201207155 六、發明說明： 【發明所屬之技術領域】 本發明係為一種製造氫氧氣的電解裝置，涉及一種電解 製造氫氧氣的裝置，尤指能提高氫氧氣產製效能的電解裝置。 【先前技術】 氫氧燃料產生裝置係藉由電解方式將電解槽内之電解液 • 電解產生氫、氧氣，將氫、氧氣混合輸送到油氣混合室，與可 - 燃性液體（如：烷類、醇類、酒精、汽油）的揮發氣混合，並 - 輸出做為燃料使用。 電解槽的工作效率關係著氫氧燃料的可運用效益。若 100KL的電能只能產生30KL的熱能，工作效益僅達3〇%，會使 氫氧氣燃料的成本提高，不符合經濟效益。目前所使用的電解 槽内的各組電解極板之間採並聯設置，為高電壓、高電流型 • 態，使用上較料發生危險。按電流有她抗較小的路徑流動 的原理’ 4成各組電解極板之間的工作效益也會有明顯差異， 厫重影響電解槽的工作效率。產量低、危險性高，是氮氧燃料 不易被廣用的主要原因之一。 【發明内容】 本發明的主要目的，在提供一種製造氫氧氣的電解裝 置，其能使產生氫氧氣紅作效率提高，使氫氧轉的生產成 201207155 本降低。 本發明的主要目的，在提供一種製造氫氧氣的電解裝 置’其電解卫作係在低賴、低電流的條件下進行，安全性高 為達上述目的，本發明的電解裝置包含設置有一電解 槽，前述電解槽内設置有至少二個各自獨立作業的電解室，以 及一氫氧氣輸出口。所述電解室内填充適量電解液及設置有 一電解極板組。所述各電解室的各電解極板組為串聯電路型態 • 5又置。所述電解極板組包含設置有至少一個的陽極板與至少二 _ 個的陰極板。該電解極板組内的各陽極板與各陰極板係以並聯 - 電路型態設置。任相鄰二陰極板之間的間隙插設一陽極板，且 各陰極板的設置所產生的間隙數量等於陽極板的數量。 本發明的電解裝置中’所述陽極板與陰極板上設有多數 個可供氣體分子與電解液分子穿過的小孔。 本發明的電解裝置中’所述電解極板組中的相鄰的陽極 鲁 板與陰極板之間的間隙在0. 6〜1. Omm之間。 本發明的電解裝置可更包含一電解液補充桶，其内儲放 適量的電解液’並至少二個輸出管路。所述各輸出管路與電解 槽的各電解室以一對一型態連通，能夠將電解液補充桶内的電 解液自動輸送到電解室内。所述電解液補充桶包含設置一與電 解槽的氫氧氣輸出口連通的氫氧氣輸入口。藉由氫氧氣送入電 解液補充桶内對電解液所產生的推力，而使電解液補充桶内電 解液與電解槽内的電解液產生對流。 201207155 【實施方式】 申請人有鑑於目前電解裝置產製氤、氧氣的效益過低， 且裝置運作時有電壓、電流偏高的問題，而研創一種製造氣氣 氣的電解裝置，其氫、氧氣產量高，可提高氫氧燃料的使用致 益；其工作電壓低，電流強度穩定且低，安全性高。茲列舉實 施例，並配合圖式，詳述本發明的構造特徵與功效。 請參閱圖一、圖二、圖三。本發明所揭露的製造氫氧氣 的電解裝置，其包含設置有一電解槽10，該電解槽1〇内設置 有至少二個各自獨立的電解室11，以及一氫氧氣輸出口 12。 本實施例中，該電解槽10内設置有六個各自獨立作業的電解 室11。各電解室11内填充適量電解液2〇，以及各設置有一電 解極板組30。所述各電解室11的各電解極板組3〇之間為串 聯電路型態設置（見圖七）。該各電解極板組30之間的串聯係 藉由導電片33所連接。該電解槽1〇設置有一正極輸入端13 及一負極輸入端14，可與電源裝置（見圖七）連接，以將電 源輸送入電解槽10内供各電解極板組3〇進行電解工作。電解 所得到的氫氧氣可由該氫氧氣輸出口 12送出。 請參閱圖四、圖五、圖六。前述電解極板組3〇包含設置 有至少一個的陽極板31與至少二個的陰極板32。該電解極板 組30内的各陽極板31與各陰極板32之間係以並聯電路型態 設置。本實施例中，該電解極板組30包含設置有二個的陽極 201207155 板31與三個的陰極板32。其間，任相鄰二陰極板32之間的 間隙插設-1%極板3卜且各陰極板32的設置所產生的間隙數 量等於陽極板31龍4。本實關的三個陰極％板可構成二 個間隙’該二個陽極板31係、插置在該二個間隙内。當輸入電 流進行電解功時，陰難上會產生域，雜板會產生氧 氣。由於陰極板32的數量較陽極板31的數量多一個，即會多 增加一對陰陽極進行電解，相較於陰極板32與陽極板31數量 相等的情形，可提高約30%的氫、氧氣產量。該陽極板32與 陰極板31之間係設置絕緣塾34阻隔。 雖然電解工作的電流強度過高，容易發生危險。但電流 強度越大電解作用也越佳。在工作電壓固定時，電流阻抗的大 小即決定電流的強度。電解工作中，電解液2〇就是阻抗。陰 極板32與陽極板31之間的距離越大，在二者之間的電解液 20的阻抗越大，反之則越小。前述電解極板組3〇中相鄰的陽 極板31與陰極板32之間的間隙係在〇·6〜l.〇mm之間。本實 施例中’電解極板組30中相鄰的陽極板31與陰極板32之間 的間隙為0. 8mm。 前述陰極板32與陽極板31之間的距離較小，會造成二 者之間的電解液20不易流動，嚴重影響電解效益。又，陰極 板32與陽極板31之間的距離過小，也會影響氫、氧氣向上流 動的速度，降低電解效益。為解決此問題，前述陽極板31與 陰極板32上設有多數個可供氣體分子與電解液分子穿過的小 201207155 孔311、321，使陽極板31與陰極板32之間的電解液2〇會與 電解極板組30外的電解液20進行對流，且氣、氧氣也可由小 孔311、321穿出後向上溢出液面’以相對提高電解效益。 前述_板31與陰極板32可為奈米電極板。亦即，在 陽極板3卜陰極板32的表面鍍有奈米陶磁塗層，而形成奈米 電極板。該奈米陶磁塗層係具有孔隙，足供電子水分子、氫 氧氣體分子穿過。該具有表面塗層的陽極板31、陰極板犯可 為欽板。 配合圖七。本實施斯連接的電賴置4()的輸出電壓可 為12 V (伏特），則電解槽1〇内每一電解極板組3〇的工作電 壓為2 V (伏特），為低電壓。電壓與電流強度成正比，所以 電解極板組30係在低電流狀態下進行電解工作。本發明裝置 在低電壓、低電流狀態下工作，安全性高。 兩述製造氫氧氣的電解裝置可更包含設置一電解液補充 桶50 ’見圖八。該電解液補充桶5〇内儲放適量的電解液W， 而能適時將電解液51輸送到電解槽1〇的各電解室U内。該 電解液補絲50設置註少二個輸㈣路52，該各輸出管路 52與電解槽的各電解室11以一對一型態連通，而能夠將電解 液補充桶50内的電解液51自動輸送到電解室j j内。 知：述電解液補充桶50 &含設置-氫氧氣輸入口 53,及-氫氧氣輸出口 54。賴氧氣輸人口 53的設置高度*高於電解 液輪出管路52的高度，且與電解槽1〇的氫氧氣輸出口 12間 201207155 以S路55連接。該氫氧氣輸出口 54設置在電解液補充桶训 的頂端。電解槽10所輸出的氫、氧氣經由管路55送入電解液 補充桶50内，再由電解液補充桶5〇頂端的氣氧氣輸入口 ^ 送出。氫、氧氣進入電解液補充桶5〇内時，所產生的氣泡會 對電解液51產生推擠力，而將電解液51強行推送到電解室 11内’使電解室11⑽液Φ瞬間略為高於電解賴充桶 内的液面；又因為壓力平衡關係，電解室12内的電解液2〇又 • 會回流到電解液補充桶50内，使得電解室11的電解液20形 成活水狀態，而更能提高電解的效益，增加氣、氧氣產量 ' 树_電職置提高統氣產量的方式包含有： 1. 在每-電解極板組30中以增設一片陰極板32的方式，提高 虱、氧氣產量。 2. 縮小相鄰陽極板31與陰極板％的距離，崎低阻抗，提高 電流強度。 » 3·在陽極板31與陰極板32上設有多數個可供氣體分子與電解 液分子穿過的小孔311、321，使電解液可對流，且增加氣 氧氣的排出方向。 4·藉由氫氧氣推動電解液補充桶5〇内的電解液5】，而使電解 至Π與電解液補充桶5〇間產生對流使電解室】】内的電 解液20呈活水的狀態。 本發明裝置除了能增加氫氧氣的產量，更能在低電屢、 低電流的作業條件下進行電解，安全性高。本發明裝置的氩氧 201207155 氣產里付合經濟政益’足供產業上利用，為一理想而又實用的 的創新設計。 【圖式簡單說明】 圖一為本發明實施例的外觀圖。 圖二為圖一所示實施例的内部結構圖。 圖二為圖二的3 — 3剖面圖。 圖四為電解極板組的外觀圖。 圖五為電解極板組的分解圖。 圖六為三組相互連接的電解極板組的外觀圖 圖七為本發明與電源裝置連接後的電路示意圖。 圖八為圖-所示實麵連接t驗補充_外觀圖。 【主要元件符號說明】 10.· …·電解槽 12·. …·氫氧氣輪出 14.· 負極輪入端 20.· …·電解液 30·. …·電解極板組 311. .....小孔 321· 34··· …絕緣勢片 40... 11......電解室 13......正極輸入端 31…···陽極板 32 ......陰極板 33 ......導電片 201207155 50… …電解液補充桶 51··· …電解液 52… …輸出管路 53… …氫氧氣輸入 54… …氫氧氣輸出口 55… …管路201207155 VI. Description of the Invention: [Technical Field] The present invention relates to an electrolysis device for producing hydrogen and oxygen, and relates to a device for electrolytically producing hydrogen and oxygen, and more particularly to an electrolysis device capable of improving hydrogen and oxygen production efficiency. [Prior Art] The oxyhydrogen fuel generating device electrolyzes the electrolyte in the electrolytic cell to produce hydrogen and oxygen, and mixes hydrogen and oxygen into the oil and gas mixing chamber, and combustible liquid (such as alkanes). The volatile gases of alcohol, alcohol, and gasoline are mixed, and the output is used as fuel. The efficiency of the electrolysis cell is related to the operational benefits of the oxyhydrogen fuel. If 100KL of electric energy can only generate 30KL of heat energy, the working efficiency is only 3〇%, which will increase the cost of hydrogen and oxygen fuel, which is not economical. At present, each group of electrolytic plates in the electrolytic cell used is arranged in parallel, which is a high-voltage, high-current type, and is dangerous when used. According to the current, there is a principle that she resists the flow of smaller paths. 4 The working benefits between the groups of electrolytic plates will also be significantly different, and the weight will affect the working efficiency of the electrolytic cell. Low yield and high risk are one of the main reasons why nitrogen-oxygen fuels are not widely used. SUMMARY OF THE INVENTION A primary object of the present invention is to provide an electrolysis apparatus for producing hydrogen and oxygen, which can increase the efficiency of hydrogen and oxygen generation, and reduce the production of hydrogen-oxygen conversion to 201207155. The main object of the present invention is to provide an electrolysis device for producing hydrogen and oxygen. The electrolysis device is operated under low and low current conditions, and the safety is high. The electrolysis device of the present invention comprises an electrolysis cell. The electrolysis cell is provided with at least two electrolysis chambers which are independently operated, and a hydrogen-oxygen output port. The electrolysis chamber is filled with an appropriate amount of electrolyte and an electrolytic plate group is disposed. Each of the electrolytic plate sets of the respective electrolysis chambers is in a series circuit type. The electrolytic plate group includes at least one anode plate and at least two cathode plates. Each of the anode plates and the cathode plates in the electrolytic plate group are arranged in a parallel-circuit type. An anode plate is interposed between the gaps between adjacent two cathode plates, and the number of gaps generated by the arrangement of each cathode plate is equal to the number of anode plates. In the electrolysis device of the present invention, the anode plate and the cathode plate are provided with a plurality of small holes through which gas molecules and electrolyte molecules can pass. Omm之间。 The gap between the 0. 6~1. Omm between the two. The electrolysis apparatus of the present invention may further comprise an electrolyte replenishing tank in which an appropriate amount of electrolyte 'and at least two output lines are stored. Each of the output lines communicates with each of the electrolysis chambers of the electrolytic cell in a one-to-one configuration, and the electrolyte solution in the electrolyte replenishing tank can be automatically transferred to the electrolysis chamber. The electrolyte replenishing tank includes a hydrogen oxygen input port that is connected to a hydrogen oxygen output port of the electrolysis tank. The hydrogen and oxygen are fed into the electrolyte to replenish the thrust generated by the electrolyte in the barrel, so that the electrolyte in the electrolyte replenishing tank is convected with the electrolyte in the electrolytic cell. 201207155 [Embodiment] In view of the fact that the current electrolysis device produces bismuth and oxygen, the efficiency of oxygen is too low, and the voltage and current are high when the device is operating, and an electrolytic device for producing gas and gas, hydrogen and oxygen. High output can improve the use of hydrogen-oxygen fuel; its working voltage is low, current intensity is stable and low, and safety is high. The construction features and effects of the present invention are detailed by way of examples and in conjunction with the drawings. Please refer to Figure 1, Figure 2 and Figure 3. The electrolysis apparatus for producing hydrogen and oxygen disclosed in the present invention comprises an electrolytic cell 10 provided with at least two independent electrolysis chambers 11 and a hydrogen-oxygen output port 12 therein. In the present embodiment, six electrolytic cells 11 each independently operated are disposed in the electrolytic cell 10. Each of the electrolytic chambers 11 is filled with an appropriate amount of electrolyte 2, and an electrolytic plate group 30 is provided for each. The respective electrolytic plate groups 3 of each of the electrolysis chambers 11 are arranged in a series circuit type (see Fig. 7). The string connection between the respective electrolytic plate groups 30 is connected by the conductive sheets 33. The electrolytic cell 1 is provided with a positive input terminal 13 and a negative input terminal 14, which can be connected to a power supply device (see FIG. 7) to supply power into the electrolytic cell 10 for electrolysis of each electrolytic plate group 3〇. Hydrogen oxygen obtained by electrolysis can be sent out from the hydrogen oxygen outlet 12. Please refer to Figure 4, Figure 5 and Figure 6. The foregoing electro-electrode plate group 3A includes at least one anode plate 31 and at least two cathode plates 32. The anode plates 31 and the cathode plates 32 in the electrolytic plate group 30 are arranged in a parallel circuit type. In the present embodiment, the electrolytic plate group 30 includes two anodes 201207155 plates 31 and three cathode plates 32. In the meantime, the gap between the adjacent two cathode plates 32 is interposed with -1% of the plates 3 and the number of gaps generated by the arrangement of the cathode plates 32 is equal to that of the anode plate 31. The three cathode % plates of the present embodiment can form two gaps. The two anode plates 31 are interposed in the two gaps. When the input current is used for electrolysis work, a field is generated on the yin and the board generates oxygen. Since the number of the cathode plates 32 is one more than the number of the anode plates 31, a pair of anodes and cathodes are added to perform electrolysis. Compared with the case where the number of the cathode plates 32 and the anode plates 31 are equal, about 30% of hydrogen and oxygen can be increased. Yield. An insulating barrier 34 is disposed between the anode plate 32 and the cathode plate 31. Although the current intensity of the electrolysis work is too high, it is prone to danger. However, the greater the current intensity, the better the electrolysis. When the operating voltage is fixed, the magnitude of the current impedance determines the strength of the current. In the electrolysis work, the electrolyte 2 is the impedance. The greater the distance between the cathode plate 32 and the anode plate 31, the greater the impedance of the electrolyte 20 between the two, and vice versa. The gap between the adjacent anode plates 31 and the cathode plates 32 in the above-mentioned electrolytic plate group 3 is between 〇·6 and 1.0 mm. 8毫米。 The gap between the adjacent anode plate 31 and the cathode plate 32 is 0. 8mm. The distance between the cathode plate 32 and the anode plate 31 is small, which causes the electrolyte 20 between the two to flow less, which seriously affects the electrolysis efficiency. Further, the distance between the cathode plate 32 and the anode plate 31 is too small, which also affects the speed at which hydrogen and oxygen flow upward, and reduces the electrolysis efficiency. In order to solve this problem, the anode plate 31 and the cathode plate 32 are provided with a plurality of small 201207155 holes 311 and 321 through which gas molecules and electrolyte molecules pass, so that the electrolyte 2 between the anode plate 31 and the cathode plate 32 is provided. The enthalpy will convect with the electrolyte 20 outside the electrolytic plate group 30, and the gas and oxygen may also pass through the small holes 311 and 321 and then overflow upward to the liquid surface to relatively improve the electrolysis efficiency. The aforementioned plate 31 and cathode plate 32 may be nanoelectrode plates. Namely, a surface of the anode plate 3 and the cathode plate 32 is plated with a nano ceramic coating to form a nanoelectrode plate. The nano-ceramic magnetic coating has pores for electron water molecules and hydrogen-oxygen gas molecules to pass through. The anode plate 31 and the cathode plate having the surface coating can be used as a plate. Match Figure VII. The output voltage of the current connection 4() of the present embodiment can be 12 V (volts), and the operating voltage of each of the electrolytic plate groups 3 in the electrolytic cell 1 is 2 V (volts), which is a low voltage. Since the voltage is proportional to the current intensity, the electrolytic plate group 30 is subjected to electrolysis in a low current state. The device of the invention operates under low voltage and low current conditions and has high safety. The two electrolyzers for producing hydrogen and oxygen may further comprise an electrolyte replenishing tank 50' as shown in Fig. 8. An appropriate amount of the electrolytic solution W is stored in the electrolytic solution replenishing tank 5, and the electrolytic solution 51 can be timely supplied to the respective electrolytic chambers U of the electrolytic cell 1〇. The electrolyte supply wire 50 is provided with two injection (four) channels 52, and the respective output lines 52 communicate with the respective electrolysis chambers 11 of the electrolysis tank in a one-to-one type, and the electrolyte can be replenished in the electrolyte in the barrel 50. 51 is automatically delivered into the electrolysis chamber jj. It is understood that the electrolyte replenishing tank 50 & includes a set-hydrogen oxygen input port 53, and a hydrogen-oxygen output port 54. The set height of the oxygen-containing population 53 is higher than the height of the electrolyzer wheel outlet line 52, and is connected to the hydrogen-oxygen outlet port 12 of the electrolyzer 1〇 201207155 by the S-way 55. The hydrogen-oxygen output port 54 is disposed at the top of the electrolyte replenishing barrel. The hydrogen and oxygen output from the electrolytic cell 10 are sent to the electrolyte replenishing tank 50 via the line 55, and are sent out by the gas oxygen inlet port ^ at the top of the electrolyte replenishing tank 5. When hydrogen and oxygen enter the electrolyte replenishing tank 5, the generated bubbles will push the electrolyte 51, and the electrolyte 51 is forcibly pushed into the electrolysis chamber 11 to make the electrolysis chamber 11 (10) liquid Φ slightly higher than the moment. The electrolyte is in the liquid level in the filling tank; and because of the pressure balance relationship, the electrolyte 2 in the electrolytic chamber 12 is again returned to the electrolyte replenishing tank 50, so that the electrolyte 20 of the electrolysis chamber 11 forms a living water state, and It can improve the efficiency of electrolysis and increase the production of gas and oxygen. The way of increasing the output of the gas is as follows: 1. In each electro-electrode plate group 30, a cathode plate 32 is added to increase the enthalpy and oxygen. Yield. 2. Reduce the distance between the adjacent anode plate 31 and the cathode plate, and lower the impedance to increase the current intensity. » 3. On the anode plate 31 and the cathode plate 32, a plurality of small holes 311 and 321 through which gas molecules and electrolyte molecules pass are provided, so that the electrolyte can convect and increase the discharge direction of the gas and oxygen. 4. The electrolyte is replenished by the hydrogen and oxygen to replenish the electrolyte 5 in the barrel 5, and the electrolysis is caused to cause convection between the crucible and the electrolyte replenishing tank 5, so that the electrolyte 20 in the electrolysis chamber is in a state of living water. In addition to increasing the production of hydrogen and oxygen, the device of the present invention can perform electrolysis under low-current and low-current operating conditions, and has high safety. The argon oxygen 201207155 of the device of the invention is sufficient for the industrial use, and is an ideal and practical innovative design. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an external view of an embodiment of the present invention. Figure 2 is an internal structural view of the embodiment shown in Figure 1. Figure 2 is a 3 - 3 cross-sectional view of Figure 2. Figure 4 is an external view of the electrolytic plate group. Figure 5 is an exploded view of the electrolytic plate set. Figure 6 is an external view of three sets of interconnected electrolytic plate sets. Figure 7 is a schematic view of the circuit after the invention is connected to the power supply unit. Figure 8 is a diagram of the solid-surface connection t-review _ appearance. [Explanation of main component symbols] 10.· ...· Electrolytic cell 12·. ...· Hydrogen oxygen wheel out 14.· Negative wheel wheel end 20.·...·Electrolyte 30·.··Electrode plate group 311. ... .. small hole 321 · 34 · · · ... insulating potential sheet 40 ... 11 ... electrolytic chamber 13 ... positive input terminal 31 ... · · · anode plate 32 ..... Cathode plate 33 ... Conductive sheet 201207155 50... Electrolyte refill tank 51 · · · Electrolyte 52 ... Output line 53 ... Hydrogen oxygen input 54 ... Hydrogen oxygen output port 55 ... Tube road