JPH0512287Y2 - - Google Patents
Info
- Publication number
- JPH0512287Y2 JPH0512287Y2 JP1986145511U JP14551186U JPH0512287Y2 JP H0512287 Y2 JPH0512287 Y2 JP H0512287Y2 JP 1986145511 U JP1986145511 U JP 1986145511U JP 14551186 U JP14551186 U JP 14551186U JP H0512287 Y2 JPH0512287 Y2 JP H0512287Y2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen
- water
- electrolytic cell
- anode chamber
- cathode chamber
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 69
- 239000001257 hydrogen Substances 0.000 claims description 51
- 229910052739 hydrogen Inorganic materials 0.000 claims description 51
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 49
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 27
- 239000001301 oxygen Substances 0.000 claims description 27
- 229910052760 oxygen Inorganic materials 0.000 claims description 27
- 239000011261 inert gas Substances 0.000 claims description 17
- 238000000926 separation method Methods 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 6
- 150000002431 hydrogen Chemical class 0.000 claims description 5
- 239000005518 polymer electrolyte Substances 0.000 claims description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 16
- 229910021645 metal ion Inorganic materials 0.000 description 11
- 229910052757 nitrogen Inorganic materials 0.000 description 8
- 238000005868 electrolysis reaction Methods 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- 239000002184 metal Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 238000011109 contamination Methods 0.000 description 5
- 238000007599 discharging Methods 0.000 description 5
- 230000007423 decrease Effects 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000012159 carrier gas Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000008346 aqueous phase Substances 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000002829 nitrogen Chemical class 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
Landscapes
- Sampling And Sample Adjustment (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
【考案の詳細な説明】
(イ) 産業上の利用分野
この考案は水素発生装置に関する。さらに詳し
くはガスクロマトグラフの水素炎イオン化検出器
またはキヤリアガス等に使用される水素ガス供給
源として好適な水素発生装置に関する。[Detailed explanation of the invention] (a) Industrial application field This invention relates to a hydrogen generator. More specifically, the present invention relates to a hydrogen generator suitable as a hydrogen gas supply source used in a hydrogen flame ionization detector or carrier gas of a gas chromatograph.
(ロ) 従来の技術
ガスクロマトグラフの検出器またはキヤリアガ
スに使用される水素ガス供給源として好適な水素
発生装置としては、一対の電極を両面に有する高
分子電解質を隔膜として陽極室および陰極室が構
成された電解セルと、陽極室および陰極室へ各々
弁を介して水を供給する給水槽と、上記一対の電
極間に電圧を印加する電圧印加手段と、陰極室か
ら発生水素含有水を放出し水分離部へ延設される
水素放出流路および陽極室から発生酸素含有水を
放出する酸素放出流路とを備え、さらに前記水分
離部で水素ガスと分離される水を給水槽へ戻す戻
し流路が付設された構成のものが知られている。(b) Prior Art A hydrogen generator suitable as a hydrogen gas supply source used for a gas chromatograph detector or a carrier gas has an anode chamber and a cathode chamber configured with a polymer electrolyte diaphragm having a pair of electrodes on both sides. a water supply tank that supplies water to the anode chamber and the cathode chamber through valves, a voltage application means that applies a voltage between the pair of electrodes, and discharges generated hydrogen-containing water from the cathode chamber. It includes a hydrogen release channel extending to the water separation section and an oxygen release channel for discharging generated oxygen-containing water from the anode chamber, and further returns the water separated from hydrogen gas in the water separation section to the water tank. A structure in which a flow path is provided is known.
(ハ) 考案が解決しようとする問題点
しかしながら上記電解質セルを使用する水素発
生装置は、低価格、高効率、高純度等の利点を有
しかつ電解質溶液を用いず純水のみで電解できる
利点を有するが、純水中に金属イオンが混入して
いると上記セル内ことに電極表面に該金属が析出
してセルを汚染し、水素発生の効率が急に低下す
る。このため従来より供給する純水に金属イオン
が混入しないように充分注意する必要があり、ま
た一旦セルが汚染されると交換するまで使用でき
ないという問題もある。(c) Problems that the invention aims to solve However, the hydrogen generator using the above electrolyte cell has advantages such as low cost, high efficiency, and high purity, and the advantage that it can perform electrolysis only with pure water without using an electrolyte solution. However, if metal ions are mixed in the pure water, the metals will precipitate inside the cell, especially on the electrode surface, contaminating the cell, and the efficiency of hydrogen generation will suddenly decrease. For this reason, it is necessary to take great care to prevent metal ions from being mixed into the pure water conventionally supplied, and there is also the problem that once the cell becomes contaminated, it cannot be used until it is replaced.
この考案はかかる状況に鑑み為されたものであ
り、ことに上記電解セルの水素発生効率を良好に
維持しうる機構を備えた水素発生装置を提供しよ
うとするものである。 This invention was devised in view of the above situation, and is particularly intended to provide a hydrogen generation device equipped with a mechanism capable of maintaining the hydrogen generation efficiency of the electrolytic cell at a good level.
(ニ) 問題点を解決するための手段
かくしてこの考案によれば、一対の電極を両面
に有する高分子電解質を隔膜として陽極室および
陰極室が構成された電解セルと、陽極室および陰
極室へ各々弁を介して水を供給する給水槽と、陰
極室から発生水素含有水を放出し気液分離手段へ
延設される水素放出流路および陽極室から発生酸
素含有水を放出する酸素放出流路から構成されて
なり、
上記陽極室および陰極室それぞれに不活性ガス
導入管路および排水用管路が付設され、
電解セルへの給水を停止した後陽極室および陰
極室に不活性ガスを導入してこれらの室の残存水
をそれぞれの排水用管路から排水し次いでこれら
の室に水を導入しこの状態で前記一対の電極間に
逆電圧を印加すべく制御しうる制御手段が具備さ
れてなる水素発生装置が提供される。(d) Means for solving the problem Thus, according to this invention, an electrolytic cell is provided in which an anode chamber and a cathode chamber are constructed using a polymer electrolyte having a pair of electrodes on both sides as a diaphragm, and an anode chamber and a cathode chamber are connected to the anode chamber and the cathode chamber. A water supply tank that supplies water through valves, a hydrogen discharge channel that discharges generated hydrogen-containing water from the cathode chamber and extends to the gas-liquid separation means, and an oxygen discharge flow that discharges generated oxygen-containing water from the anode chamber. The anode chamber and cathode chamber are each equipped with an inert gas introduction conduit and a drainage conduit, and after stopping the water supply to the electrolytic cell, inert gas is introduced into the anode and cathode chambers. control means is provided which can control the residual water in these chambers to be drained from the respective drainage pipes, then introduce water into these chambers, and apply a reverse voltage between the pair of electrodes in this state. A hydrogen generator is provided.
この考案の水素発生装置は、水を電気分解して
水素を発生させる電解セルが水素発生用の通常の
電圧およびその逆電圧の印加を可能に構成されか
つ該電解セル内からの速やかな気体・液体の排出
機構を有し、通常の電圧による電解の後所定時間
逆電圧を印加して該電解セル内ことに電極上に析
出した金属をイオン化して溶解しかつこの金属イ
オン含有水溶液を電解セル外へ排出することによ
り電解セル内の金属イオンによる汚染を除去しう
るよう構成されたことを特徴とする。 In the hydrogen generating device of this invention, the electrolytic cell that electrolyzes water to generate hydrogen is configured to be able to apply a normal voltage for hydrogen generation and its reverse voltage, and the electrolytic cell can quickly generate gas and gas from within the electrolytic cell. It has a liquid discharge mechanism, and after electrolysis with a normal voltage, a reverse voltage is applied for a predetermined period of time to ionize and dissolve the metal deposited in the electrolytic cell and on the electrode, and this metal ion-containing aqueous solution is transferred to the electrolytic cell. It is characterized in that it is configured so that contamination by metal ions inside the electrolytic cell can be removed by discharging it to the outside.
上記電解セルは、一対の電極を両面に有する高
分子電解質を隔膜として陽極室および陰極室が構
成され、これらの各室に導入された水を一対の電
極間に印加された電圧により電気分解し、通常、
陽極室に酸素を陰極室に水素をそれぞれ発生する
よう構成されている。これら陽極室および陰極室
それぞれに付設される不活性ガス導入管路および
排水用管路は、これらの各室からの気体・液体の
排出を意図する以外は通常使用しないため、弁が
設けられる。弁は各排水用管路および各不活性ガ
ス導入管路それぞれに独立して設定されてもよい
が、各排水用管路をその排出口部で1つの管路に
合流してこの合流管路に1つの弁を設定するもの
であつてもよく、同じく各不活性ガス導入管路も
その不活性ガス供給部からの1つの供給路を分岐
して各不活性ガス導入管路に構成されている場合
分岐手前の供給路に1つの弁を設定するものであ
つてもよい。 The electrolytic cell described above has an anode chamber and a cathode chamber configured using a polymer electrolyte diaphragm having a pair of electrodes on both sides, and water introduced into each of these chambers is electrolyzed by a voltage applied between the pair of electrodes. ,usually,
It is configured to generate oxygen in the anode chamber and hydrogen in the cathode chamber. The inert gas introduction conduit and drainage conduit attached to each of the anode and cathode chambers are provided with valves because they are normally not used except for the purpose of discharging gas and liquid from each of these chambers. The valve may be set independently for each drainage pipe and each inert gas introduction pipe, but the valve may be set independently for each drainage pipe and each inert gas introduction pipe, but the valve may be set independently for each drainage pipe and each inert gas introduction pipe. Similarly, each inert gas introduction pipe may be configured such that one supply line from the inert gas supply section is branched to form each inert gas introduction pipe. If there is, one valve may be installed in the supply path before the branch.
上記電解セルの陽極室に設定される酸素放出流
路は、通常給水槽に接続されるものが好ましい。 The oxygen release channel set in the anode chamber of the electrolytic cell is preferably connected to a normal water supply tank.
この考案の装置において電解セルの陽極室およ
び陰極室からの気体・液体の排出を行うときは、
上記不活性ガス導入路から導入される不活性ガス
圧により行うため、このとき排水用管路以外の流
路を機密に保持しうるよう構成されるものが排水
の効率の点で好ましく、従つて上記酸素放出流路
および水素放出流路に弁が設定されることが好ま
しい。 When discharging gas and liquid from the anode chamber and cathode chamber of the electrolytic cell in the device of this invention,
Since this is carried out using the inert gas pressure introduced from the above-mentioned inert gas introduction path, it is preferable in terms of drainage efficiency that the flow path other than the drainage pipe be kept secret. Preferably, valves are provided in the oxygen release channel and the hydrogen release channel.
この考案の装置の制御においては、上記電解セ
ルへの給水を停止した後、該電解セルの一対の電
極に逆電圧を印加するに先立つて陽極室および陰
極室に不活性ガスを導入して各室内、水素放出流
路内および酸素放出流路内に残存している発生水
素含有水および発生酸素含有水を排出するが、こ
れは逆電圧の印加により陽極室に水素、陰極室に
酸素が発生し、水素と酸素が混在して爆発が生ず
る危険を避ける点で必要な作動である。 In controlling the device of this invention, after stopping the water supply to the electrolytic cell and before applying a reverse voltage to the pair of electrodes of the electrolytic cell, an inert gas is introduced into the anode chamber and the cathode chamber. The generated hydrogen-containing water and generated oxygen-containing water remaining indoors, in the hydrogen release channel, and in the oxygen release channel are discharged, but this is because hydrogen is generated in the anode chamber and oxygen is generated in the cathode chamber by applying a reverse voltage. However, this operation is necessary to avoid the risk of explosion due to the mixture of hydrogen and oxygen.
上記制御において、不活性ガスの導入により電
解セル内から気体・液体の排出を行うときは電解
セルへの電圧の印加を停止しうる制御がなされる
ことが好ましい。 In the above-mentioned control, it is preferable that the control is such that when the gas/liquid is discharged from the electrolytic cell by introducing an inert gas, the application of voltage to the electrolytic cell is stopped.
この考案の装置において、逆電圧の印加により
電解セル内ことに電極上の析出金属を除去する時
期としては、水素の発生効率が低下してきたとき
に随時行うように制御部に指示してもよく、また
定期的に行うように予め制御部の作動に組込んで
おくものであつてもよい。 In the device of this invention, the control unit may be instructed to remove the metal deposited inside the electrolytic cell and on the electrodes by applying a reverse voltage whenever the hydrogen generation efficiency decreases. Alternatively, it may be incorporated in advance into the operation of the control unit so as to be performed periodically.
この考案の装置に用いられる不活性ガスとして
は、窒素ガスが好ましい。 Nitrogen gas is preferred as the inert gas used in the device of this invention.
(ホ) 作用
この考案によれば、電気分解による水素の発生
後、電解セル内に不活性ガスが導入されて陽極室
内および陰極室内に保留されている発生酸素含有
水および発生水素含有水が排水され、次いでこれ
らの各室内に給水されて逆電圧を所定時間印加さ
れて析出した金属が水相中に金属イオンとして溶
解され、その後該金属イオン含有水溶液が不活性
ガスの導入により電解セル外へ排出されて金属イ
オンによる汚染が除去された後再び該電解セル内
に給水されて通常の電圧で水素発生が続行され
る。(E) Effect According to this invention, after hydrogen is generated by electrolysis, an inert gas is introduced into the electrolysis cell, and the generated oxygen-containing water and generated hydrogen-containing water retained in the anode chamber and the cathode chamber are drained. Water is then supplied into each of these chambers and a reverse voltage is applied for a predetermined period of time to dissolve the precipitated metal into the aqueous phase as metal ions, after which the metal ion-containing aqueous solution is forced out of the electrolytic cell by introducing an inert gas. After being discharged to remove contamination by metal ions, water is again supplied into the electrolytic cell and hydrogen generation is continued at a normal voltage.
以下実施例によりこの考案を詳細に説明する
が、これによりこの考案は限定されるものではな
い。 This invention will be explained in detail below with reference to examples, but the invention is not limited thereby.
(ヘ) 実施例
第1図はこの考案の一実施例の構成説明図であ
る。図において水素発生装置1は、給水槽2から
電解セル3へ純水を供給する純水供給流路aと、
電解セル3から水分離部4へ発生水素含有水を移
送する水素放出流路bと、上記電解セル3で発生
する酸素を発生酸素含有水として放出する酸素放
出流路cと、前記水分離部4から給水槽2へ該分
離部で水素から分離した純水を戻す戻し流路d
と、該水分離部4で分離された水素を乾燥部5を
経て供給する水素供給流路eと、電解セルへの窒
素導入用管路fと制御部6とから構成されてい
る。(F) Embodiment FIG. 1 is an explanatory diagram of the configuration of an embodiment of this invention. In the figure, the hydrogen generator 1 includes a pure water supply channel a that supplies pure water from the water tank 2 to the electrolytic cell 3;
a hydrogen release channel b for transferring generated hydrogen-containing water from the electrolysis cell 3 to the water separation section 4; an oxygen release channel c for discharging oxygen generated in the electrolysis cell 3 as generated oxygen-containing water; and the water separation section. A return flow path d for returning pure water separated from hydrogen in the separation section from 4 to the water tank 2
, a hydrogen supply channel e for supplying hydrogen separated in the water separation section 4 via a drying section 5 , a pipe f for introducing nitrogen into the electrolytic cell, and a control section 6 .
電解セル3は一対の電極を両面に有する高分子
電解質を隔膜31として陰極室32および陽極室
33が構成されており、陰極室32には上記水素
放出流路bおよび排水用管路g1が、陽極室33に
は上記純水供給流路a、酸素放出流路cおよび排
水用管路g2がそれぞれ接続されている。また上記
一対の電極は制御部6に電気的に接続され、この
接続は該制御部内で正負切換可能に構成されてい
る。通常水素発生時は陰極室32側が負極に、陽
極室33側が正極に接続されている。 The electrolytic cell 3 includes a cathode chamber 32 and an anode chamber 33 using a polymer electrolyte diaphragm 31 having a pair of electrodes on both sides, and the cathode chamber 32 includes the hydrogen release channel b and the drainage pipe g1 . The pure water supply channel a, the oxygen release channel c, and the drainage pipe g2 are connected to the anode chamber 33, respectively. Further, the pair of electrodes are electrically connected to the control section 6, and this connection is configured to be switchable between positive and negative within the control section. Normally, when hydrogen is generated, the cathode chamber 32 side is connected to the negative electrode, and the anode chamber 33 side is connected to the positive electrode.
上記窒素導入用管路fは分岐部Aから2本の管
路f1,f2に分かれ、電解セル3近傍で一方f1は純
水供給流路aに、他方f2は水素放出流路bにそれ
ぞれ管路接続されている。 The nitrogen introduction pipe f is divided into two pipes f 1 and f 2 from the branch A, and near the electrolytic cell 3, one f 1 is connected to the pure water supply flow path a, and the other f 2 is a hydrogen discharge flow path. b, respectively.
また酸素放出流路cは給水槽2に接続され、陽
極室33から酸素と同時に流出する純水を給水槽
にもどしている。 Further, the oxygen release channel c is connected to the water supply tank 2, and returns the pure water that flows out from the anode chamber 33 together with oxygen to the water supply tank.
酸素放出流路c、戻し流路d、水素供給流路
e、窒素導入用管路f1,f2および排水用管路g1,
g2にはそれぞれ電磁弁Vc,Vd,Ve,Vf1,Vf2
およびVg1,Vg2が設定されており、これらの電
磁弁は制御部6に電気的に接続され該制御部から
の電気信号によりそれぞれ作動される。純水供給
流路a上のVaは逆止弁である。 Oxygen release channel c, return channel d, hydrogen supply channel e, nitrogen introduction pipes f 1 , f 2 and drainage pipe g 1 ,
G 2 has solenoid valves Vc, Vd, Ve, Vf 1 and Vf 2 , respectively.
, Vg 1 and Vg 2 are set, and these solenoid valves are electrically connected to the control section 6 and are respectively operated by electric signals from the control section. Va on the pure water supply channel a is a check valve.
次ぎにこの考案の装置の作動を説明する。 Next, the operation of the device of this invention will be explained.
まず制御部により電磁弁Vc,Vd,Veが開状
態にかつ電磁弁Vf1,Vf2,Vg1,Vg2が閉状態に
保持され、電極は陰極室側が負極に、陽極室側が
正極になるように切換接続され、電解セルが給水
槽からの純水で満たされた後一定の直流電圧(通
常2〜3V)が電解セルに印加されて電気分解が
開始され、陰極室には水素陽極室には酸素がそれ
ぞれ発生する。発生した水素は純水と共に水素放
出流路内を進み水分離部に流入して該水分離部で
水素は純水と分離され、ついで水素供給流路を進
み乾燥部で乾燥されて電磁弁を経て供給部に供給
される。一方水分離部で分離された純水は戻し流
路により給水槽に戻される。 First, the control unit holds the solenoid valves Vc, Vd, and Ve in the open state and the solenoid valves Vf 1 , Vf 2 , Vg 1 , and Vg 2 in the closed state, and the cathode chamber side becomes the negative electrode and the anode chamber side becomes the positive electrode. After the electrolytic cell is filled with pure water from the water tank, a constant DC voltage (usually 2 to 3 V) is applied to the electrolytic cell to start electrolysis, and the cathode chamber is connected to the hydrogen anode chamber. Oxygen is generated respectively. The generated hydrogen travels through the hydrogen discharge channel together with pure water, flows into the water separation section, where the hydrogen is separated from pure water, and then advances through the hydrogen supply channel, where it is dried in the drying section, and then the electromagnetic valve is removed. It is then supplied to the supply section. On the other hand, the pure water separated in the water separation section is returned to the water supply tank through the return channel.
また水素と同時に陽極室で発生する酸素は純水
と共に酸素放出流路内に放出され給水槽に移送さ
れて酸素は該給水槽から放出される。 Further, oxygen generated in the anode chamber at the same time as hydrogen is released into the oxygen release flow path together with pure water and transferred to the water tank, and the oxygen is released from the water tank.
上記作動が制御部に予め設定された時間続けら
れた後、該制御部は次のように装置を作動する。
まず電解セルの印加電圧を0Vにし次いで電磁弁
Vc,Vd,Veを閉状態にかつ電磁弁Vf1,Vf2,
Vg1,Vg2を開状態に切換える。と同時に窒素導
入用管路に窒素が導入されこの窒素圧により電解
セルの陰極室から残存水素および純水が、陽極室
から残存酸素および純水がそれぞれの排水用管路
から排出される。次ぎに電磁弁Vc,Vd,Veを
開状態にかつ電磁弁Vf1,Vf2,Vg1,Vg2を閉状
態に切換えて電解セル内に純水を満たした後電極
の極性を反対に切換接続して通常の場合の逆電圧
(−2V〜−3V)を所定時間(30秒間程度)電解
セルに印加する。次いで再び電解セルの印加電圧
を0Vにした後電磁弁Vc,Vd,Veを閉状態にか
つ電磁弁Vf1,Vf2,Vg1,Vg2を開状態に切換え
て陰極室および陽極室内の金属イオン含有水をそ
れぞれの排水用管路から窒素圧により排出する。
この後電磁弁Vc,Vd,Veを開状態にかつ電磁
弁Vf1,Vf2,Vg1,Vg2を閉状態に切換えさらに
電解セル中の電極の極性を反対に切換接続して通
常の水素発生を行う。 After the above operation continues for a period of time preset by the controller, the controller operates the device as follows.
First, set the applied voltage of the electrolytic cell to 0V, and then turn on the solenoid valve.
Vc, Vd, Ve are closed and solenoid valves Vf 1 , Vf 2 ,
Switch Vg 1 and Vg 2 to open state. At the same time, nitrogen is introduced into the nitrogen introduction pipe, and due to this nitrogen pressure, residual hydrogen and pure water are discharged from the cathode chamber of the electrolytic cell, and residual oxygen and pure water from the anode chamber are discharged from the respective drainage pipes. Next, open the solenoid valves Vc, Vd, Ve and close the solenoid valves Vf 1 , Vf 2 , Vg 1 , Vg 2 to fill the electrolytic cell with pure water, and then reverse the polarity of the electrodes. Connect it and apply the normal reverse voltage (-2V to -3V) to the electrolytic cell for a predetermined period of time (about 30 seconds). Next, after reducing the voltage applied to the electrolytic cell to 0V again, the solenoid valves Vc, Vd, and Ve are closed, and the solenoid valves Vf 1 , Vf 2 , Vg 1 , and Vg 2 are opened, and the metal in the cathode and anode chambers is removed. Ion-containing water is discharged from each drainage pipe using nitrogen pressure.
After this, the solenoid valves Vc, Vd, and Ve are opened, and the solenoid valves Vf 1 , Vf 2 , Vg 1 , and Vg 2 are closed, and the polarity of the electrodes in the electrolytic cell is reversed and connected. Perform occurrence.
上記作動により電解セルの中に析出した金属が
逆電圧により金属イオンとして溶解され、さらに
この金属イオン含有水が電解セルから排出されて
水素発生の効率が向上することとなる。 As a result of the above operation, the metal deposited in the electrolytic cell is dissolved as metal ions by the reverse voltage, and furthermore, this metal ion-containing water is discharged from the electrolytic cell, thereby improving the efficiency of hydrogen generation.
(ト) 考案の効果
この考案によれば、電解セルが金属イオンに基
づく汚染により水素発生効率が低下した際、該汚
染が簡便に除去できかつ該電解セルの使用を続行
できるので、該セルを交換する手間がかからず水
素発生が効率良く行える。また定期的に金属イオ
ンによる汚染を除去することにより電解セルの損
傷を少なくし長期間にわたつて使用することがで
きる。(g) Effects of the invention According to this invention, when the hydrogen generation efficiency of an electrolytic cell decreases due to contamination based on metal ions, the contamination can be easily removed and the electrolytic cell can be continued to be used. Hydrogen can be generated efficiently without the need for replacement. Furthermore, by periodically removing contamination caused by metal ions, damage to the electrolytic cell can be reduced and it can be used for a long period of time.
第1図はこの考案の一実施例の構成説明図であ
る。
2……給水槽、3……電解セル、4……水分離
部、5……乾燥部、6……制御部、31……電
極、32……陰極室、33……陽極室、a……純
水供給流路、b……水素放出流路、c……酸素放
出流路、d……戻し流路、e……水素供給流路、
f……窒素導入用管路、g1,g2……排水用管路、
Vc,Vd,Ve,Vf1,Vf2,Vg1,Vg2……電磁
弁。
FIG. 1 is an explanatory diagram of the configuration of an embodiment of this invention. 2... Water supply tank, 3... Electrolytic cell, 4... Water separation section, 5... Drying section, 6... Control section, 31... Electrode, 32... Cathode chamber, 33... Anode chamber, a... ...Pure water supply channel, b...Hydrogen release channel, c...Oxygen release channel, d...Return channel, e...Hydrogen supply channel,
f...Nitrogen introduction pipe, g1 , g2 ...Drainage pipe,
Vc, Vd, Ve, Vf 1 , Vf 2 , Vg 1 , Vg 2 ... Solenoid valve.
Claims (1)
として陽極室および陰極室が構成された電解セル
と、電解セルに水を給水槽から供給する水供給流
路と、陰極室から発生水素含有水を放出し気液分
離手段へ延設される水素放出流路および陽極室か
ら発生酸素含有水を放出する酸素放出流路から構
成されてなり、 上記陽極室および陰極室それぞれに不活性ガス
導入管路と、陽極室および陰極室の残存水を排水
しうる排水用管路が付設され、 前記一対の電極間に印加される電圧を正負切換
可能に構成した制御部を具備してなる水素発生装
置。[Claims for Utility Model Registration] An electrolytic cell in which an anode chamber and a cathode chamber are constructed using a polymer electrolyte having a pair of electrodes on both sides as a diaphragm, and a water supply channel that supplies water to the electrolytic cell from a water tank; The anode chamber and the cathode chamber are composed of a hydrogen discharge channel that discharges the generated hydrogen-containing water from the cathode chamber and extends to the gas-liquid separation means, and an oxygen discharge channel that discharges the generated oxygen-containing water from the anode chamber. Each is provided with an inert gas introduction pipe and a drainage pipe for draining residual water in the anode chamber and the cathode chamber, and a control unit configured to be able to switch the voltage applied between the pair of electrodes between positive and negative. A hydrogen generator equipped with:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1986145511U JPH0512287Y2 (en) | 1986-09-22 | 1986-09-22 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1986145511U JPH0512287Y2 (en) | 1986-09-22 | 1986-09-22 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6351250U JPS6351250U (en) | 1988-04-06 |
| JPH0512287Y2 true JPH0512287Y2 (en) | 1993-03-29 |
Family
ID=31057120
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1986145511U Expired - Lifetime JPH0512287Y2 (en) | 1986-09-22 | 1986-09-22 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0512287Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2026002230A (en) * | 2024-06-21 | 2026-01-08 | 株式会社日立製作所 | Water electrolysis system and method for controlling the water electrolysis system |
-
1986
- 1986-09-22 JP JP1986145511U patent/JPH0512287Y2/ja not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6351250U (en) | 1988-04-06 |
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