JP2541163Y2 - Hydrogen / oxygen mixed gas generator - Google Patents

Hydrogen / oxygen mixed gas generator

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Publication number
JP2541163Y2
JP2541163Y2 JP1991032228U JP3222891U JP2541163Y2 JP 2541163 Y2 JP2541163 Y2 JP 2541163Y2 JP 1991032228 U JP1991032228 U JP 1991032228U JP 3222891 U JP3222891 U JP 3222891U JP 2541163 Y2 JP2541163 Y2 JP 2541163Y2
Authority
JP
Japan
Prior art keywords
water
gas
hydrogen
liquid separation
cell
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
Application number
JP1991032228U
Other languages
Japanese (ja)
Other versions
JPH04118455U (en
Inventor
人見  周二
寿士 工藤
Original Assignee
日本電池株式会社
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Application filed by 日本電池株式会社 filed Critical 日本電池株式会社
Priority to JP1991032228U priority Critical patent/JP2541163Y2/en
Publication of JPH04118455U publication Critical patent/JPH04118455U/en
Application granted granted Critical
Publication of JP2541163Y2 publication Critical patent/JP2541163Y2/en
Anticipated expiration legal-status Critical
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Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】この考案は固体高分子電解質(以
下SPEという)セルを用いた水電解式の水素・酸素混
合ガス発生装置に関する。
BACKGROUND OF THE INVENTION The present invention relates to a water electrolysis type hydrogen / oxygen mixed gas generator using a solid polymer electrolyte (SPE) cell.

【0002】[0002]

【従来の技術】SPEセルを用いた従来の水素・酸素混
合ガス発生装置の流路構成を図2に示す。同図において
3は内部に陽極室4と陰極室5を備えたSPEセルであ
る。ポンプ2により水タンク1から流路13を経て強制
的に該陽極室4に供給された水は直流電源12から与え
られた電力により電解され、陽極室4で酸素ガスを、陰
極室5では水素ガスを発生する。この時、酸素ガスは電
気分解されなかった余剰の水とともに、一方水素ガスは
電気分解に伴ない陽極から陰極へ移動したわずかな水と
ともに気液分離タンク6へ送り込まれる。気液分離タン
ク6では、これらガスと水とは比重の差により分離され
る。
2. Description of the Related Art FIG. 2 shows a flow path configuration of a conventional hydrogen / oxygen mixed gas generator using an SPE cell. In the figure, reference numeral 3 denotes an SPE cell having an anode chamber 4 and a cathode chamber 5 therein. Water forcibly supplied to the anode chamber 4 from the water tank 1 via the flow path 13 by the pump 2 is electrolyzed by the electric power supplied from the DC power supply 12, and oxygen gas is supplied in the anode chamber 4 and hydrogen gas is supplied in the cathode chamber 5. Generates gas. At this time, the oxygen gas is sent to the gas-liquid separation tank 6 together with the surplus water that has not been electrolyzed, and the hydrogen gas together with the small amount of water that has moved from the anode to the cathode during the electrolysis. In the gas-liquid separation tank 6, these gases and water are separated by a difference in specific gravity.

【0003】気液分離タンク6上方に分離された水素・
酸素混合ガスは調圧器10により所定の圧力に調圧さ
れ、ガス出口11に接続されるバ−ナ等に供給される。
一方、気液分離タンク6下方に分離された水は、内部の
ガスの圧力を利用して、水面検知センサ7および8から
の信号により開閉する電磁弁9および流路14を経て大
気に開放され水タンク1へ断続的に戻される。ここで電
磁弁9の動作は、気液分離タンク6中の水面が上限検知
センサ7を越えると開となり、下限検知センサ8より下
がると閉となるよう電気的に接続されている。
The hydrogen separated above the gas-liquid separation tank 6
The oxygen mixed gas is regulated to a predetermined pressure by a pressure regulator 10 and supplied to a burner or the like connected to a gas outlet 11.
On the other hand, the water separated below the gas-liquid separation tank 6 is released to the atmosphere through the electromagnetic valve 9 and the flow path 14 which are opened and closed by signals from the water level detection sensors 7 and 8 using the pressure of the gas inside. It is returned to the water tank 1 intermittently. Here, the operation of the solenoid valve 9 is electrically connected so as to be opened when the water level in the gas-liquid separation tank 6 exceeds the upper limit detection sensor 7 and closed when the water level falls below the lower limit detection sensor 8.

【0004】[0004]

【考案が解決しようとする課題】水電解セルでは、とり
わけSPEセルにおいては、セルに送り込まれる水量の
管理が極めて重要である。なぜなら、水は電気分解の原
料であるばかりでなく電気分解に伴ない生じる熱をセル
外部へ持ち出す役目をしているからである。万が一、水
が不足状態となれば、セル内部の温度上昇によりSPE
セルや電極等に大きなダメ−ジが加わるばかりでなく、
両極がショ−トして発火する危険性がある。
SUMMARY OF THE INVENTION In a water electrolysis cell, particularly in an SPE cell, it is extremely important to control the amount of water sent into the cell. This is because water is not only a raw material for electrolysis, but also serves to bring out heat generated by electrolysis to the outside of the cell. Should the water shortage occur, the SPE may increase due to the temperature rise inside the cell.
Not only will large damage be added to cells and electrodes,
There is a risk that both poles will short out and catch fire.

【0005】しかるに従来の装置においては、セルへの
水の供給が過不足状態になったことを検知する機構が設
けられていない。これは、従来の流路機構を用いて過不
足状態を検知しようと思えば、流路13または流路14
に流量センサ等の高価で電気的処理の煩雑な構を取り
付けなければならないためと、流量のセンサの信頼性に
問題があるためである。
However, the conventional apparatus does not include a mechanism for detecting that the supply of water to the cell has become excessive or insufficient. This is because if it is desired to detect the excess or deficiency state using the conventional channel mechanism, the channel 13 or the channel 14
And because they must attach the complicated machine structure of the electrical processing expensive, such flow sensors, and there is a problem in reliability of the flow sensor.

【0006】本考案はこのような課題を解決するために
なされたものであり、その目的とするところは、構造が
簡単で、かつ安価な水量検知機能を有する、安全性の高
い水素・酸素混合ガス発生装置を提供するにある。
The present invention has been made to solve such a problem, and an object of the present invention is to provide a highly safe hydrogen / oxygen mixture having a simple structure and an inexpensive water amount detecting function. To provide a gas generator.

【0007】[0007]

【課題を解決するための手段】そこで、このような課題
を解決するためになしたのが、水電解セルと電解液貯蔵
手段と気液分離手段と水面位検出手段と第1の水還流手
段と第2の水還流手段とを有し、水電解セルはSPEセ
ルを有し、電解水貯蔵手段から送り込まれた水を電解に
より水素ガスと酸素ガスとを発生させるものであり、気
液分離手段は、水電解セルから送られてきた酸素ガスと
水素ガスと水とを気液分離するとともに、これらを一時
貯蔵するためのものであり、水面位検出手段は気液分離
手段中に貯った水面位を検出するためのものであり、第
1の水還流手段と第2の水還流手段とは気液貯蔵手段中
の水を水素・酸素混合ガスのガス圧を利用して電解水貯
蔵手段へ戻すためのものであって、第1の水還流手段は
水面位検出手段からの信号によりその流路を開閉するよ
う構成してあり、第2の水還流手段は電解水貯蔵手段と
気液分離手段の水貯蔵部とを常時連通するよう構成した
ものである、水素・酸素混合ガス発生手段装置の考案で
ある。
SUMMARY OF THE INVENTION In order to solve such a problem, a water electrolysis cell, an electrolytic solution storing means, a gas-liquid separating means, a water level detecting means, and a first water recirculating means are provided. And a second water recirculation means. The water electrolysis cell has an SPE cell. The water fed from the electrolyzed water storage means generates hydrogen gas and oxygen gas by electrolysis. The means is for gas-liquid separation of oxygen gas, hydrogen gas, and water sent from the water electrolysis cell and for temporarily storing them, and the water level detecting means is stored in the gas-liquid separation means. The first water recirculation means and the second water recirculation means use the gas pressure of the hydrogen / oxygen mixed gas to store the water in the gas-liquid storage means. The first water recirculation means is a water level detection means. The second water recirculation means is configured to always communicate between the electrolyzed water storage means and the water storage part of the gas-liquid separation means. It is a device of a mixed gas generating device.

【0008】[0008]

【作用】電解水貯蔵手段と気液分離手段の水貯蔵部とを
常時連通する第2の水還流手段を設けることにより、S
PEセルよりガスとともに送られてきた水を電解水貯蔵
手段へ還流させることができる。この還流量をSPEセ
ルの冷却に必要な水量に設定することで異常発熱を伴う
ことなく運転を続けることができる。SPEセルへの水
の供給量が、その冷却に必要な水量以下になると気液分
離タンクの水面が下限レベルを大きく下回るため、気液
分離タンクの下限センサの未検知状態が続く。これを信
号処理し、アラ−ム機能を持たせれば発熱によるセルの
劣化を未然に防ぐことができる。
By providing a second water recirculation means for constantly communicating the electrolyzed water storage means and the water storage section of the gas-liquid separation means,
Water sent with the gas from the PE cell can be returned to the electrolytic water storage means. By setting this reflux amount to the amount of water necessary for cooling the SPE cell, the operation can be continued without abnormal heat generation. When the amount of water supplied to the SPE cell becomes equal to or less than the amount of water required for cooling, the level of the water in the gas-liquid separation tank falls significantly below the lower limit level, so that the lower limit sensor of the gas-liquid separation tank remains undetected. If this is signal processed and an alarm function is provided, the deterioration of the cell due to heat generation can be prevented beforehand.

【0009】[0009]

【実施例】以下、本考案を好適な実施例を用いて説明す
る。図1は本考案の一実施例に係る水素・酸素混合ガス
発生装置の流路構成図である。同図において、3は内部
に陽極室4と陰極室を備えたSPEセルで、ポンプ2
により水タンク1から流路13を経て強制的に該陽極室
4に供給された水を、直流電源12から与えられた電力
により水分解し、陽極室4で酸素ガスを、陰極室5では
水素ガスを発生させる。この時酸素ガスは電気分解され
なかった余剰水とともに、一方水素ガスは電気分解に伴
い陽極から陰極へ移動したわずかな水とともに、気液分
離タンク6へ送り込まれる。気液分離タンク6ではこれ
らのガスと水とを比重の差により分離する。タンク上方
に分離されたガスは調圧器10により所定の圧力に調整
され、ガス出口11に接続されるバーナ等に供給され
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below using preferred embodiments. FIG. 1 is a flow diagram of a hydrogen / oxygen mixed gas generator according to an embodiment of the present invention. In the figure, reference numeral 3 denotes an SPE cell having an anode chamber 4 and a cathode chamber 5 therein.
The water supplied from the water tank 1 to the anode chamber 4 via the flow path 13 is decomposed by the power supplied from the DC power supply 12 so that oxygen gas is supplied in the anode chamber 4 and hydrogen gas is supplied in the cathode chamber 5. Generate gas. At this time, the oxygen gas is sent to the gas-liquid separation tank 6 together with the surplus water that has not been electrolyzed, and the hydrogen gas together with the slight water that has moved from the anode to the cathode during the electrolysis. In the gas-liquid separation tank 6, these gases and water are separated by a difference in specific gravity. The gas separated above the tank is adjusted to a predetermined pressure by a pressure regulator 10 and supplied to a burner or the like connected to a gas outlet 11.

【0010】一方、タンク6の下方に分離された水は、
上方のガス圧を利用して、あらかじめセルの冷却に必要
な水量だけが流れるようニードルバルブ15により適当
に調整された常に開状態の流路16および水面検知セン
サ7およびからの信号により開閉する電磁弁9を途中
設けた流路14を経て、大気に開放された水タンク1に
連続的または断続的に戻る。ここで電磁弁9の動作は気
液分離タンク6の水面が上限センサ7の検知レベルを越
えると開となり、その水面が下限センサ8の検知レベル
より下がると閉となるように各センサと接続されてい
る。また、下限センサには連続して一定時間以上水を検
知しないと装置全体を停止させるアラーム回路が設けて
ある。
On the other hand, the water separated below the tank 6
Utilizing the upper gas pressure, it is opened and closed by signals from the always open channel 16 and the water level detection sensors 7 and 8 appropriately adjusted by the needle valve 15 so that only the amount of water necessary for cooling the cell flows in advance. It returns continuously or intermittently to the water tank 1 opened to the atmosphere via a flow path 14 provided with a solenoid valve 9 in the middle. Here, the operation of the solenoid valve 9 is connected to each sensor so as to be opened when the water level of the gas-liquid separation tank 6 exceeds the detection level of the upper limit sensor 7 and closed when the water level falls below the detection level of the lower limit sensor 8. ing. Further, the lower limit sensor is provided with an alarm circuit that stops the entire apparatus unless water is continuously detected for a predetermined time or more.

【0011】上述のように構成された本考案の装置は、
ガスとともにSPEセル3より気液分離タンク6に送り
込まれた水のうちSPEセル3の冷却に必要な水量分は
流路16より連続的に水タンク1へ戻されるが、それ以
上の水量分については液面センサ7および8からの信号
により開閉する電磁弁9を設けた流路14を経て断続的
に水タンクに戻される。ここでSPEセル3に送られる
水が不足状態となり、気液分離タンク6に送り込まれる
水量がSPEセル3の冷却に必要な水量以下となれば、
電磁弁9が閉の状態であっても気液分離タンク6の水面
は下がりつづけ、そして下限センサ8の検知レベルを下
回り、センサ8は未検知状態が続く。設定時間以上その
状態が続くと、アラ−ム回路作動により装置は停止し、
SPEセル3の内部の発熱によるSPEや電極等の劣化
を未然に回避することができる。
[0011] The device of the present invention configured as described above,
Of the water sent from the SPE cell 3 to the gas-liquid separation tank 6 together with the gas, the amount of water necessary for cooling the SPE cell 3 is continuously returned to the water tank 1 through the flow path 16. Is intermittently returned to the water tank via a flow path 14 provided with an electromagnetic valve 9 which opens and closes in response to signals from the liquid level sensors 7 and 8. Here, if the amount of water sent to the SPE cell 3 becomes insufficient and the amount of water sent to the gas-liquid separation tank 6 becomes equal to or less than the amount of water necessary for cooling the SPE cell 3,
Even when the solenoid valve 9 is closed, the water surface of the gas-liquid separation tank 6 continues to drop, falls below the detection level of the lower limit sensor 8, and the sensor 8 remains undetected. If the condition continues for more than the set time, the device stops due to the alarm circuit operation,
Deterioration of the SPE, electrodes, etc. due to heat generation inside the SPE cell 3 can be avoided beforehand.

【0012】[0012]

【考案の効果】従来の流路機構に、新たに常時連通する
流路を設けることにより、構造が簡単かつ安価な水量検
知機能を有した安全性の高い水素・酸素混合ガス発生装
置を提供するもので、産業上の発達に寄与すること非常
に大である。
The present invention provides a highly safe hydrogen / oxygen mixed gas generator having a simple and inexpensive water amount detection function by providing a new flow path that is always in communication with the conventional flow path mechanism. It is very important to contribute to industrial development.

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

【図1】本考案の1実施例である水素・酸素混合ガス発
生装置の流路図である。
FIG. 1 is a flow diagram of a hydrogen / oxygen mixed gas generator according to one embodiment of the present invention.

【図2】従来装置の流路図である。FIG. 2 is a flow chart of a conventional device.

【符号の説明】[Explanation of symbols]

1 電解水貯蔵タンク 2 ポンプ 3 SPEセル 6 気液分離タンク 7、8 液面センサ 9 電磁弁 10 調圧器 12 直流電源 Reference Signs List 1 electrolyzed water storage tank 2 pump 3 SPE cell 6 gas-liquid separation tank 7, 8 liquid level sensor 9 solenoid valve 10 pressure regulator 12 DC power supply

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭63−250481(JP,A) 実開 平2−51263(JP,U) 実開 昭64−7267(JP,U) 実開 昭63−69162(JP,U) 実開 平3−74670(JP,U) 実開 平4−64569(JP,U) ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-63-250481 (JP, A) JP-A-2-51263 (JP, U) JP-A 64-7267 (JP, U) JP-A-63-267 69162 (JP, U) Japanese Utility Model 3-74670 (JP, U) Japanese Utility Model 4-64569 (JP, U)

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 水電解セル(3)と電解水貯蔵手段
(1)と気液分離手段(6)と水面位検出手段(7、
8)と第1の水還流手段(14)と第2の水還流手段
(16)とを有し、水分解セル(3)は固体高分子電解
質を有し、電解水貯蔵手段(1)から送り込まれた水を
電解することにより水素ガスと酸素ガスとを発生させる
ものであり、 気液分離手段(6)は、水電解セルから
送られてきた酸素ガスと水素ガスと水とを気液分離する
とともに、これらを一時貯蔵するためのものであり、水
面位検出手段(7、8)は、気液分離手段(6)中に貯
った水面位を検出するためのものであり、第1の水還流
手段(14)と第2の水還流手段(16)とは気液貯蔵
手段(6)中の水を水素・酸素混合ガスのガス圧を利用
して電解水貯蔵手段(1)へ戻すためのものであって、
第1の水還流手段(14)は水面位検出手段(7、8)
からの信号によりその流路を開閉するよう構成してあ
り、第2の水還流手段(16)は、電解水貯蔵手段
(1)と気液分離手段(6)の水貯蔵部とを常時連通す
るよう構成したものである、水素・酸素混合ガス発生装
置。
1. A water electrolysis cell (3), an electrolyzed water storage means (1), a gas-liquid separation means (6), and a water level detection means (7,
8), a first water reflux means (14) and a second water reflux means (16), the water splitting cell (3) has a solid polymer electrolyte, Hydrogen gas and oxygen gas are generated by electrolyzing the supplied water. The gas-liquid separation means (6) separates the oxygen gas, hydrogen gas, and water sent from the water electrolysis cell into gas and liquid. The water level detecting means (7, 8) is for detecting the water level stored in the gas-liquid separating means (6) while separating and temporarily storing them. The first water recirculation means (14) and the second water recirculation means (16) convert the water in the gas-liquid storage means (6) into an electrolyzed water storage means (1) by utilizing the gas pressure of a hydrogen / oxygen mixed gas. To return to
The first water recirculation means (14) is a water level detection means (7, 8)
The second water recirculation means (16) constantly communicates the electrolyzed water storage means (1) with the water storage part of the gas-liquid separation means (6). A hydrogen / oxygen mixed gas generator configured to perform
JP1991032228U 1991-04-09 1991-04-09 Hydrogen / oxygen mixed gas generator Expired - Lifetime JP2541163Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991032228U JP2541163Y2 (en) 1991-04-09 1991-04-09 Hydrogen / oxygen mixed gas generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991032228U JP2541163Y2 (en) 1991-04-09 1991-04-09 Hydrogen / oxygen mixed gas generator

Publications (2)

Publication Number Publication Date
JPH04118455U JPH04118455U (en) 1992-10-22
JP2541163Y2 true JP2541163Y2 (en) 1997-07-09

Family

ID=31915241

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991032228U Expired - Lifetime JP2541163Y2 (en) 1991-04-09 1991-04-09 Hydrogen / oxygen mixed gas generator

Country Status (1)

Country Link
JP (1) JP2541163Y2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100407481B1 (en) * 2000-12-01 2003-12-06 오둔영 Hydrogen gas occurrence equipment
JP2013209735A (en) * 2012-03-30 2013-10-10 Equos Research Co Ltd Sunlight utilization system

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0251263U (en) * 1988-09-29 1990-04-10

Also Published As

Publication number Publication date
JPH04118455U (en) 1992-10-22

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