JPH0740769U - Horizontal multi-stage electrolyzer - Google Patents
Horizontal multi-stage electrolyzerInfo
- Publication number
- JPH0740769U JPH0740769U JP069735U JP6973593U JPH0740769U JP H0740769 U JPH0740769 U JP H0740769U JP 069735 U JP069735 U JP 069735U JP 6973593 U JP6973593 U JP 6973593U JP H0740769 U JPH0740769 U JP H0740769U
- Authority
- JP
- Japan
- Prior art keywords
- flanges
- terminal case
- inlet nozzle
- outlet nozzle
- terminal
- 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.)
- Granted
Links
Abstract
(57)【要約】
【目的】 ガス溜りやスケール溜りの生じない横型多段
電解槽を得る。
【構成】 複数の電極板1が多段に配置され両端にフラ
ンジを持つ蓋付のチャンネル型の槽本体5を有する横型
多段電解槽において、槽本体の両端のフランジにそれぞ
れ接続され箱型で両端にフランジを持つ端子ケース4、
上流側および下流側の端子ケースにそれぞれ接続され両
端にフランジを持ちほぼ中央に同端子ケース方向に拡大
する流路を有する入口ノズル7、および出口ノズル8、
入口ノズルおよび出口ノズルのフランジの左右両端部か
ら流れ方向に端子ケース内にそれぞれ挿入され電極板に
接続される陰極通電棒7および陽極通電棒8を設ける。
(57) [Summary] [Purpose] To obtain a horizontal multi-stage electrolytic cell without gas accumulation or scale accumulation. [Structure] In a horizontal multi-stage electrolytic cell having a channel-type cell body 5 with a lid having a plurality of electrode plates 1 arranged in multiple stages and having flanges at both ends, a box-shaped cell is connected to the flanges at both ends of the cell body at both ends. Terminal case with flange 4,
An inlet nozzle 7 and an outlet nozzle 8, which are connected to the upstream and downstream terminal cases, respectively, have flanges at both ends, and have a flow passage extending substantially in the center toward the terminal case,
A cathode energizing rod 7 and an anode energizing rod 8 which are respectively inserted into the terminal case in the flow direction from both left and right ends of the flanges of the inlet nozzle and the outlet nozzle and connected to the electrode plate are provided.
Description
【0001】[0001]
本考案は、海水電気分解用の横型多段電解槽に関する。 The present invention relates to a horizontal multistage electrolytic cell for seawater electrolysis.
【0002】[0002]
従来例を図5〜図10により説明する。図6は縦断面図、図7は図6のB−B 断面図、図8は図6のC−C断面図、図9は図6のF−F断面図、図10は電極 板配置説明図である。 A conventional example will be described with reference to FIGS. 6 is a vertical sectional view, FIG. 7 is a sectional view taken along the line BB of FIG. 6, FIG. 8 is a sectional view taken along the line CC of FIG. 6, FIG. 9 is a sectional view taken along the line FF of FIG. 6, and FIG. It is a figure.
【0003】 図6にて、蓋6を持つチャンネル型の槽本体5の両端には端子ケース4が接続 される。さらにその両端には入口ノズル管7と出口ノズル管8とが接続される。 端子ケース4の上面にはガス抜きフランジ9が取付けられている。In FIG. 6, terminal cases 4 are connected to both ends of a channel type tank body 5 having a lid 6. Further, an inlet nozzle pipe 7 and an outlet nozzle pipe 8 are connected to both ends thereof. A gas vent flange 9 is attached to the upper surface of the terminal case 4.
【0004】 一方の端子ケース4の中央上下には陰極通電棒2が流れ方向に平行に挿入され 、電極板1につながれている。他方の端子ケース4にも同様に陽極通電棒3が挿 入され電極1につながれている(図6)。Cathode conducting rods 2 are inserted parallel to the flow direction above and below the center of one of the terminal cases 4 and are connected to the electrode plate 1. Similarly, the anode current-carrying rod 3 is inserted into the other terminal case 4 and connected to the electrode 1 (FIG. 6).
【0005】 槽本体5内の電極板1の配置は図9、図10に示すように、流れに平行にスタ ガに多段に配置されている。図中各電極板1の黒ぬり部が陽極になる。As shown in FIGS. 9 and 10, the electrode plates 1 in the tank body 5 are arranged in multiple stages in a stagger in parallel with the flow. In the figure, the black-colored portion of each electrode plate 1 serves as an anode.
【0006】 以上において、電流は+側通電棒2より電極板1へ流れ、各段の電極板1を順 次流れ−側通電棒3より電源装置へと流れる。この間に海水は電気分解され、次 亜塩素酸ソーダとなる。この時、通電棒2及び3の上部は電解時に生成する水素 ガスの溜り場となる。又下部は電解時に生成するスケールの溜り場となる。In the above description, the current flows from the + side current-carrying rod 2 to the electrode plate 1, and sequentially flows through the electrode plate 1 at each stage from the-side current-carrying rod 3 to the power supply device. During this time, seawater is electrolyzed into sodium hypochlorite. At this time, the upper portions of the current-carrying rods 2 and 3 serve as a reservoir for hydrogen gas generated during electrolysis. In addition, the lower part serves as a pool of scale generated during electrolysis.
【0007】[0007]
上記従来装置では、通電棒が上下に付いているため上部通電棒まわりが、電解 時に発生する水素ガスのガス溜りとなる。このガスを抜くために通電端子ケース にフランジを取り付け、ガス抜き用の配管を敷設しなければならなかった。 In the above-mentioned conventional device, since the current-carrying rods are attached to the upper and lower sides, the area around the upper current-carrying rod becomes a gas reservoir for hydrogen gas generated during electrolysis. In order to remove this gas, it was necessary to attach a flange to the energizing terminal case and lay out a gas exhaust pipe.
【0008】 又、下部通電棒まわりが電解時に発生するスケールの溜りとなり、定期的な清 掃が必要であった。In addition, around the lower energizing rod becomes a pool of scale generated during electrolysis, which requires periodic cleaning.
【0009】[0009]
本考案は上記課題を解決するため次の手段を講ずる。 The present invention takes the following measures to solve the above problems.
【0010】 すなわち、複数の電極板が多段に配置され両端にフランジを持つ蓋付のチャン ネル型の槽本体を有する横型多段電解槽において、上記槽本体の両端のフランジ にそれぞれ接続され箱型で両端にフランジを持つ端子ケースと、上流側および下 流側の上記端子ケースにそれぞれ接続され両端にフランジを持ちほぼ中央に同端 子ケース方向に拡大する流路を有する入口ノズルおよび出口ノズルと、上記入口 ノズルおよび出口ノズルの接続側フランジの左右両端部から流れ方向に上記端子 ケース内にそれぞれ挿入され上記電極板に接続される陰極通電棒および陽極通電 棒を設ける。That is, in a horizontal multi-stage electrolysis cell having a channel-type cell body with a lid having a plurality of electrode plates arranged in multiple stages and having flanges at both ends, a box-type is connected to the flanges at both ends of the cell body, respectively. A terminal case having flanges at both ends, an inlet nozzle and an outlet nozzle connected to the above-mentioned terminal case on the upstream side and the downstream side, respectively, and having flanges at both ends, and having a flow passage expanding in the direction of the same terminal case at substantially the center, A cathode energizing rod and an anode energizing rod which are respectively inserted into the terminal case in the flow direction from the left and right ends of the connection side flanges of the inlet nozzle and the outlet nozzle and connected to the electrode plate are provided.
【0011】[0011]
以上において、左右配置の陽極通電棒から陰極通電棒に電流が流される。さら に入口ノズルから海水が導入される。すると、槽本体内の各段の電極板で順次海 水が電気分される。このとき従来例のように上下に通電棒がないため、端子ケー ス下面および上面部は槽本体の上面および下面にそれぞれほぼなめらかにつなが れているので、流体はなめらかに流れる。このためガス溜りやスケール溜りが発 生しなくなる。 In the above, a current is passed from the left and right anode conducting rods to the cathode conducting rods. Furthermore, seawater is introduced from the inlet nozzle. Then, seawater is sequentially divided into electricity by the electrode plates at each stage in the tank body. At this time, unlike the conventional example, since there are no current-carrying rods on the upper and lower sides, the lower and upper surfaces of the terminal case are connected to the upper and lower surfaces of the tank body almost smoothly, so that the fluid flows smoothly. For this reason, gas pools and scale pools do not occur.
【0012】[0012]
本発明の一実施例を図1〜図5により説明する。 An embodiment of the present invention will be described with reference to FIGS.
【0013】 図1は縦断面図、図2は図1のA−A断面図、図3は図1のE−E断面図、図 4は図1のD−D視図である。図5は電極板配置説明図である。なお、従来例で 説明した部分は、同一の番号をつけ説明を省略し、この考案に関する部分を主体 に説明する。1 is a longitudinal sectional view, FIG. 2 is a sectional view taken along the line AA of FIG. 1, FIG. 3 is a sectional view taken along the line EE of FIG. 1, and FIG. 4 is a view taken along the line DD of FIG. FIG. 5 is an explanatory diagram of the electrode plate arrangement. The parts explained in the conventional example are given the same numbers and their explanations are omitted, and the parts relating to the present invention will be mainly explained.
【0014】 図1にて、槽本体5の両端フランジに、両端にフランジを持つ箱型の端子ケー ス4が接続される。各端子ケース4のフランジには、両端にフランジを持ち、ほ ぼ中央に端子ケース4側に拡大する流路を持つ入口ノズル7と出口ノズル8とが それぞれ接続される。入口ノズル7と出口ノズル8の接続側(基部側)フランジ の左右両端部から図2〜図5に示すように、陰極通電棒2と陽極通電棒3が、流 れ方向に端子ケース4内に挿入される。各通電棒2,3は左右両端の補強された 電極板1Aに溶接またはボルト等で接続される。In FIG. 1, a box-shaped terminal case 4 having flanges at both ends is connected to both end flanges of the tank body 5. An inlet nozzle 7 and an outlet nozzle 8 each having a flange at both ends and a flow passage extending to the terminal case 4 side at the center are connected to the flange of each terminal case 4, respectively. As shown in FIGS. 2 to 5, the cathode energizing rod 2 and the anode energizing rod 3 are placed in the terminal case 4 in the flowing direction from both left and right ends of the flange on the connecting side (base side) of the inlet nozzle 7 and the outlet nozzle 8. Is inserted. The current-carrying rods 2 and 3 are welded or connected to the reinforced electrode plates 1A at the left and right ends by bolts or the like.
【0015】 端子ケース4内の各電極板1,1Aの下部は上面bが槽本体5の下面(低面) にほぼ等しい高さを持つスペーサ11を介して保持されている。また上部は下面 cが槽本体5の下面にほぼ等しい高さを持つスペーサ12を介して保持されてい る。The lower part of each electrode plate 1, 1 A in the terminal case 4 is held via a spacer 11 whose upper surface b has a height substantially equal to the lower surface (lower surface) of the tank body 5. The lower surface c of the upper portion is held via a spacer 12 having a height substantially equal to the lower surface of the tank body 5.
【0016】 以上において、左右配置の陽極通電棒3から陰極通電棒2に電流が流される。 さらに入口ノズル7から海水が導入される。すると、槽本体5内の各段の電極板 1で順次海水が電気分される。このとき端子ケース4下面および上面部は槽本体 の上面および下面にそれぞれほぼなめらかにつながれている(スペーサ11の上 面b、12の下面c)ので、流体はなめらかに流れる。このためガス溜りやスケ ール溜りが発生しなくなる。In the above, a current is passed from the left and right anode conducting rods 3 to the cathode conducting rods 2. Further, seawater is introduced from the inlet nozzle 7. Then, the seawater is sequentially electrically divided by the electrode plates 1 at the respective stages in the tank body 5. At this time, the lower surface and the upper surface of the terminal case 4 are connected to the upper surface and the lower surface of the tank main body almost smoothly (the upper surface b of the spacer 11 and the lower surface c of the spacer 12), so that the fluid flows smoothly. For this reason, gas pools and scale pools do not occur.
【0017】 また構造的にも簡単になり、ガス抜きフランジや配管等も不要となる。このた め定期的清掃も不要となり安全かつメンテナンスフリーの運転ができる。Further, it is structurally simple, and a gas vent flange, piping, etc. are not required. This eliminates the need for regular cleaning and enables safe and maintenance-free operation.
【0018】[0018]
端子ケースの上面、下面がほぼなめらかに槽本体の上面、下面につながるので 、流体が滑らかに流れ危険な水素ガスの溜りがなくなる。又、スケール溜りもな くなる。 Since the upper and lower surfaces of the terminal case are connected to the upper and lower surfaces of the tank body almost smoothly, the fluid smoothly flows and dangerous hydrogen gas is not accumulated. In addition, there will be no scale accumulation.
【図1】本考案の一実施例の縦断面図である。FIG. 1 is a vertical sectional view of an embodiment of the present invention.
【図2】同実施例の図1のA−A断面図である。FIG. 2 is a sectional view taken along line AA of FIG. 1 of the same embodiment.
【図3】同実施例の図1のE−E断面図である。FIG. 3 is a sectional view taken along line EE in FIG. 1 of the same embodiment.
【図4】同実施例の図1のD−D視図である。FIG. 4 is a DD view of FIG. 1 of the embodiment.
【図5】同実施例の電極板配置の説明図である。FIG. 5 is an explanatory diagram of an electrode plate arrangement of the same embodiment.
【図6】従来例の縦断面図である。FIG. 6 is a vertical sectional view of a conventional example.
【図7】同従来例の図5のB−B断面図である。7 is a sectional view taken along line BB of FIG. 5 of the conventional example.
【図8】同従来例の図5のC−C断面図である。8 is a sectional view taken along line CC of FIG. 5 of the conventional example.
【図9】同従来例の図5のF−F断面図である。FIG. 9 is a sectional view taken along line FF of FIG. 5 of the conventional example.
【図10】同従来例の電極板配置説明図である。FIG. 10 is an explanatory view of the electrode plate arrangement of the conventional example.
1,1A 電極板 2 陰極通電棒 3 陽極通電棒 4 端子ケース 5 槽本体 6 蓋 7 入口ノズル 8 出口ノズル 10 流路 11,12 スペーサ 1, 1A Electrode plate 2 Cathode energizing rod 3 Anode energizing rod 4 Terminal case 5 Tank body 6 Lid 7 Inlet nozzle 8 Outlet nozzle 10 Flow path 11, 12 Spacer
───────────────────────────────────────────────────── フロントページの続き (72)考案者 原田 誠一 横浜市中区錦町12番地 三菱重工業株式会 社横浜製作所内 (72)考案者 関 奈保子 横浜市中区錦町12番地 三菱重工業株式会 社横浜製作所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Seiichi Harada, 12 Nishiki-cho, Naka-ku, Yokohama-shi, Mitsubishi Heavy Industries Ltd. Yokohama Works (72) Naoko Seki, 12 Nishiki-cho, Naka-ku, Yokohama Mitsubishi Heavy Industries, Ltd. Yokohama Works Within
Claims (1)
ランジを持つ蓋付のチャンネル型の槽本体を有する横型
多段電解槽において、上記槽本体の両端のフランジにそ
れぞれ接続され箱型で両端にフランジを持つ端子ケース
と、上流側および下流側の端子ケースにそれぞれ接続さ
れ両端にフランジを持ちほぼ中央に同端子ケース方向に
拡大する流路を有する入口ノズルおよび出口ノズルと、
上記入口ノズルおよび出口ノズルの接続側フランジの左
右両端部から流れ方向に上記端子ケース内にそれぞれ挿
入され上記電極板に接続される陰極通電棒および陽極通
電棒を備えてなることを特徴とする横型多段電解槽。1. A horizontal multi-stage electrolytic cell having a channel-type cell body with a lid having a plurality of electrode plates arranged in multiple stages and having flanges at both ends, and box-shaped both ends respectively connected to flanges at both ends of the cell body. A terminal case having a flange, and an inlet nozzle and an outlet nozzle that are connected to the upstream and downstream terminal cases, respectively, have flanges at both ends, and have a flow passage that expands in the same direction toward the terminal case at approximately the center.
A horizontal type comprising a cathode current-carrying rod and an anode current-carrying rod, which are respectively inserted into the terminal case in the flow direction from the left and right ends of the connection side flanges of the inlet nozzle and the outlet nozzle and are connected to the electrode plate. Multi-stage electrolyzer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1993069735U JP2601202Y2 (en) | 1993-12-27 | 1993-12-27 | Horizontal multi-stage electrolytic cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1993069735U JP2601202Y2 (en) | 1993-12-27 | 1993-12-27 | Horizontal multi-stage electrolytic cell |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0740769U true JPH0740769U (en) | 1995-07-21 |
JP2601202Y2 JP2601202Y2 (en) | 1999-11-15 |
Family
ID=13411375
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JP1993069735U Expired - Lifetime JP2601202Y2 (en) | 1993-12-27 | 1993-12-27 | Horizontal multi-stage electrolytic cell |
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JP (1) | JP2601202Y2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012070468A1 (en) * | 2010-11-22 | 2012-05-31 | 三菱重工環境・化学エンジニアリング株式会社 | Seawater electrolysis system and seawater electrolysis method |
JP2012111990A (en) * | 2010-11-22 | 2012-06-14 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co Ltd | Apparatus, system and method for electrolyzing seawater |
JP2015172251A (en) * | 2015-05-20 | 2015-10-01 | 三菱重工環境・化学エンジニアリング株式会社 | Seawater electrolysis system and seawater electrolysis method |
-
1993
- 1993-12-27 JP JP1993069735U patent/JP2601202Y2/en not_active Expired - Lifetime
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012070468A1 (en) * | 2010-11-22 | 2012-05-31 | 三菱重工環境・化学エンジニアリング株式会社 | Seawater electrolysis system and seawater electrolysis method |
JP2012111990A (en) * | 2010-11-22 | 2012-06-14 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co Ltd | Apparatus, system and method for electrolyzing seawater |
CN103201412A (en) * | 2010-11-22 | 2013-07-10 | 三菱重工环境·化学工程株式会社 | Seawater electrolysis system and seawater electrolysis method |
AU2011333018B2 (en) * | 2010-11-22 | 2014-07-03 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co., Ltd. | Seawater electrolysis system and seawater electrolysis method |
AU2011333018C1 (en) * | 2010-11-22 | 2014-09-25 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co., Ltd. | Seawater electrolysis system and seawater electrolysis method |
CN105239090A (en) * | 2010-11-22 | 2016-01-13 | 三菱重工环境·化学工程株式会社 | Seawater electrolysis system and seawater electrolysis method |
JP2015172251A (en) * | 2015-05-20 | 2015-10-01 | 三菱重工環境・化学エンジニアリング株式会社 | Seawater electrolysis system and seawater electrolysis method |
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Publication number | Publication date |
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JP2601202Y2 (en) | 1999-11-15 |
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