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JP2011168857A - Electrolytic cell structure of diaphragm electrolytic cell - Google Patents

Electrolytic cell structure of diaphragm electrolytic cell Download PDF

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JP2011168857A
JP2011168857A JP2010035069A JP2010035069A JP2011168857A JP 2011168857 A JP2011168857 A JP 2011168857A JP 2010035069 A JP2010035069 A JP 2010035069A JP 2010035069 A JP2010035069 A JP 2010035069A JP 2011168857 A JP2011168857 A JP 2011168857A
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electrode plate
electrolytic cell
diaphragm
electrolysis
electrolyzed water
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JP5380327B2 (en
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Koji Hatada
康治 畑田
Kyoichiro Yoshida
恭一郎 吉田
Masahiro Fujita
昌浩 藤田
Isao Ito
勲 伊藤
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Hoshizaki Electric Co Ltd
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Hoshizaki Electric Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an electrolytic cell with which early corrosion of an electrode plate is drastically suppressed or prevented by rapidly introducing gaseous chlorine or the like, tending to build up on the upper side of each electrolytic chamber of a diaphragm electrolytic cell, to an outlet of water produced by electrolysis, discharging it to the outside of the system, making the water produced by electrolysis smoothly flow out from the outlet, and suppressing or certainly controlling exposure of an upper end portion of the electrode plate to the gaseous chlorine. <P>SOLUTION: The electrolytic cell is constructed by forming a plurality of gaps E arranged in parallel to one another in the direction of the width of the electrolytic chamber between members facing stepped parts 13a, 13b and members opposite thereto, wherein the stepped parts 13a, 13b having recessed shapes and opening on the side opposite to a membrane 10c are arranged on the upper end portion of each vertical frame portion 13 of spacers 10a, 10b constructing an electrode plate unit 10, so as to capture a gas produced on surfaces of the electrode plates 10d, 10e in the respective gaps E, and to make the captured gas flow out together with the water produced by electrolysis. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、電解水生成装置を構成する有隔膜電解槽に関し、特に、当該有隔膜電解槽の電解槽構造に関する。   The present invention relates to a diaphragm electrolytic cell constituting an electrolyzed water generating device, and more particularly to an electrolytic cell structure of the diaphragm electrolytic cell.

電解水生成装置を構成する有隔膜電解槽の一形成として、下方の部位に被電解水の導入口部を有するとともに上方の部位に電解生成水の導出口部を有する所定長さの筺体内に、一対の方形枠状のスペーサにて挟持された状態の隔膜の各側面側に前記各スペーサにて規定される間隔を保持して陽極側の電極板と陰極側の電極板を配置してなる電極板ユニットを1または複数収容してなる形式の有隔膜電解槽がある(特許文献1,2を参照)。   As one formation of the diaphragm membrane electrolytic cell constituting the electrolyzed water generating apparatus, the electrolyzed water is introduced in the lower part and the electrolyzed water outlet part is provided in the upper part. The electrode plate on the anode side and the electrode plate on the cathode side are arranged on the side surfaces of the diaphragm sandwiched between a pair of square frame spacers while maintaining the interval defined by each spacer. There is a diaphragm membrane electrolytic cell in which one or a plurality of electrode plate units are accommodated (see Patent Documents 1 and 2).

当該形式の有隔膜電解槽においては、電極板ユニットが形成する各電解室に流入した被電解水は各電極板に沿って上方へ流動し、この間、被電解水は有隔膜電解されて電解生成水となり、各生成された各電解生成水は、各電解室から各導出口部に導入されて、各導出口部から流出するようになっている。   In the diaphragm membrane electrolytic cell of this type, the electrolyzed water flowing into each electrolysis chamber formed by the electrode plate unit flows upward along each electrode plate, and during this time, the electrolyzed water is electrolyzed by diaphragm electrolysis. Each electrolyzed water produced is introduced into each outlet port from each electrolysis chamber and flows out from each outlet port.

特開平8−158084号公報JP-A-8-158084 特開2004−18836号公報JP 2004-18836 A

このように、当該形式の有隔膜電解槽においては、各電解室にて生成される各電解生成水を、各電解室から各導出口部に導入して、各導出口部から流出するように構成されているが、各電解室の上方に部位には、有隔膜電解時に発生する塩素ガス等のガスが漸次滞溜し、滞留するガスが各電解生成水の各導出口部への導入を妨げ、各導出口部から必ずしも円滑には流出しなくなるおそれがある。
また、一般に、電極板ユニットを構成する電極板は、その電解効率を考慮して、スペーサと略同等の寸法に形成されている。このため、電極板はその上端部を、各電解室の上方に滞留する塩素ガス等に曝される状態にあって、電極板は早期に腐食されるおそれがある。
As described above, in the diaphragm electrolytic cell of this type, each electrolytically generated water generated in each electrolytic chamber is introduced into each outlet port from each electrolytic chamber and flows out from each outlet port. However, gas such as chlorine gas generated at the time of diaphragm electrolysis gradually accumulates above each electrolysis chamber, and the retained gas is introduced into each outlet port of each electrolyzed water. There is a risk that it will not flow out smoothly from each outlet.
In general, the electrode plate constituting the electrode plate unit is formed to have substantially the same dimensions as the spacer in consideration of the electrolytic efficiency. For this reason, the upper end of the electrode plate is exposed to chlorine gas or the like staying above each electrolysis chamber, and the electrode plate may be corroded early.

従って、本発明の目的は、当該形式の有隔膜電解槽において、各電解室の上方に滞留しがちな塩素ガス等を、導出口部に速やかに導入して系外へ排出して、生成される電解生成水を導出口からスムーズに流出させるようにするとともに、各電極板の上端部が塩素ガスに曝されるのを極力抑制しまたは確実に規制して、電極板の早期の腐食を大幅に抑制しまたは防止することにある。   Accordingly, an object of the present invention is to generate chlorine gas, etc., which tends to stay above each electrolytic chamber, in a diaphragm membrane electrolytic cell of this type, by quickly introducing it into the outlet and discharging it out of the system. Electrolytically generated water is allowed to flow smoothly from the outlet, and the upper end of each electrode plate is prevented from being exposed to chlorine gas as much as possible. It is to suppress or prevent.

本発明は、有隔膜電解槽の電解槽構造に関する。本発明が適用対象とする有隔膜電解槽は、下方の部位に被電解水の導入口部を有するとともに上方の部位に電解生成水の導出口部を有する所定長さの筺体内に、一対の方形枠状のスペーサにて挟持された状態の隔膜の各側面側に前記各スペーサにて規定される間隔を保持して陽極側の電極板と陰極側の電極板を配置してなる電極板ユニットを1または複数収容してなり、前記電極板ユニットが形成する各電解室に流入して前記各電極板に沿って上方へ流動する被電解水を有隔膜電解するとともに、生成される電解生成水を前記各電解室から前記導出口部を通して流出するように構成してなる形式の有隔膜電解槽である。   The present invention relates to an electrolytic cell structure of a diaphragm membrane electrolytic cell. The diaphragm electrolyzer to which the present invention is applied has a pair of a predetermined length of a casing having an inlet for electrolyzed water at a lower part and an outlet for electrolytically generated water at an upper part. An electrode plate unit in which an electrode plate on the anode side and an electrode plate on the cathode side are arranged on the side surfaces of the diaphragm sandwiched by square frame spacers while maintaining the distances defined by the spacers. Electrolyzed water produced by separating the electrolyzed water flowing into the electrolysis chambers formed by the electrode plate unit and flowing upward along the electrode plates, together with the electrolysis of the diaphragm Is a diaphragm electrolytic cell of a type configured to flow out from each electrolytic chamber through the outlet port.

しかして、本発明に係る有隔膜電解槽においては、前記スペーサは、方形の外枠部の下枠部位から上枠部位に至る互いに所定間隔を保持して並列して延びる複数の縦枠部を備える格子状枠体であって、同格子状枠体の各縦枠部の上端部位には前記隔膜とは反対側に開口する凹状の段差部を備え、同段差部は対向する部材との間に隙間を形成し、同隙間は前記各電解室の幅方向に複数並列していて、有隔膜電解時に前記電極板の表面にて発生するガスを捕捉し、捕捉したガスを電解生成水とともに前記導出口部へ導入すべく機能することを特徴とするものである。   Therefore, in the diaphragm membrane electrolytic cell according to the present invention, the spacer includes a plurality of vertical frame portions extending in parallel while maintaining a predetermined distance from the lower frame portion to the upper frame portion of the rectangular outer frame portion. A grid-like frame body, the upper end portion of each vertical frame portion of the grid-like frame body is provided with a concave step portion that opens to the opposite side of the diaphragm, the step portion between the opposing members A plurality of the gaps are arranged in parallel in the width direction of each of the electrolysis chambers, capture gas generated on the surface of the electrode plate during diaphragm membrane electrolysis, and capture the trapped gas together with electrolyzed water. It functions to be introduced into the outlet port.

本発明に係る有隔膜電解槽においては、前記電極板ユニットを構成する電極板は前記スペーサより短い寸法に形成して、同電極板の上端部を、前記スペーサの縦枠部位の段差部が形成する隙間から回避するように構成することができる。   In the diaphragm electrolyzer according to the present invention, the electrode plate constituting the electrode plate unit is formed to be shorter than the spacer, and the upper end portion of the electrode plate is formed as a step portion of the vertical frame portion of the spacer. It can be configured so as to avoid from the gap.

また、本発明に係る有隔膜電解槽においては、前記電極板ユニットの複数を、互いに重合した状態で筺体内に収容して、前記各電極板ユニットを構成する各スペーサの縦枠部の段差部を互いに対向させて前記隙間を形成するように構成することができる。   Further, in the diaphragm membrane electrolytic cell according to the present invention, a plurality of the electrode plate units are accommodated in a casing in a state of being overlapped with each other, and a step portion of a vertical frame portion of each spacer constituting each electrode plate unit Can be configured to face each other to form the gap.

本発明に係る有隔膜電解槽においては、電解槽内の上方の部位に、スペーサを構成する格子状枠体の各縦枠部に設けた段差部にて形成される隙間が複数並列していて、これらの隙間は、有隔膜電解時に電極板の表面にて発生するガスを積極的に捕捉し、捕捉したガスを電解生成水とともに前記導出口部へ導入すべく機能する。
このため、本発明に係る有隔膜電解槽においては、各電解室内に発生したガスが各電解室内の上方の部位に大量に滞留することはなく、電解生成水を導出口部に円滑に導入して、導出口部から円滑に流出させることができる。また、各電解室から電解生成水が流出する際には、各隙間に受け入れられたガスを伴って流出することから、各電極板の上端部の塩素ガス等による影響を大幅に抑制し得て、電極板の早期の腐食を防止することができる。
本発明に係る有隔膜電解槽において、各電極板を、各スペーサより短い寸法に形成して、各電極板の上端部を各隙間から回避するように構成すれば、換言すれば、各電極板の上端部を各隙間に臨むことが無いように構成すれば、各電極板の上端部の塩素ガス等による影響をほぼ確実に規制し得て、電極板の一層の早期の腐食を防止することができる。
また、本発明に係る有隔膜電解槽において、電極板ユニットの複数を互いに重合された状態で筺体内に収容して、各電極板ユニットを構成する各スペーサの縦枠部の段差部を互いに対向して配置すれば、互いに対向する段差によって大きな隙間を形成することができ、形成される各隙間は発生するガスを一層確実に受け入れることができて、発生する塩素ガス等の排出を一層有利にすることができる。
In the diaphragm membrane electrolytic cell according to the present invention, a plurality of gaps formed in step portions provided in each vertical frame portion of the grid frame constituting the spacer are arranged in parallel in an upper portion in the electrolytic cell. These gaps function to positively capture the gas generated on the surface of the electrode plate during diaphragm electrolysis and introduce the trapped gas into the outlet port together with the electrolytically generated water.
Therefore, in the diaphragm electrolyzer according to the present invention, a large amount of gas generated in each electrolytic chamber does not stay in the upper part of each electrolytic chamber, and the electrolytically generated water is smoothly introduced into the outlet port. Thus, it can be smoothly discharged from the outlet. In addition, when electrolytically generated water flows out from each electrolysis chamber, it flows out with the gas received in each gap, so that the influence of chlorine gas etc. at the upper end of each electrode plate can be greatly suppressed. The early corrosion of the electrode plate can be prevented.
In the diaphragm electrolyzer according to the present invention, each electrode plate is formed to be shorter than each spacer, and the upper end portion of each electrode plate is avoided from each gap. In other words, each electrode plate If it is configured so that the upper end of the electrode does not face each gap, the influence of chlorine gas etc. on the upper end of each electrode plate can be regulated almost certainly, and further early corrosion of the electrode plate can be prevented. Can do.
Further, in the diaphragm electrolytic cell according to the present invention, a plurality of electrode plate units are accommodated in a casing in a state of being polymerized with each other, and the step portions of the vertical frame portions of the spacers constituting each electrode plate unit are opposed to each other. If arranged in this manner, a large gap can be formed by the steps facing each other, and each gap that is formed can more reliably receive the generated gas, thereby further advantageously discharging the generated chlorine gas and the like. can do.

本発明に係る有隔膜電解槽を装備した電解水生成装置の装置本体を後側からみた背面図である。It is the rear view which looked at the apparatus main body of the electrolyzed water generating apparatus equipped with the diaphragm membrane electrolyzer concerning the present invention from the back side. 同有隔膜電解槽の正面図(a)、および、同図の矢印2−2線で縦断した縦断側面図(b)である。It is the front view (a) of the said diaphragm membrane electrolytic cell, and the vertical side view (b) longitudinally cut | disconnected by the arrow 2-2 line of the same figure. 同有隔膜電解槽を構成する電極板ユニットを分解した状態の斜視図である。It is a perspective view of the state which decomposed | disassembled the electrode plate unit which comprises the said diaphragm membrane electrolytic cell. 同電極板ユニットを構成するスペーサの正面図(a)、同図の矢印4−4線で縦断した縦断側面図(b)、同図の矢印Dで示す上方の部位の拡大図(c)、同スペーサの側面図(d)である。Front view of spacer constituting the electrode plate unit (a), vertical side view (b) vertically cut by the line 4-4 in the same figure, enlarged view (c) of the upper part indicated by the arrow D in the same figure, It is a side view (d) of the spacer.

本発明は、有隔膜電解槽の電解槽構造に関する。図1には、本発明に係る電解槽構造を採用した有隔膜電解槽を装備する電解水生成装置を示している。当該電解水生成装置は、装置本体AをケースB内に収容してなるもので、図1は、ケースBから取出した状態の装置本体Aの背面側を示している。   The present invention relates to an electrolytic cell structure of a diaphragm membrane electrolytic cell. In FIG. 1, the electrolyzed water generating apparatus equipped with the diaphragm membrane electrolyzer which employ | adopted the electrolyzer structure which concerns on this invention is shown. The electrolyzed water generating apparatus is configured by housing the apparatus main body A in a case B. FIG. 1 shows the back side of the apparatus main body A in a state of being taken out from the case B.

当該電解水生成装置は、本発明に係る電解槽構造に構成された有隔膜電解槽Cを主体とするものである。有隔膜電解槽Cは、図2に示すように、複数の電極板ユニット10を重合した状態で筺体20内に収容して構成されていて、各電極板ユニット10の内部には、一対の電解室(陽極側電解室および陰極側電解室)が形成されている。   The electrolyzed water generating apparatus is mainly composed of a diaphragm electrolyzer C configured in an electrolyzer structure according to the present invention. As shown in FIG. 2, the diaphragm electrolytic cell C is configured by accommodating a plurality of electrode plate units 10 in a housing 20 in a polymerized state, and inside each electrode plate unit 10 is a pair of electrolytic cells. Chambers (anode-side electrolysis chamber and cathode-side electrolysis chamber) are formed.

当該電解水生成装置Cにおいては、有隔膜電解槽10を収容する筺体20の下方の部位に設けられた被電解水の導入口部には、被電解水の供給管路31(31a,31b)が接続されており、また、筺体20の上方の部位に設けられた電解生成水の導出口部には、各電解生成水を流出させる各流出管路32a,32bが接続されている。   In the electrolyzed water generating apparatus C, an electrolyzed water supply pipe 31 (31a, 31b) is provided at an electrolyzed water introduction port provided at a site below the housing 20 that houses the diaphragm electrolyzer 10. In addition, the outflow pipes 32a and 32b through which the electrolytically generated water flows out are connected to the outlet of the electrolytically generated water provided in the region above the housing 20.

被電解水は、高濃度の塩水を原水にて所定濃度に希釈してなる希薄塩水であって、原水が流入する供給管路33の途中に、図示しない塩水タンクから塩水供給管路34を通して一定量の高濃度塩水を継続して供給することによって、供給管路33内にて調製される。調製された被電解水は、供給管路31の分岐管路部31a,31bを通して、各電極板ユニット10内に形成されている陽極側電解室および陰極側電解室にそれぞれ供給される。   The electrolyzed water is dilute salt water obtained by diluting high-concentration salt water to a predetermined concentration with raw water, and is constant through a salt water supply line 34 from a salt water tank (not shown) in the middle of the supply line 33 into which the raw water flows. It is prepared in the supply line 33 by continuously supplying a quantity of high-concentration salt water. The prepared electrolyzed water is supplied to the anode-side electrolysis chamber and the cathode-side electrolysis chamber formed in each electrode plate unit 10 through the branch conduit portions 31a, 31b of the supply conduit 31, respectively.

有隔膜電解槽Cにおいては、陽極側電解室および陰極側電解室に供給された各被電解水は、電極板ユニット10が有する陽極側電極板、陰極側電極板に沿って上方へ流動し、この間に有隔膜電解されて、陽極側電解室では電解生成酸性水が生成され、かつ、陰極側電解室では電解生成アルカリ性水が生成される。陽極側電解室にて生成された電解生成酸性水、および、陰極側電解室にて生成された電解生成アルカリ性水は、各導出口部から各流出管路32a,32bに流出して、予め指定されている場所に供給される。   In the diaphragm electrolyzer C, each electrolyzed water supplied to the anode side electrolysis chamber and the cathode side electrolysis chamber flows upward along the anode side electrode plate and the cathode side electrode plate of the electrode plate unit 10, During this time, the diaphragm is electrolyzed, so that electrolytically generated acidic water is generated in the anode side electrolytic chamber, and electrolytically generated alkaline water is generated in the cathode side electrolytic chamber. The electrolytically generated acidic water generated in the anode side electrolytic chamber and the electrolytically generated alkaline water generated in the cathode side electrolytic chamber flow out from the outlets to the outflow pipes 32a and 32b and are designated in advance. Supplied to the place where it is.

しかして、本発明に係る有隔膜電解槽Cを構成する電極板ユニット10は、図3に示すように、一対の方形枠状のスペーサ10a,10bにて挟持された状態の隔膜10cの各側面側に、各スペーサ10a,10bにて規定される間隔を保持して陽極側の電極板10dと陰極側の電極板10eをそれぞれ配置して構成されている。但し、図3に例示している電極ユニット10は、互いに重合されて筺体20に収容されて使用される態様を採ることから、互いに隣り合う同士の電極板ユニット10間では、同一の電極板10d,10eを互いに共用する構成になっている。   Therefore, as shown in FIG. 3, the electrode plate unit 10 constituting the diaphragm electrolytic cell C according to the present invention has each side surface of the diaphragm 10c sandwiched between a pair of square frame spacers 10a and 10b. The anode-side electrode plate 10d and the cathode-side electrode plate 10e are respectively arranged on the side while maintaining the intervals defined by the spacers 10a and 10b. However, since the electrode units 10 illustrated in FIG. 3 are used by being superposed on each other and accommodated in the housing 20, the same electrode plate 10 d is used between the electrode plate units 10 adjacent to each other. , 10e are shared with each other.

電極板ユニット10を構成するスペーサ10a,10bは、図4に示すように、隔膜10cを左右から挟持した状態で一体化されていて、電極ユニット10内の隔膜10cと電極板10d、および、隔膜10cと電極板10e間に、陽極側電解室および陰極側電解室を形成している。このため、当該有隔膜電解槽10においては、複数の電極板ユニット10が互いに重合して収容されていることから、上記した一対の電解室を複数対備えていて、電解運転時には、被電解水は複数対の各電解室に同時に供給されて、有隔膜電解を受けるになっている。   As shown in FIG. 4, the spacers 10a and 10b constituting the electrode plate unit 10 are integrated with the diaphragm 10c sandwiched from the left and right, and the diaphragm 10c in the electrode unit 10, the electrode plate 10d, and the diaphragm An anode side electrolysis chamber and a cathode side electrolysis chamber are formed between 10c and the electrode plate 10e. For this reason, in the said diaphragm membrane electrolytic cell 10, since the several electrode plate unit 10 superposed | polymerized and accommodated mutually, it is provided with several pairs of the above-mentioned pair of electrolysis chambers, Are supplied simultaneously to a plurality of pairs of electrolysis chambers to undergo diaphragm electrolysis.

当該電極板ユニット10を構成するスペーサ10a,10bは、図4に示すように、同一構成の格子状枠体であって、隔膜10cを挟持した状態では、互いに左右対称を呈している。格子状枠体である各スペーサ10a,10bは、長方形状の外枠部11,12と、外枠部11,12内にて上下方向に延びる複数本の縦枠部13にて構成されている。
各縦枠部13は、外枠部11,12を構成する下枠部位11a,12aと上枠部位11b,12b間に、所定間隔を保持して上下方向に並列して延びていて、各縦枠部13,13の上端部(図4(b)の矢印Dが示す円で包囲する上端部)には、段差部13a,13bが形成されている。各段差部13a,13bは、図4(c)にて拡大して示すように、挟持している隔膜10cに対して反対側で、重合される電極板10d,10e側に開口している。
As shown in FIG. 4, the spacers 10 a and 10 b constituting the electrode plate unit 10 are lattice frame bodies having the same configuration and are symmetrical with each other in a state where the diaphragm 10 c is sandwiched. Each of the spacers 10a and 10b, which is a lattice-shaped frame body, includes a rectangular outer frame portion 11 and 12 and a plurality of vertical frame portions 13 extending in the vertical direction within the outer frame portions 11 and 12. .
Each vertical frame portion 13 extends in parallel in the vertical direction while maintaining a predetermined interval between the lower frame portions 11a and 12a and the upper frame portions 11b and 12b constituting the outer frame portions 11 and 12. Step portions 13a and 13b are formed at the upper end portions of the frame portions 13 and 13 (the upper end portion surrounded by the circle indicated by the arrow D in FIG. 4B). As shown in an enlarged view in FIG. 4C, each of the stepped portions 13a and 13b is open to the electrode plates 10d and 10e to be polymerized on the opposite side to the sandwiched diaphragm 10c.

また、各スペーサ10a,10bを構成する外枠部11,12には、図4の図示左側の左枠部位11c,12c、および、図示右側の右枠部位11d,12dに、嵌合凸部11e,12eと、嵌合凹部11f,12fが形成されている。当該電極板ユニット10の隣り合う同士のスペーサ10a,10bにおいては、左枠部位11c,12cの嵌合凸部11eおよび嵌合凹部11fが、右枠部位11d,12dの嵌合凹部11f,12fおよび嵌合凸部11e,12eに対向していて、両スペーサ10a,10bは互いに嵌合した状態で重合されている。   Further, the outer frame portions 11 and 12 constituting the spacers 10a and 10b are respectively provided with the left frame portions 11c and 12c on the left side in FIG. 4 and the right frame portions 11d and 12d on the right side in FIG. , 12e and fitting recesses 11f, 12f are formed. In the adjacent spacers 10a and 10b of the electrode plate unit 10, the fitting convex portions 11e and the fitting concave portions 11f of the left frame portions 11c and 12c are fitted into the fitting concave portions 11f and 12f of the right frame portions 11d and 12d, and Opposing to the fitting convex portions 11e and 12e, both the spacers 10a and 10b are overlapped with each other.

一方、電極板ユニット10を構成する各電極板10d,10eは、各スペーサ10a,10bの外枠部11,12に丁度嵌り込む幅寸法に、かつ、各縦枠部13の段差部13a,13bにはとどかない長さ寸法に形成されている。各電極板10d,10eは各スペーサ10a,10bの外枠部11,12内に嵌合された状態では、各スペーサ10a,10bに挟持された隔膜10cの一方の側面と電極板10dとの間に、例えば、陽極側電解室を構成し、隔膜10cの他方の側面と電極板10eとの間に、例えば、陰極側電解室を構成する。     On the other hand, the electrode plates 10d and 10e constituting the electrode plate unit 10 have a width dimension that fits just into the outer frame portions 11 and 12 of the spacers 10a and 10b, and step portions 13a and 13b of the vertical frame portions 13 respectively. It is formed in a length dimension that does not reach. In a state where the electrode plates 10d and 10e are fitted in the outer frame portions 11 and 12 of the spacers 10a and 10b, the gap between one side surface of the diaphragm 10c sandwiched between the spacers 10a and 10b and the electrode plate 10d. For example, an anode-side electrolysis chamber is formed, and, for example, a cathode-side electrolysis chamber is formed between the other side surface of the diaphragm 10c and the electrode plate 10e.

かかる構成の電極板ユニット10は、その複数を互いに重合した状態で筺体20内に収容されている。また、当該収容状態では、上記したように、各電極板ユニット10を構成する隔膜10cの一方の側面と電極板10d間、および、隔膜10cの他方の側面と電極板10e間に、陽極側電解室および陰極側電解室からなる電解室が構成されている。
また、各電解室の上方の部位Dには、図4(c)に示すように、隣り合う同士のスペーサ10a,10bの各縦枠部13に設けた段差部13a,13bが互いに対向して隙間Eを形成している。当該隙間Eには、電解板10d,10eの上端部はとどいておらず、隙間Eには位置していない。当該隙間Eは、各電解室内の上方の部位にて、その幅方向に所定間隔を保持して並列している。
The electrode plate unit 10 having such a configuration is accommodated in the housing 20 in a state where a plurality of the electrode plate units 10 are superposed on each other. In the accommodated state, as described above, anode-side electrolysis is performed between one side surface of the diaphragm 10c and the electrode plate 10d constituting each electrode plate unit 10 and between the other side surface of the diaphragm 10c and the electrode plate 10e. An electrolysis chamber comprising a chamber and a cathode side electrolysis chamber is constituted.
Further, as shown in FIG. 4C, the step portions 13a and 13b provided in the vertical frame portions 13 of the adjacent spacers 10a and 10b are opposed to each other in the portion D above each electrolysis chamber. A gap E is formed. The upper ends of the electrolytic plates 10d and 10e do not reach the gap E and are not located in the gap E. The gaps E are arranged in parallel at predetermined positions in the width direction at the upper part in each electrolytic chamber.

かかる構成の本発明に係る有隔膜電解槽Cにおいては、電解運転時には、希薄塩水である被電解水が供給管路31(31a,31b)を通して、各電極板ユニット10内の各電解室に連続して供給され、各電解室に供給された被電解水は、各スペーサ10a,10bの各縦枠部13にて区画されたチャンネル内を、各電極板10d,10eに沿って上方へ流動する。被電解水は、この間、各電解室にて有隔膜電解を受けて、陽極側電解室では電解生成酸性水が生成され、かつ、陰極側電解室では電解生成アルカリ性水が生成される。生成された各電解生成水は、各流出管路32a,32bを通して予め指定された場所に流出し、消費者に供されるか、排水される。   In the diaphragm electrolyzer C according to the present invention having such a configuration, during electrolysis operation, water to be electrolyzed, which is dilute salt water, continues to each electrolysis chamber in each electrode plate unit 10 through the supply pipes 31 (31a, 31b). The electrolyzed water supplied to the electrolysis chambers flows upward along the electrode plates 10d and 10e through the channels defined by the vertical frame portions 13 of the spacers 10a and 10b. . During this time, the electrolyzed water undergoes diaphragm membrane electrolysis in each electrolysis chamber, electrolysis-generated acidic water is generated in the anode-side electrolysis chamber, and electrolysis-generated alkaline water is generated in the cathode-side electrolysis chamber. The generated electrolyzed water flows out to a predetermined location through the outflow pipes 32a and 32b, and is supplied to consumers or drained.

ところで、当該有隔膜電解槽Cの電解運転においては、各電解室では電解生成酸性水および電解生成アルカリ性水が同期して生成されるが、その際、各電極板10d,10eの表面には塩素ガス、水素ガス等のガスが発生する。これらのガスは、各電解室内を上方へ流動する各電解生成水とともに上方へ移動する。従来の有隔膜電解槽では、発生した塩素ガス等は、各電解室内を上方へ移動してその上方の部位に漸次滞留することになる。   By the way, in the electrolysis operation of the diaphragm electrolyzer C, the electrolyzed acidic water and the electrolyzed alkaline water are generated synchronously in each electrolysis chamber. At that time, the surface of each electrode plate 10d, 10e is chlorine. Gases such as gas and hydrogen gas are generated. These gases move upward together with each electrolytically generated water flowing upward in each electrolytic chamber. In the conventional diaphragm membrane electrolytic cell, the generated chlorine gas or the like moves upward in each electrolytic chamber and gradually stays in the upper portion.

これに対して、本発明に係る有隔膜電解槽においては、各電解室の上方の部位に、各スペーサ10a,10bを構成する各縦枠部13の段差部13a,13bが形成する複数の隙間Eが、各電解室の幅方向に並列状態に存在する。このため、各電解室内を上方へ移動する塩素ガス等は、各隙間Eに集中的に捕捉されることになる。各隙間Eに捕捉された塩素ガス等は、各電解室の上方を導出口部に向かって流動する各電解生成水に伴って、各導出口部を経て、各流出管路32a,32bに流出し、系外へ排出される。   On the other hand, in the diaphragm electrolyzer according to the present invention, a plurality of gaps formed by the step portions 13a and 13b of the vertical frame portions 13 constituting the spacers 10a and 10b are formed in the upper portions of the electrolysis chambers. E exists in parallel in the width direction of each electrolytic chamber. For this reason, chlorine gas or the like moving upward in each electrolytic chamber is trapped in each gap E in a concentrated manner. Chlorine gas or the like trapped in each gap E flows out to the outflow pipes 32a and 32b through the outlets along with the electrolyzed water flowing above the electrolysis chambers toward the outlets. And discharged outside the system.

従って、本発明に係る有隔膜電解槽Cにおいては、各電解室で発生した塩素ガス等が各電解室内の上方の部位に大量に滞留することがなく、各電解生成水は大量に滞留する塩素ガス等に影響されることなく、各導出口部に円滑に導入して、各流出管路32a,32bを通して円滑に流出させることができる。
また、当該有隔膜電解槽Cにおいては、各電極板10d,10eの上端部が各隙間Eには臨んでいないため、各電極板10d,10eの上端部が各隙間Eに受け入れられ塩素ガス等に曝されることはなく、各電極板10d,10eの上端部の塩素ガス等による影響を一層確実に規制することができて、電極板10d,10eの早期の腐食を効果的に防止することができる。
Therefore, in the diaphragm electrolytic cell C according to the present invention, chlorine gas generated in each electrolysis chamber does not stay in a large amount in the upper part of each electrolysis chamber, and each electrolyzed water contains a large amount of chlorine. Without being influenced by gas or the like, the gas can be smoothly introduced into each outlet port and smoothly flowed out through the outflow pipes 32a and 32b.
Moreover, in the said diaphragm membrane electrolytic cell C, since the upper end part of each electrode plate 10d, 10e does not face each gap | interval E, the upper end part of each electrode plate 10d, 10e is received by each gap | interval E, chlorine gas etc. It is possible to more reliably regulate the influence of chlorine gas or the like at the upper end of each electrode plate 10d, 10e, and effectively prevent early corrosion of the electrode plates 10d, 10e. Can do.

本発明に係る有隔膜電解槽Cにおいては、電極板ユニット10の複数を互いに重合された状態で筺体20内に収容して、各電極板ユニット10を構成する各スペーサ10a,10bの縦枠部13の段差部13a,13bを互いに対向して位置させているので、互いに対向する段差部13a,13bによって大きな隙間Eを形成され、発生する塩素ガス等を大量に受け入れることができる利点がある。   In the diaphragm electrolytic cell C according to the present invention, a plurality of electrode plate units 10 are accommodated in the casing 20 in a state of being polymerized with each other, and the vertical frame portions of the spacers 10a and 10b constituting each electrode plate unit 10 are accommodated. Since the 13 step portions 13a and 13b are positioned to face each other, there is an advantage that a large gap E is formed by the step portions 13a and 13b facing each other and a large amount of generated chlorine gas or the like can be received.

A…装置本体、B…ケース、C…有隔膜電解槽、D…上方の部位、E…隙間、10…電極板ユニット、10a,10b…スペーサ、10c…隔膜、10d,10e…電極板、11,12…外枠部、11a,12a…下枠部位、11b,12b…上枠部位、11c,12c…左枠部位、11d,12d…右枠部位、11e,12e…嵌合凸部、11f,12f…嵌合凹部、13…縦枠部、13a,13b…段差部、20…筺体、31(31a,31b)…被電解水の供給管路、32a,32b…電解生成水の流出管路、33…原水供給管路、34…塩水供給管路。 A ... apparatus main body, B ... case, C ... diaphragm cell, D ... upper part, E ... gap, 10 ... electrode plate unit, 10a, 10b ... spacer, 10c ... diaphragm, 10d, 10e ... electrode plate, 11 , 12 ... Outer frame part, 11a, 12a ... Lower frame part, 11b, 12b ... Upper frame part, 11c, 12c ... Left frame part, 11d, 12d ... Right frame part, 11e, 12e ... Fitting convex part, 11f, 12f ... fitting recess, 13 ... vertical frame part, 13a, 13b ... step part, 20 ... housing, 31 (31a, 31b) ... supply line for electrolyzed water, 32a, 32b ... outflow pipe for electrolytically generated water, 33: Raw water supply pipe, 34 ... Salt water supply pipe.

Claims (3)

下方の部位に被電解水の導入口部を有するとともに上方の部位に電解生成水の導出口部を有する所定長さの筺体内に、一対の方形枠状のスペーサにて挟持された状態の隔膜の各側面側に前記各スペーサにて規定される間隔を保持して陽極側の電極板と陰極側の電極板をそれぞれ配置してなる電極板ユニットを1または複数収容してなり、前記電極板ユニットが形成する各電解室に流入して前記各電極板に沿って上方へ流動する被電解水を有隔膜電解するとともに、生成される電解生成水を前記各電解室から前記導出口部を通して流出するように構成した有隔膜電解槽であり、当該有隔膜電解槽においては、前記スペーサは、方形の外枠部の下枠部位から上枠部位に至る互いに所定間隔を保持して並列して延びる複数の縦枠部を備える格子状枠体であって、同格子状枠体の各縦枠部の上端部位には前記隔膜とは反対側に開口する凹状の段差部を備え、同段差部は対向する部材との間に隙間を形成し、同隙間は前記電解室の幅方向に複数並列していて、有隔膜電解時に前記電極板の表面にて発生するガスを捕捉し、捕捉したガスを電解生成水とともに前記導出口部へ導入すべく機能することを特徴とする有隔膜電解槽の電解槽構造。 A diaphragm in a state of being sandwiched by a pair of rectangular frame-like spacers within a predetermined length of a casing having an inlet for electrolyzed water at a lower portion and an outlet for electrolyzed water at an upper portion. One or a plurality of electrode plate units each including an electrode plate on the anode side and an electrode plate on the cathode side, each of which is provided with an interval defined by each spacer on each side surface of the electrode plate, Electrolyzed water flowing into the electrolysis chambers formed by the unit and flowing upward along the electrode plates is subjected to diaphragm electrolysis, and the generated electrolyzed water flows out from the electrolysis chambers through the outlet ports. In the diaphragm electrolytic cell, the spacers extend in parallel while maintaining a predetermined distance from the lower frame portion to the upper frame portion of the rectangular outer frame portion. Lattice frame with multiple vertical frames The upper end portion of each vertical frame portion of the lattice frame is provided with a concave step portion that opens to the opposite side of the diaphragm, and the step portion forms a gap with the opposing member. A plurality of the gaps are juxtaposed in the width direction of the electrolysis chamber, trapping gas generated on the surface of the electrode plate during electrolysis of the diaphragm, and introducing the trapped gas into the outlet port together with electrolyzed water. An electrolytic cell structure of a diaphragm electrolytic cell characterized by functioning as much as possible. 請求項1に記載の有隔膜電解槽の電解槽構造であり、当該有隔膜電解槽においては、前記電極板ユニットを構成する電極板は前記スペーサより短い寸法に形成されていて、同電極板の上端部は前記スペーサの縦枠部の段差部からは回避されていることを特徴とする有隔膜電解槽の電解槽構造。 It is an electrolytic cell structure of the diaphragm electrolytic cell according to claim 1, wherein the electrode plate constituting the electrode plate unit is formed in a shorter dimension than the spacer, The electrolytic cell structure of a diaphragm membrane electrolytic cell, wherein an upper end portion is avoided from a step portion of a vertical frame portion of the spacer. 請求項2に記載の有隔膜電解槽の電解槽構造であり、当該有隔膜電解槽においては、前記電極板ユニットの複数が互いに重合された状態で筺体内に収容されていて、前記各電極板ユニットを構成する各スペーサの縦枠部の段差部は互いに対向して前記隙間を形成していることを特徴とする有隔膜電解槽の電解槽構造。 3. The electrolytic cell structure of the diaphragm electrolytic cell according to claim 2, wherein a plurality of the electrode plate units are accommodated in a casing in a state of being polymerized to each other, and each of the electrode plates The electrolytic cell structure of a diaphragm membrane electrolytic cell, wherein the step portions of the vertical frame portions of the spacers constituting the unit face each other to form the gap.
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