液をポンプ2を介して循環させる回路1を設
け、小容量の脱塩室にて該脱塩室内を撹拌しつ
つ脱塩を行なうようにし、かつ該ポンプが正逆
回転可能で、正回転によつて透析を行ない、逆
回転によつて脱塩液が回収できることを特徴と
する電気脱塩装置。 2 電極電解液をポンプ4を介して循環させる回
路3を有する実用新案登録請求の範囲第1項に
記載の電気脱塩装置。 3 ポンプ4は正逆回転可能なもであり、電極室
液を回収できるようにした実用新案登録請求の
範囲第2項に記載の電気脱塩装置。 4 電気透析槽は定電圧の直流電流が印加された
ものであり、かつ、脱塩の終了を電流の降下を
もつて自動的に判断する手段を備え、直流電流
の停止及び脱塩液と電極室液の容器への回収を
自動的に行なうようにした実用新案登録請求の
範囲第3項に記載の電気脱塩装置。 5 電気透析槽は定電流の直流電流が印加された
ものであり、かつ、脱塩の終了を電圧の上昇を
もつて自動的に判断する手段を備え、直流電圧
の停止及び脱塩液と電極室液の容器への回収を
自動的に行なうようにした実用新案登録請求の
範囲第3項に記載の電気脱塩装置。 6 試料液を循環させる回路に洗浄液を通す配管
5が接続されている実用新案登録請求の範囲第
1項から第5項のいずれか1項に記載の電気脱
塩装置。 7 配管及び脱塩室内の洗浄、試料液及び電極室
液の循環、直流電流の印加、脱塩の終了と脱塩
液及び電極室液の回収の一連の工程を自動的に
行なう手段を有する実用新案登録請求の範囲第
6項に記載の電気脱塩装置。 8 試料室及び電極室液の各々のポンプ及び各々
の容器、電気透析槽、直流電源、制御装置等の
全てをひとつのケースに収容若しくは固定して
一体化した実用新案登録請求の範囲第1項から
第7項のいずれか1項に記載の電気脱塩装置。
[Scope of Claim for Utility Model Registration] 1. Current-carrying area of a membrane consisting of an anion exchange membrane or a neutral membrane, a demineralization chamber frame, a cation exchange membrane, or a neutral membrane arranged in sequence between an anode frame and a cathode frame. is 0.5cm2 or more
In an electrodesalination apparatus having a three-chamber electrodialysis tank of 100 cm 2 or less, a circuit 1 is provided to circulate the sample solution supplied to and drained from the demineralization chamber via a pump 2, and a The electric pump is characterized in that desalination is carried out while stirring the interior of the desalination chamber, and that the pump can be rotated in forward and reverse directions, and that dialysis can be performed by forward rotation and the desalted solution can be recovered by reverse rotation. Desalination equipment. 2. The electric desalination apparatus according to claim 1, which has a circuit 3 for circulating an electrode electrolyte via a pump 4. 3. The electric desalination apparatus according to claim 2, wherein the pump 4 can be rotated in forward and reverse directions to recover the electrode chamber liquid. 4 The electrodialysis tank is one to which a constant-voltage direct current is applied, and is equipped with a means to automatically judge the end of desalination based on a drop in the current, stopping the direct current and removing the desalting solution and electrode The electrodesalination apparatus according to claim 3 of the utility model registration, wherein the chamber liquid is automatically collected into a container. 5 The electrodialysis tank is one to which a constant direct current is applied, and is equipped with a means for automatically determining the end of desalination by a rise in voltage, and is equipped with a means to automatically judge the end of desalination by a rise in voltage, and to stop the direct voltage and remove the desalination solution and electrodes. The electrodesalination apparatus according to claim 3 of the utility model registration, wherein the chamber liquid is automatically collected into a container. 6. The electrodesalination apparatus according to any one of claims 1 to 5, wherein a pipe 5 for passing a cleaning liquid is connected to a circuit for circulating a sample liquid. 7 Practical equipment that has a means to automatically perform a series of steps such as cleaning the piping and demineralization chamber, circulating the sample solution and electrode chamber solution, applying direct current, completing desalination, and recovering the desalination solution and electrode chamber solution. The electrical desalination apparatus according to claim 6 of the patent registration claim. 8. Scope of Utility Model Registration Claim Paragraph 1, in which the sample chamber and electrode chamber liquid pumps and containers, electrodialysis tank, DC power supply, control device, etc. are all housed or fixed in one case and integrated. The electrodesalination apparatus according to any one of Items 7 to 8.
JP1985199331U 1985-12-26 1985-12-26 Expired JPH0341784Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1985199331U JPH0341784Y2 (en) 1985-12-26 1985-12-26

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1985199331U JPH0341784Y2 (en) 1985-12-26 1985-12-26

Publications (2)

Publication Number Publication Date
JPS62106602U JPS62106602U (en) 1987-07-08
JPH0341784Y2 true JPH0341784Y2 (en) 1991-09-02

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WO2013015229A1 (en) * 2011-07-22 2013-01-31 Semiconductor Energy Laboratory Co., Ltd. Graphite oxide, graphene oxide or graphene, electric device using the same and method of manufacturing the same, and electrodialysis apparatus

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