JPH0971886A - Water electrolysis device - Google Patents
Water electrolysis deviceInfo
- Publication number
- JPH0971886A JPH0971886A JP7248619A JP24861995A JPH0971886A JP H0971886 A JPH0971886 A JP H0971886A JP 7248619 A JP7248619 A JP 7248619A JP 24861995 A JP24861995 A JP 24861995A JP H0971886 A JPH0971886 A JP H0971886A
- Authority
- JP
- Japan
- Prior art keywords
- water
- electrolysis
- current
- electrode plates
- electrolytic 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.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 54
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 35
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000007789 gas Substances 0.000 claims description 33
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 2
- 229910001882 dioxygen Inorganic materials 0.000 claims description 2
- 230000000903 blocking effect Effects 0.000 claims 1
- 238000012856 packing Methods 0.000 abstract description 12
- 239000001257 hydrogen Substances 0.000 abstract description 10
- 229910052739 hydrogen Inorganic materials 0.000 abstract description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 7
- 239000001301 oxygen Substances 0.000 abstract description 7
- 229910052760 oxygen Inorganic materials 0.000 abstract description 7
- 239000008246 gaseous mixture Substances 0.000 abstract 2
- 230000010349 pulsation Effects 0.000 abstract 2
- 238000000354 decomposition reaction Methods 0.000 description 9
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 239000008151 electrolyte solution Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、水を電解して酸、
水素混合ガスを発生させる水電解装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention electrolyzes water to produce an acid,
The present invention relates to a water electrolysis device that generates a hydrogen mixed gas.
【0002】[0002]
【従来の技術及び発明が解決しようとする課題】水ある
いは電解質水溶液を電気分解して酸素と水素を発生さ
せ、その混合ガスを燃焼に利用する方法、装置が知られ
ている。そのような従来公知の水電解装置は、H−Oウ
ェルダー用の燃焼用ガス発生装置等として用いられてい
るが、水や電解質水溶液に直流通電が行なわれている。
ところが、直流電解方式では電流密度を増大させかつコ
ンパクトな装置により大量の混合ガスを発生させようと
すると、分極作用等により電流効率が大幅に低下し、発
生ガス量が理論値の数分の一程度になってしまうという
問題がある。2. Description of the Related Art There are known methods and apparatuses for electrolyzing water or an aqueous electrolyte solution to generate oxygen and hydrogen, and utilizing a mixed gas thereof for combustion. Such a conventionally known water electrolysis device is used as a combustion gas generation device for a HO welder, etc., but a direct current is applied to water or an electrolyte aqueous solution.
However, in the direct current electrolysis method, when an attempt is made to increase the current density and generate a large amount of mixed gas with a compact device, the current efficiency is significantly reduced due to the polarization effect, etc., and the amount of generated gas is a fraction of the theoretical value. There is a problem that it becomes a degree.
【0003】本発明はこのような従来の問題点に鑑みて
なしたもので、小型でありながら大量の酸、水素混合ガ
スを効率よく発生させることができる水電解装置を提供
することを目的とする。The present invention has been made in view of such conventional problems, and an object thereof is to provide a water electrolysis apparatus which is small in size and can efficiently generate a large amount of acid-hydrogen mixed gas. To do.
【0004】[0004]
【課題を解決するための手段】本発明のうち請求項1に
係る水電解装置は上記目的を達成するために、電解槽内
の電解用水中に電極板を多数枚並設し、これら電極板間
に電解電流を流して酸素ガス及び水素ガスを発生させ、
発生ガスを上記電解槽外へ供給可能とした水電解装置に
おいて、上記電極板間に脈流を通電する電源を備えると
ともに、該脈流の交流成分の周波数を、上記電解槽及び
内蔵する電極板等からなる構造体の共振周波数あるいは
その近傍としたことを特徴とする。In order to achieve the above object, a water electrolysis apparatus according to claim 1 of the present invention has a large number of electrode plates arranged side by side in electrolyzed water in an electrolytic cell. An electrolytic current is passed between them to generate oxygen gas and hydrogen gas,
In a water electrolysis apparatus capable of supplying generated gas to the outside of the electrolytic cell, a power source for energizing a pulsating current is provided between the electrode plates, and the frequency of the alternating component of the pulsating current is set in the electrolytic cell and an electrode plate incorporated therein. It is characterized in that it is set at or near the resonance frequency of the structure made of, for example.
【0005】また請求項2に係る水電解装置は、上記脈
流が、水の電解に要する電流値の直流電流に、上記共振
周波数あるいはその近傍の周波数の交流電流を重畳して
なるものであることを特徴とする。In the water electrolysis apparatus according to a second aspect of the present invention, the pulsating flow is formed by superimposing an alternating current having a resonance frequency or a frequency in the vicinity thereof on a direct current having a current value required for electrolysis of water. It is characterized by
【0006】さらに請求項3に係る水電解装置は、上記
電極板で上記電解槽内を遮断して区分し、かつ各電極板
に発生ガスの流路をなす通孔と、電解用水の循環路をな
す通孔とを設け、少なくとも上記発生ガス用の通孔を相
隣る電極板同士で対向しない位置に設けたことを特徴と
する。Further, in the water electrolysis apparatus according to a third aspect of the present invention, the electrode plate blocks the inside of the electrolytic cell to separate the electrode plate, and the electrode plate has a through hole which forms a flow path for the generated gas and a circulation path for electrolyzing water. And at least the through hole for the generated gas is provided at a position where adjacent electrode plates do not face each other.
【0007】[0007]
【発明の実施の形態】以下本発明の実施形態及び実施例
を図面を参照して説明する。図1は本発明に係る水電解
装置の一実施形態を示す断面図であり、密閉した電解槽
1内に多数枚の電極板2・・・とパッキン3・・・とを
交互に平行に支持してなり、電解槽1の一側には電解用
水の供給配管4と、発生ガス、即ち水素と酸素の混合ガ
スの送出配管5とを接続してある。電極板2には、電源
6を接続して電源供給を可能としてある。電解槽1内に
は、一般的には電解質として用いられる水酸化カリウム
等を混合したアルカリ溶液等を電解用水として供給配管
4を介して供給するが。もちろんその他の水や水溶液で
あってもよい。なお詳細な図示は省略するが、もちろん
電極板2と電解槽1の間は電気的に絶縁してあり、また
電解用水の給水用タンク等や排水用の配管等の周辺装置
も備える。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments and examples of the present invention will be described below with reference to the drawings. FIG. 1 is a sectional view showing an embodiment of a water electrolysis apparatus according to the present invention, in which a large number of electrode plates 2 ... And packings 3 ... In addition, a supply pipe 4 for electrolyzing water and a delivery pipe 5 for delivering a generated gas, that is, a mixed gas of hydrogen and oxygen are connected to one side of the electrolytic cell 1. A power supply 6 is connected to the electrode plate 2 to enable power supply. In the electrolytic cell 1, an alkaline solution or the like mixed with potassium hydroxide or the like which is generally used as an electrolyte is supplied as electrolyzing water through a supply pipe 4. Of course, other water or aqueous solution may be used. Although not shown in detail, of course, the electrode plate 2 and the electrolytic cell 1 are electrically insulated from each other, and peripheral devices such as a tank for supplying electrolytic water and a pipe for draining water are also provided.
【0008】電極板2は、図2に示すように発生ガスを
送出配管5へ導くための通孔(以下ガス孔)7と電解用
水を還流させるための通孔(以下水孔)8をそれぞれ一
対ずつ形成してあり、周縁の複数のボルト孔9に連結固
定用のボルトを通して多数枚が連結できるようになって
いる。電極板2にはステンレススチール等からなる板材
を用いるが、プラチナ箔を表面に貼付した鉄の薄板等そ
の他の素材のものも採用できる。パッキン3は、電極板
2の間に位置して相隣る電極板2、2間に分解室10を
形成するが、図示のように枠状部分の中央下側から上方
途中まで伸びる突部3aとを備えている。このため電極
板2とパッキン3とを組み合わせると、分解室10は突
部3aによって上部に僅かな隙間を残して2分され(以
下この2分された分解室を区分室10a、10bとい
う。)、ガス孔7、水孔8はそれぞれ1個ずつ区分室1
0a、10bに臨む状態となる。またパッキン3は、電
極板2のボルト孔9と対応する位置に同じくボルト孔9
aを形成してある。As shown in FIG. 2, the electrode plate 2 has a through hole (hereinafter referred to as a gas hole) 7 for guiding the generated gas to the delivery pipe 5 and a through hole (hereinafter referred to as a water hole) 8 for refluxing electrolyzing water. Each pair is formed so that a large number of bolts can be connected through a plurality of bolt holes 9 on the periphery through connecting and fixing bolts. A plate material made of stainless steel or the like is used for the electrode plate 2, but other materials such as a thin iron plate having a platinum foil adhered to the surface can also be used. The packing 3 forms a decomposition chamber 10 between the electrode plates 2 and 2 which are located between the electrode plates 2 and are adjacent to each other, but as shown in the figure, a protrusion 3a extending from the lower center of the frame-shaped portion to an upper middle thereof. It has and. Therefore, when the electrode plate 2 and the packing 3 are combined, the decomposition chamber 10 is divided into two parts by the projection 3a leaving a slight gap in the upper part (hereinafter, these divided decomposition parts are referred to as division chambers 10a and 10b). , 1 gas hole 7 and 1 water hole 8
0a and 10b are reached. In addition, the packing 3 has bolt holes 9 at the positions corresponding to the bolt holes 9 of the electrode plate 2.
a is formed.
【0009】このような電極板2とパッキン3とを組み
合わせるにあたっては、図3に示すように、電極板2は
1枚ごとに図中の左右を反転させる。すると、ガス孔
7、水孔8はそれぞれ相隣る電極版2のガス孔7、水孔
8と図中の左右の反対側に位置する。これによって、図
4に示すように、発生ガスと電解用水がそれぞれ一の区
分室10a、10b内で曲折する経路、いわゆるカスケ
ード状の経路を取り得るようになる。When assembling the electrode plate 2 and the packing 3 as described above, as shown in FIG. 3, the electrode plates 2 are reversed one by one in the figure. Then, the gas holes 7 and the water holes 8 are located on the opposite sides of the gas holes 7 and the water holes 8 of the electrode plates 2 adjacent to each other on the left and right sides in the figure. As a result, as shown in FIG. 4, the generated gas and the electrolyzed water can take a bent path in each of the compartments 10a and 10b, that is, a so-called cascade path.
【0010】電源6は水や電解質水溶液を電気分解させ
るのに必要な電圧の直流に交流を重畳して脈流とした電
流を供給するものである。供給する脈流は、単に直流に
交流を重畳したものだけでなく、オフセットをかけた矩
形波や三角波、正弦波等種々採用できるが、その交流成
分の周波数は、電解槽1や電極板2、パッキン3等から
なる構造体の共振周波数あるいはその近傍の値とする。
本発明者等の行った実験では、このようにすると分解効
率が非常に効率化することが確かめられた。なお、電源
6の具体的な回路構成は、供給しようとする脈流に応じ
て種々公知の回路を採用すればよいので、詳細な図示及
び説明は省略する。The power source 6 supplies a pulsating current by superimposing an alternating current on a direct current having a voltage necessary for electrolyzing water or an aqueous electrolyte solution. The pulsating current to be supplied is not limited to one in which direct current is superimposed on alternating current, and various types such as offset rectangular waves, triangular waves, and sine waves can be adopted, but the frequency of the alternating current component is the electrolytic cell 1, the electrode plate 2, It is set to a value at or near the resonance frequency of the structure composed of the packing 3 and the like.
In the experiments conducted by the present inventors, it was confirmed that the decomposition efficiency was remarkably improved by doing so. It should be noted that various known circuits may be adopted as the specific circuit configuration of the power supply 6 depending on the pulsating current to be supplied, and thus detailed illustration and description thereof will be omitted.
【0011】図示は省略するが、発生ガスによって電解
槽1内の圧力が一定以上になったことを検出したときに
電解抑制信号を送出する圧力制御器を設けたり、内部に
不撚性の液体を貯留し、その上部にガス滞留部を設けた
燃焼防止槽を介して発生ガスの送出配管5を連結したり
することができる。Although not shown in the drawings, a pressure controller for sending an electrolysis suppressing signal when detecting that the pressure in the electrolytic cell 1 exceeds a certain level due to the generated gas is provided, or a non-twisting liquid is provided inside. Can be stored, and the generated gas delivery pipe 5 can be connected via a combustion prevention tank having a gas retention portion provided above it.
【0012】次に上述の装置によって水電解を行なう際
の動作について説明するが、水電解を行なうにあたって
は図5に示すように電解槽1を若干傾け、ガス孔7の周
囲が広く空くようにする。電源6より電源供給すると、
各区分室10a、10b内で電解用水が電気分解され、
これにより陽極側に酸素が、陰極側に水素が発生する。
この発生ガス、即ち水素と酸素の混合ガスは、送出配管
5から供給されるが、このとき発生ガスは図4に示すよ
うに曲折した経路を取り、送出配管5への排出が抵抗と
なって出口となる端部の区分室10b側へ向かうに連れ
て室内圧が高まるとともに、この室内圧が分解室10内
の電解用水の液面に掛かり、電解用水が水孔8を通じて
分解室10内を循環する。この動作によって分解効率が
高められる。Next, the operation when water electrolysis is carried out by the above-mentioned apparatus will be described. When carrying out water electrolysis, the electrolyzer 1 is slightly tilted as shown in FIG. 5 so that the circumference of the gas hole 7 is wide. To do. When power is supplied from the power supply 6,
Electrolyzed water is electrolyzed in each compartment 10a, 10b,
As a result, oxygen is generated on the anode side and hydrogen is generated on the cathode side.
This generated gas, that is, a mixed gas of hydrogen and oxygen is supplied from the delivery pipe 5. At this time, the generated gas takes a curved path as shown in FIG. 4, and the discharge to the delivery pipe 5 becomes a resistance. The room pressure increases as it goes to the side of the division chamber 10b at the end that serves as the outlet, and this room pressure is applied to the liquid surface of the electrolysis water in the decomposition chamber 10, so that the electrolysis water flows through the water holes 8 in the decomposition chamber 10 inside. Circulate. This operation enhances the disassembly efficiency.
【0013】[0013]
【実施例】次に本発明の実施例を説明する。以下のよう
な諸元で本発明に係る水電解装置を構成したところ、7
〜8リットル/毎分のガス生成能力を得られた。 分解室容量 1.8リットル 分解室数 76室 電極板寸法 高さ142mm、幅231mm 電極板枚数 77枚(ステンレススチール製) 電極板間隔 2mm 電解用水 水酸化カリウム混合水溶液 電解用水濃度 20% 印加直流 170V、12A 印加交流 11〜13KHz(波形については図
6参照)、8〜9V 装置共振周波数 約12KHz 比較のため、交流を印加しない以外は上記と同条件で水
電解を行なったところ、4リットル/毎分程度のガス生
成能力しか得られなかった。Next, embodiments of the present invention will be described. When the water electrolysis apparatus according to the present invention is constructed with the following specifications, 7
A gas generation capacity of ~ 8 liters / minute was obtained. Decomposition chamber capacity 1.8 liters Decomposition chamber number 76 chambers Electrode plate height 142 mm, width 231 mm Number of electrode plates 77 (stainless steel) Electrode plate spacing 2 mm Electrolysis water / potassium hydroxide mixed solution electrolysis water concentration 20% Applied DC 170V , 12 A AC applied 11 to 13 KHz (see FIG. 6 for waveform), 8 to 9 V, device resonance frequency of about 12 KHz For comparison, water electrolysis was performed under the same conditions as above except that no AC was applied. Only a gas generation capacity of about a minute was obtained.
【0014】[0014]
【発明の効果】本発明に係る水電解装置は以上説明して
きたように、小型で非常に高効率で水電解を行なって大
量の酸、水素混合ガスを生成させることができるように
なるという効果がある。As described above, the water electrolysis apparatus according to the present invention is small in size and can produce a large amount of acid-hydrogen mixed gas by performing water electrolysis with extremely high efficiency. There is.
【図1】本発明に係る水電解装置の一実施形態を示す断
面図である。FIG. 1 is a sectional view showing an embodiment of a water electrolysis device according to the present invention.
【図2】電極板とパッキンの平面形状を示す正面図であ
る。FIG. 2 is a front view showing a planar shape of an electrode plate and a packing.
【図3】電極板とパッキンの組み合わせ状態を示す斜視
図である。FIG. 3 is a perspective view showing a combined state of an electrode plate and a packing.
【図4】電解槽内での発生ガスと電解用水の流れる経路
を示す図である。FIG. 4 is a diagram showing a flow path of generated gas and electrolysis water in an electrolytic cell.
【図5】ガスを発生させるときの電解槽の使用状態を示
す断面図である。FIG. 5 is a cross-sectional view showing a use state of the electrolytic cell when generating gas.
【図6】電源から印加する交流の波形図である。FIG. 6 is a waveform diagram of alternating current applied from a power source.
1 電解槽 2 電極板 3 パッキン 4 電解用水の供給配管 5 発生ガスの送出配管 6 電源 7 ガス孔 8 水孔 9、9a ボルト孔 3a パッキンの突部 10 分解室 10a、10b 区分室 DESCRIPTION OF SYMBOLS 1 Electrolyzer 2 Electrode plate 3 Packing 4 Supply pipe for electrolyzing water 5 Delivery pipe for generated gas 6 Power supply 7 Gas hole 8 Water hole 9, 9a Bolt hole 3a Packing protrusion 10 Decomposition chamber 10a, 10b Division chamber
Claims (3)
並設し、これら電極板間に電解電流を流して酸素ガス及
び水素ガスを発生させ、発生ガスを上記電解槽外へ供給
可能とした水電解装置において、上記電極板間に脈流を
通電する電源を備えるとともに、該脈流の交流成分の周
波数を、上記電解槽及び内蔵する電極板等からなる構造
体の共振周波数あるいはその近傍としたことを特徴とす
る水電解装置。1. A large number of electrode plates are arranged in parallel in electrolyzed water in an electrolyzer, and an electrolysis current is passed between the electrode plates to generate oxygen gas and hydrogen gas, and the generated gas is supplied to the outside of the electrolyzer. In the possible water electrolysis device, a power source for supplying a pulsating current between the electrode plates is provided, and the frequency of the alternating current component of the pulsating current is set to the resonance frequency of a structure composed of the electrolytic cell and an electrode plate incorporated therein, or the like. A water electrolysis device characterized by being in the vicinity thereof.
直流電流に、上記共振周波数あるいはその近傍の周波数
の交流電流を重畳してなるものであることを特徴とする
請求項1の水電解装置。2. The pulsating flow is formed by superposing an alternating current having a frequency at or near the resonance frequency on a direct current having a current value required for electrolysis of water. Water electrolysis device.
分し、かつ各電極板に発生ガスの流路をなす通孔と、電
解用水の循環路をなす通孔とを設け、少なくとも上記発
生ガス用の通孔を相隣る電極板同士で対向しない位置に
設けたことを特徴とする請求項1または2の水電解装
置。3. The electrode plate is divided into sections by blocking the inside of the electrolytic cell, and each electrode plate is provided with a through hole which forms a flow path of generated gas and a through hole which forms a circulation path of electrolysis water, 3. The water electrolysis apparatus according to claim 1, wherein the through holes for the generated gas are provided at positions where adjacent electrode plates do not face each other.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7248619A JPH0971886A (en) | 1995-09-01 | 1995-09-01 | Water electrolysis device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7248619A JPH0971886A (en) | 1995-09-01 | 1995-09-01 | Water electrolysis device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0971886A true JPH0971886A (en) | 1997-03-18 |
Family
ID=17180813
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7248619A Pending JPH0971886A (en) | 1995-09-01 | 1995-09-01 | Water electrolysis device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0971886A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000000670A1 (en) * | 1998-06-26 | 2000-01-06 | Xogen Power Inc. | Apparatus for producing orthohydrogen and/or parahydrogen |
| WO2004031450A1 (en) * | 2002-09-30 | 2004-04-15 | Honda Giken Kogyo Kabushiki Kaisha | Hydrogen activating apparatus |
| JP2009074162A (en) * | 2007-09-18 | 2009-04-09 | Samsung Electro-Mechanics Co Ltd | Reactor cover, hydrogen generating apparatus with the same, and fuel cell power generation system |
| US7837882B2 (en) * | 2002-11-19 | 2010-11-23 | Xogen Technologies Inc. | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| JP2012515845A (en) * | 2009-01-20 | 2012-07-12 | パルミル | Electrolysis method, apparatus and system |
| RU2506349C2 (en) * | 2013-01-21 | 2014-02-10 | Геннадий Леонидович Багич | Method of determination of maximum water decomposition and device to this end (versions) |
| US9187347B2 (en) | 2002-11-19 | 2015-11-17 | Xogen Technologies Inc. | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| US9296629B2 (en) | 2002-11-19 | 2016-03-29 | Xogen Technologies Inc. | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| DE102018203604A1 (en) * | 2018-03-09 | 2019-09-12 | Peter Schulz | Electrolysis apparatus and method |
-
1995
- 1995-09-01 JP JP7248619A patent/JPH0971886A/en active Pending
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6790324B2 (en) | 1998-06-26 | 2004-09-14 | Xogen Power Inc. | Hydrogen producing apparatus |
| US6126794A (en) * | 1998-06-26 | 2000-10-03 | Xogen Power Inc. | Apparatus for producing orthohydrogen and/or parahydrogen |
| JP2002519513A (en) * | 1998-06-26 | 2002-07-02 | エクサジャン パワー インコーポレイテッド | Ortho hydrogen and / or para hydrogen production equipment |
| US6419815B1 (en) | 1998-06-26 | 2002-07-16 | Xogen Power Inc. | Method for producing orthohydrogen and/or parahydrogen |
| WO2000000670A1 (en) * | 1998-06-26 | 2000-01-06 | Xogen Power Inc. | Apparatus for producing orthohydrogen and/or parahydrogen |
| US7410557B2 (en) | 2002-09-30 | 2008-08-12 | Honda Motor Co., Ltd. | Hydrogen activating apparatus |
| WO2004031450A1 (en) * | 2002-09-30 | 2004-04-15 | Honda Giken Kogyo Kabushiki Kaisha | Hydrogen activating apparatus |
| US7837882B2 (en) * | 2002-11-19 | 2010-11-23 | Xogen Technologies Inc. | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| US9187347B2 (en) | 2002-11-19 | 2015-11-17 | Xogen Technologies Inc. | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| US9296629B2 (en) | 2002-11-19 | 2016-03-29 | Xogen Technologies Inc. | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| JP2009074162A (en) * | 2007-09-18 | 2009-04-09 | Samsung Electro-Mechanics Co Ltd | Reactor cover, hydrogen generating apparatus with the same, and fuel cell power generation system |
| JP2012515845A (en) * | 2009-01-20 | 2012-07-12 | パルミル | Electrolysis method, apparatus and system |
| RU2506349C2 (en) * | 2013-01-21 | 2014-02-10 | Геннадий Леонидович Багич | Method of determination of maximum water decomposition and device to this end (versions) |
| DE102018203604A1 (en) * | 2018-03-09 | 2019-09-12 | Peter Schulz | Electrolysis apparatus and method |
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