M360246 八、新型說明： 【新型所屬之技術領域】 本創作係有關一種具有結合式與複合式電極導電材料 之電解氣體容器，尤指一種將氣體電解出之裝置。 【先前技術】 按，所謂電解是使電流通過離子傳導體（如電解質溶 液或溶解電解質等）而產生化學變化之意，即在加上電能 * $ '之後會出現自由能量增加反應，在離子傳導體中插入一對 電極，兩端連接適當的電源，電流在離子傳導體内部藉著 離子的移動而傳送。在電極與溶液的介面，由於電極反應 進行而有電荷移動，陽極面進行金屬的溶解、產生氧等氧 化反應（陽極氧化），陰極面則進行金屬的析出、產生氫等 還原反應（陰極還原），此即為電解氣體容器之電解原理。 如第1 0圖所示，為習用之電解氣體容器，其於一瓶 φ 體9 0中設有數電極部9 1，電極部9 1並於瓶體9 0側 . 邊電性連接直流電源9 2，各電極部9 1係呈板狀，且具 有外凸之結構，俾供將水中之氫氣與氧氣電解出以供外部 使用。 然而，習用之電解氣體容器通常體積大，於電解時所 需電流量可達2 0〜3 0安培，因此必須耗費相當高之電 量，始能電解出適量之氫氣，而且電解時通常必須加入催 化劑，一般是使用氫氧化鈉，而此催化劑遇水後會產生高 M360246 溫，故於電解過程會有造成瓶體炸開的危險。 此外，習用之電解部係於一種導電或不導電材料上電 鍍一電鍍層，電鍍層於電解電極久後，披附在電極材料表 面上之電鍍層，由於受強酸或強鹼侵蝕而產生變化，意即， 電極因電解液侵蝕電鍍層，而使阻抗產生變化而造成電鍍 層剝落或變薄，且影響電解容器内之電極導電材料，而降 低電解時之工作效益。 Φ 再者，採用單一種金屬做為電解容器内之兩電極材 料，以及單純兩種金屬分別使用在兩電極上，二者具有電 解液化學鍵結能量單純應用之問題。 因此，如何解決上述習用電解氣體容器之問題即為本 創作之重點所在。 【新型内容】 本創作之主要目的，在於解決上述的問題而提供一種 • 具有結合式與複合式電極導電材料之電解氣體容器，其相 較於習用之電解裝置，在於電極部以不同金屬結合與複合 後，產生不同對電解液化學鍵結能量變化，以加速電解， 且於電解時所需之耗電量較低，使氫氣電解量相對提高。 為達前述之目的，本創作係包括： 一瓶體，其中具有一密閉之容室、於一與直流電源之 正負電極電性連接之電極部，一供氫氣排出之出口以及一 連通口，其特徵在於：瓶體於容室中設有二分別對應於正 6 M360246 負電極之電極部電性連接之電極部，各電解部係以至少二 可相互結合之導電材料結合與複合成型，而連通口於瓶體 外部連接〜外部向瓶體方向連通之止逆閥。 本創作之上述及其他目的與優點，不難從下述所選用 實施例之詳細說明與附圖中，獲得深入了解。 當然，本創作在某些另件上，或另件之安排上容許有 所不同，钽所選用之實施例，則於本說明書中，予以詳細 _ -說明，並於附圖中展示其構造。 【實施方式】 所參閱第1圖至第9圖，圖中所示者為本創作所選用 之實施例結構，此僅供說明之用，在專利申請上並不受此 種結構之限制。 本實施例知:供一種具有結合式與複合式電極導電材料 之電解氣體容器，其係包括： 一瓶體1，其中具有一密閉之容室1i、二導電端子 ·' . 1 7分別與直流電源之正負電極3電性連接，一出口工2 * 供氣體於產生後排出收集，以及一連通口 1 3於氫氣排出 時提供對流。於本實施例中’所指之氣體係指氫氣。 於本實施例中’該瓶體1於朝上之一端以一蓋體1 4 蓋合’以形成該容室1 1 ’而各該導電端子1 7、出口 1 2以及該連通口1 3係設於蓋體14上，且蓋體14朝容 室1 1中伸設一斷面呈十字形之連結板1 5，於連結板1 5上設有多數個穿孔（於圖中未示）。此外，該連通口 1 3 係於瓶體1之容室1 1中以一連通管i 3 i連通於瓶體工 M360246 底部之容室1 1，且於連通管131底部裝設一氣泡分散 器13 2，俾供將進入瓶體1内之空氣散化，而使原為粗 大之氣泡變成細微平均的氣泡分子’而排放於容室1 1内 之水中。 弃瓦體1於容室1 1中設有二電極部2，此二電極部2 係分別與正負電極對應之導電端子17電性連接，各電極 部2係以至少二可相互結合與複合之導電材料結合與複合 - 成型，而連通口1 3於瓶體1外部連接一由外部向瓶體1 籲 方向連通之止逆閥16，（於本實施例中，此止逆閥16係 可相對於連通口1 3拆裴，故於製氫時可使空氣由止逆閥 1 6進入瓶體1之容室1 1中，使氫氣能順利排出，再者 ，可將止逆閥1 6拆下，並由連通口1 3加水進入瓶體1 之容室1 1内，以電解製造氫氣）。 於本實施例中’如第3圖配合第7圖之剖示結構圖所 示，該電極部2係於一金屬A表面上，以圓條狀或平面狀 焊接（點焊/路焊）至少一種不同之金屬B，電極部2以 鲁.不同金屬A/B結合與複合後，產生不同對電解液化學鍵 • 結能量變化，以加速電解。其中，於本實施例之金屬入係 鉛條，而金屬B係錫材，於此係在鉛條之表面上焊接踢材 成型該電極部2 ’而各電極部2係於瓶體1内之連結板工 5兩兩相鄰之二板體間穿設於穿孔定位（由圖中可見係已 穿設鉛條” 本創作之電解氣體容器於電解時，係於瓶體1之容室 1 1内置入碳酸氫鈉粉末（俗稱小蘇打粉），以作為電解氣 8 M360246 氣之催化劑，其有別於習用之氫氧化鈉，意即遇水時不會 產生爆炸而使瓶體炸開之危險。瓶體！中容置破酸氣納粉 末，並與水結合後產生化學作用催化，且電極部2於通電 狀態下，即如第4圖所示，可將氫氣電解出，並由該出口 1 2輪出以供外部使用。而該止逆闊1 6之主要作用，在 於防止瓶體1内所製成之氫氣由連通口！ 3漏出，而僅讓 空氣單向進入瓶體1，提供瓶體1内氣體之對流。 、經由上述之說明可見，以金屬材料於表面施以不同金 _ •屬的焊接而成為結合性的電極部2,以產生不同電解液化 學鍵結能量變化作用，做為具現代科學結合與複合導電材 料的電解氣體容器應用。藉此，相較於習用之電解裝置， 在於電極部2以不同金屬結合與複合後，產生不同對電解 液化學鍵結能量變化，以加速電解，且於電解時所需之耗 電量較低，使氫氣電解量相對提高。 當然，本創作仍存在許多例子，其間僅細節上之變化 -。請參閱第8圖，其係本創作之第二實施例，其中該電極 •'部2A係於一金屬A(鉛條）表面上加工孔洞（於^中未 •示），並植入至少一種不同之金屬B (錫）結合與複合。其 中’於本實施例係於金屬A (鉛條）以鑽孔或沖型沖壓方 式加工孔洞，然後再將金屬B (錫）填入於孔洞中結合與 複合，藉此以達到與第一實施例相同之功效。 、 於本實施例中，除上述之兩種金屬之結合與複合外， 亦可以金屬材料或非金屬材料以及耐温塑膠混合製作。其 中，該電極部2亦具有一製成圓條狀或長平面條狀之金^ 9 M360246 二於此金屬亦加χ數孔洞（於圖中未示），並植人非 米或奈米粉末（如石墨/竹碳類/化學導電 塑膠混合製成之導電物，或植人金屬《或奈米粉it 溫塑膠混合製成之耐溫導電塑膠，結合與複合後 對電解液化學鍵結能量變化，相同可達到加速電解之功： 0 - §t參閱第6圖與第9圖之A部分結構示意圖，其係本 創作之第三實施例’其中該電極部2係以至少兩種圓條狀 籲或長平面條狀之金屬，互相交又扭轉成長條狀而成。立中 ，於本實施例係備製金屬A (錯條）以及金屬^ (錫條） ，並以上述交又扭轉方式結合與複合二者。本實施例與第 、一實施例之結合與複合方式不同在於，以交又扭轉將 二種不同金屬結合與縣，以制實蘭：Μ目同功效 〇 於本實施例中，除上述之兩種金屬交叉扭轉結合與複 合外，亦可以金屬材料或非金屬材料製作。該電極部2係 '具有一已混合非金屬微米或奈米粉末而具有導電作用之第 耐;JBL導電塑膠，以及一混合製成的金屬微米或奈米粉末 製成之第二耐溫導電塑膠，二者分別製成圓條狀或長平面 條狀，並相互交又扭轉成長條狀而做接觸性結合與複合， 於結合與複合後產生不同對電解液化學鍵結能量變化，以 達到加速電解之功效。 此外，請參閱第5圖，其係本創作之另一實施狀態示 意圖，其中係將一電解氣體容器之出口與一氫氣乾燥瓶4 M360246 連通，此氳氣乾燥瓶4具有一入口 41與電解氣體容器之 出口1 2相連通，且氫氣乾燥瓶4於底部以隔板4 2間隔 一水分沉澱槽4 3，電解氣體容器内製造之氫氣通過此水 分沉澱槽4 3時，將氫氣内含之水分沉澱於此，以去除氫 氣内留存之水分，乾燥後之氫氣再由氫氣乾燥瓶之出口 4 4送出使用。當然，於其他實施態樣之中，亦可具有多個 電解氣體容器之結合，以達到氫氣使用需求。 以上所述實施例之揭示係用以說明本創作，並非用以 限制本創作，故舉凡數值之變更或等效元件之置換仍應隸 屬本創作之範疇。 由以上詳細說明，可使熟知本項技藝者明瞭本創作的 確可達成前述目的，實已符合專利法之規定，爰提出專利 申請。 【圖式簡單說明】 第1圖係本創作之立體外觀圖 第2圖係本創作之立體分解圖 第3圖係本創作之剖面結構示意圖 第4圖係本創作之電解狀態示意圖 第5圖係本創作之電解氣體容器氫氣乾燥示意圖 第6圖係本創作之第二實施例剖示解構圖 第7圖係第3圖之A — A剖面結構圖 第8圖係第3圖於第二實施例之A —A剖面結構圖 第9圖係第6圖之電極部A部分局部結構示意圖 第1 0圖係習用電解氣體容器之剖面示意圖 11 M360246M360246 VIII. New description: [New technical field] This is a kind of electrolytic gas container with combined and composite electrode conductive materials, especially a device for electrolyzing gas. [Prior Art] According to the so-called electrolysis, the current is passed through an ion conductor (such as an electrolyte solution or a dissolved electrolyte) to cause a chemical change, that is, after the electric energy * $ ' is added, a free energy increase reaction occurs in the ion conduction. A pair of electrodes are inserted into the body, and an appropriate power source is connected to both ends, and current is transmitted inside the ion conductor by the movement of ions. In the interface between the electrode and the solution, the charge moves due to the progress of the electrode reaction, the metal surface is dissolved on the anode surface, an oxidation reaction such as oxygen is generated (anodization), and the cathode surface is subjected to metal precipitation, hydrogen generation reduction reaction (cathodic reduction). This is the principle of electrolysis of electrolytic gas containers. As shown in Fig. 10, it is a conventional electrolytic gas container which is provided with a plurality of electrode portions 9.1 in a bottle of φ body 90, and an electrode portion 9 1 on the side of the bottle body 90. The electric power source 9 is electrically connected. 2. Each of the electrode portions 9 1 has a plate shape and has a convex structure for electrolyzing hydrogen and oxygen in water for external use. However, the conventional electrolytic gas container is usually bulky, and the current required for electrolysis can reach 20 to 30 amps. Therefore, it is necessary to consume a relatively high amount of electricity, and it is possible to electrolyze an appropriate amount of hydrogen, and it is usually necessary to add a catalyst during electrolysis. Generally, sodium hydroxide is used, and when the catalyst encounters water, it will produce a high temperature of M360246, so there is a danger that the bottle will explode in the electrolysis process. In addition, the conventional electrolysis unit electroplates a plating layer on a conductive or non-conductive material, and after plating the electroplating layer for a long time, the electroplated layer coated on the surface of the electrode material changes due to strong acid or alkali corrosion. That is to say, the electrode erodes the plating layer due to the electrolyte, and the impedance changes to cause the plating layer to peel off or become thin, and affects the electrode conductive material in the electrolytic container, thereby reducing the work efficiency in electrolysis. Φ Furthermore, a single metal is used as the two electrode materials in the electrolytic container, and two kinds of metals are respectively used on the two electrodes, and the two have the problem that the chemical bonding energy of the electrolyte is simply applied. Therefore, how to solve the above problem of the conventional electrolytic gas container is the focus of the creation. [New content] The main purpose of this creation is to solve the above problems and provide an electrolytic gas container having a combined and composite electrode conductive material, which is combined with different metals in the electrode portion compared with the conventional electrolytic device. After compounding, different chemical bonding energy changes to the electrolyte are generated to accelerate the electrolysis, and the power consumption required for electrolysis is relatively low, so that the hydrogen electrolysis amount is relatively increased. For the purpose of the foregoing, the present invention comprises: a bottle body having a sealed chamber, an electrode portion electrically connected to the positive and negative electrodes of the DC power source, an outlet for discharging hydrogen gas, and a communication port, The utility model is characterized in that: the bottle body is provided with two electrode portions respectively corresponding to the electrode portions of the negative electrode of the positive 6 M360246 negative electrode in the chamber, and each of the electrolysis portions is combined and compositely formed by at least two conductive materials which can be combined with each other. The mouth is connected to the outside of the bottle body~ the external check valve is connected to the bottle body. The above and other objects and advantages of the present invention will become more apparent from the detailed description and the accompanying drawings. Of course, the present invention may be different in some of the parts, or the arrangement of the parts. The selected embodiments are described in detail in the present specification, and the construction thereof is shown in the drawings. [Embodiment] Referring to Figures 1 to 9, the structure of the embodiment selected for the present invention is shown for illustrative purposes only, and is not limited by such a structure in the patent application. The present embodiment is directed to: an electrolytic gas container having a combined and composite electrode conductive material, comprising: a bottle body 1 having a sealed chamber 1i, two conductive terminals · '. 1 7 and DC respectively The positive and negative electrodes 3 of the power source are electrically connected, an outlet 2 * is supplied for gas to be collected after being generated, and a communication port 13 is provided for convection when the hydrogen is discharged. The gas system referred to in the present embodiment refers to hydrogen gas. In the present embodiment, the bottle body 1 is covered with a cover 14 at one end of the bottle body to form the chamber 1 1 ', and each of the conductive terminal 17 and the outlet 1 2 and the communication port 13 are The cover body 14 is disposed on the cover body 14. The cover body 14 defines a cross-shaped connecting plate 15 extending into the chamber 11. The plurality of perforations (not shown) are disposed on the connecting plate 15. In addition, the communication port 13 is connected to the chamber 1 1 of the bottle body 1 to communicate with the chamber 1 1 at the bottom of the bottle body M360246 by a communication tube i 3 i , and a bubble disperser is disposed at the bottom of the communication tube 131 . 13 2, 俾 is used to disperse the air entering the bottle body 1, and the original coarse bubble becomes a fine average bubble molecule' and is discharged into the water in the chamber 11. The abutting chamber 1 is provided with a second electrode portion 2, wherein the two electrode portions 2 are electrically connected to the conductive terminals 17 corresponding to the positive and negative electrodes, and the electrode portions 2 are combined with each other at least two. The conductive material is combined and composited, and the communication port 13 is externally connected to the bottle body 1 with a check valve 16 that is externally connected to the bottle body 1. In the present embodiment, the check valve 16 is relatively The communication port 13 is dismantled, so that when the hydrogen is produced, the air can be introduced into the chamber 1 of the bottle body 1 by the check valve 16 to allow the hydrogen gas to be smoothly discharged. Further, the check valve 16 can be removed. Next, water is supplied from the communication port 13 into the chamber 1 1 of the bottle body 1 to produce hydrogen by electrolysis. In the present embodiment, as shown in the third embodiment, in conjunction with the sectional view of FIG. 7, the electrode portion 2 is attached to a surface of a metal A, and is welded in a strip shape or a planar shape (spot welding/road welding). A different kind of metal B, the electrode part 2 is combined with and combined with different metals A/B, which produces different chemical bond energy changes to the electrolyte to accelerate electrolysis. Wherein, the metal in the present embodiment is a lead strip, and the metal B is a tin material, wherein the electrode portion 2 is welded to the surface of the lead strip and the electrode portions 2 are attached to the bottle body 1 The connecting plate 5 and the two adjacent plates are placed between the two perforations (the lead wire has been worn as shown in the figure). The electrolytic gas container of the present invention is in the chamber 1 of the bottle body 1 during electrolysis. Built-in sodium bicarbonate powder (commonly known as baking soda powder), used as a catalyst for electrolyzed gas 8 M360246 gas, which is different from the conventional sodium hydroxide, meaning that there is no danger of explosion when the water is exposed and the bottle is blasted. The bottle body is filled with acid gas nano-powder and combined with water to generate chemical catalysis, and the electrode portion 2 is energized, that is, as shown in Fig. 4, hydrogen can be electrolyzed and exited by the outlet 1 2 rounds for external use. The main function of the stop-back wide 16 is to prevent the hydrogen produced in the bottle body 1 from leaking through the communication port! 3, and only let the air enter the bottle body 1 in one direction, providing The convection of the gas in the bottle body 1. As can be seen from the above description, the metal material is applied to the surface. The electrode part 2 of the same metal is welded to form a combined electrode part 2 to produce different electrolyte chemical bonding energy changes, and is used as an electrolytic gas container application with a modern scientific combination and a composite conductive material. The electrolysis device is characterized in that the electrode portion 2 is combined and recombined with different metals to produce different chemical bonding energy changes to the electrolyte to accelerate electrolysis, and the power consumption required for electrolysis is relatively low, so that the amount of hydrogen electrolysis is relatively increased. Of course, there are still many examples in this creation, only the details of which change - see Figure 8, which is a second embodiment of the present invention, in which the electrode ''2A is attached to a metal A (lead) surface Machining holes (not shown) and implanting at least one different metal B (tin) bond and composite. Among them, in this embodiment, the metal A (lead) is drilled or stamped. The holes are processed, and then the metal B (tin) is filled in the holes to be combined and composited, thereby achieving the same effect as the first embodiment. In this embodiment, in addition to the combination of the above two metals In addition, it can also be made of a metal material or a non-metal material and a temperature-resistant plastic. The electrode portion 2 also has a gold strip formed in a strip shape or a long flat strip. Holes (not shown in the figure), and implanted with non-meter or nano powder (such as graphite / bamboo carbon / chemical conductive plastic mixed conductive materials, or implanted metal " or nano powder it warm plastic mix The temperature-resistant conductive plastic combines with the chemical bond energy change of the electrolyte after compounding, which can achieve the work of accelerating electrolysis: 0 - §t Refer to the structure diagram of Part A of Figure 6 and Figure 9, which is the first part of the creation. In the third embodiment, the electrode portion 2 is made of at least two kinds of strip-shaped or long-plane strip-shaped metal, which are mutually twisted and twisted into a strip shape. In the center, the metal A is prepared in this embodiment. Strip) and metal ^ (tin strip), combined and composited in the above-mentioned cross-twisting manner. The combination of the embodiment and the first embodiment differs from the composite method in that the two different metals are combined with the county by the twisting and twisting, so that the solid blue: the same effect is used in the embodiment, except for the above two Metal cross-torsion bonding and compounding can also be made of metal materials or non-metal materials. The electrode portion 2 has a first resistance to a non-metallic micron or nano powder and has a conductive effect; a JBL conductive plastic, and a second temperature-resistant conductive plastic made of a mixed metal micron or nano powder. The two are made into round strips or long flat strips, and they are mutually twisted and twisted into strips for contact bonding and compounding. After bonding and compounding, different chemical bonding energy changes to the electrolyte are generated to accelerate the electrolysis. The effect. In addition, please refer to FIG. 5, which is a schematic view of another embodiment of the present invention, in which an outlet of an electrolytic gas container is connected to a hydrogen drying bottle 4 M360246, which has an inlet 41 and an electrolytic gas. The outlets of the container are connected to each other, and the hydrogen drying bottle 4 is separated from the bottom of the container by a partitioning block 4 2 with a moisture precipitation tank 43. When the hydrogen gas produced in the electrolytic gas container passes through the moisture precipitation tank 4 3, the moisture contained in the hydrogen is contained. Precipitated here to remove the moisture remaining in the hydrogen, and the dried hydrogen is sent out by the outlet of the hydrogen drying bottle. Of course, in other embodiments, a combination of a plurality of electrolytic gas containers may be provided to meet hydrogen demand. The above description of the embodiments is intended to be illustrative of the present invention and is not intended to limit the scope of the present invention. From the above detailed description, it will be apparent to those skilled in the art that the present invention can achieve the foregoing objectives, and it has been in compliance with the provisions of the Patent Law and has filed a patent application. [Simplified illustration of the drawing] Figure 1 is a three-dimensional appearance of the creation. Figure 2 is a three-dimensional exploded view of the creation. Figure 3 is a schematic diagram of the cross-sectional structure of the creation. Figure 4 is a schematic diagram of the electrolytic state of the creation. FIG. 6 is a cross-sectional view of the second embodiment of the present invention. FIG. 7 is a third embodiment of the A-A cross-sectional structural view. FIG. 3 is a third embodiment. A-A cross-sectional structure diagram Figure 9 is a schematic diagram of the partial structure of the electrode portion A of the sixth figure. Figure 10 is a schematic cross-sectional view of the conventional electrolytic gas container 11 M360246
【主要元件符號說明】 (習用部分） 瓶體9 0 電極部9 1 直流電源9 2 (本創作部分） 瓶體1 容室1 1 出π 1 2 連通口 1 3 連通管131 氣泡分散器1 3 2 蓋體1 4 連結板1 5 止逆閥1 6 導電端子17 電極部2 正負電極3 氫氣乾燥瓶4 入口 4 1 隔板4 2 水分沉澱槽4 3 出π 4 4 金屬A 金屬B 12[Explanation of main component symbols] (Utility section) Bottle body 9 0 Electrode part 9 1 DC power supply 9 2 (This creation part) Bottle body 1 Chamber 1 1 Out π 1 2 Communication port 1 3 Connecting tube 131 Bubble disperser 1 3 2 Cover 1 4 Connecting plate 1 5 Check valve 1 6 Conductive terminal 17 Electrode part 2 Positive and negative electrode 3 Hydrogen drying bottle 4 Inlet 4 1 Separator 4 2 Moisture sedimentation tank 4 3 Out π 4 4 Metal A Metal B 12