TW201301627A - Battery device with electric potential generated by oxidation-reduction reaction - Google Patents
Battery device with electric potential generated by oxidation-reduction reaction Download PDFInfo
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本發明係有關一種以氧化還原反應產生電位的電池裝置,其主要透過電性觸媒(Catalyst)技術,將正電化學阻尼效應用來氧化發電,負電化學阻尼效應產生還原反應,構成物理之共振封閉迴路,達到百分之百零污染、零排放的綠色能源。The invention relates to a battery device for generating a potential by a redox reaction, which mainly uses an electrocatalyst (Catalyst) technology to use a positive electrochemical damping effect for oxidative power generation, and a negative electrochemical damping effect to generate a reduction reaction to form a physical resonance. Closed loop, reaching 100% pollution, zero emission of green energy.
按,燃料電池是化學生電的裝置,其中,氫及氧直接結合成水,合成反應所釋出的能量即為電能(Cell)。電池可分為酸性(Acid)及鹼性(Alkaline)兩種性質。據Arrhenius的酸鹼離子理論,在水溶液中可以電離(Ionization)出氫氧根離子(OH-),並不會產生其他陰離子的化合物,亦即是提供氫氧根離子(OH-)或吸收氫離子(H+)的化合物,稱為鹼性。其中電離即是一物理性質,表示在能量作用下,原子、分子形成離子的過程。若溶液中氫離子(H+)大於純水中氫離子的濃度之化合物,亦即溶解於水時釋出的陽離子全部都是氫離子(H+)的化合物,或是電子(e-)的接受者,稱為酸性。故氧離子(O2-)是氫氧根離子(OH-)的共軛鹼According to the fuel cell, the device is a student electric device, in which hydrogen and oxygen are directly combined into water, and the energy released by the synthesis reaction is electric energy (Cell). The battery can be divided into two properties: acid (Acid) and alkaline (Alkaline). According to Arrhenius's theory of acid-base ion, the hydroxide ion (OH - ) can be ionized in aqueous solution, and no other anion compound is produced, that is, hydrogen ion ion (OH - ) or hydrogen absorption is provided. A compound of ion (H + ), called alkaline. Ionization is a physical property that indicates the process by which atoms and molecules form ions under the action of energy. If the hydrogen ion (H + ) in the solution is greater than the concentration of hydrogen ions in the pure water, that is, the cations released when dissolved in water are all hydrogen ion (H + ) compounds, or electrons (e - ) The recipient is called acid. Therefore, the oxygen ion (O 2- ) is the conjugate base of the hydroxide ion (OH - )
O2-+H2O→2 OH- O 2- +H 2 O → 2 OH -
請參閱圖二。將氫、氧氣為燃料時,先將純水20電解,此時,陽極放出電子為氧化反應,陰極得到電子為還原反應,稱為電解反應。圖二中,以氧化鋅21作為陽極,以碳棒22作為陰極,箭頭表示電荷流方向23。Please refer to Figure 2. When hydrogen or oxygen is used as the fuel, the pure water 20 is first electrolyzed. At this time, the electrons are emitted from the anode to be an oxidation reaction, and the cathode is subjected to a reduction reaction, which is called an electrolytic reaction. In Fig. 2, zinc oxide 21 is used as the anode, carbon rod 22 is used as the cathode, and arrows indicate the charge flow direction 23.
陽極:2H2O→O2+4H++4e- Anode: 2H 2 O → O 2 +4H + +4e -
陰極:2H2O+2e- →H2+2OH- Cathode: 2H 2 O+2e - → H 2 + 2OH -
電解全反應:2H2O→2H2+O2 Electrolytic total reaction: 2H 2 O → 2H 2 +O 2
反電解反應,即陽極加入氫氣,陰極加入氧氣,產生純水、電動勢、及熱(即是水蒸氣),稱為氫氧燃料電堆。The reverse electrolysis reaction, that is, the addition of hydrogen to the anode and the addition of oxygen to the cathode, produces pure water, electromotive force, and heat (ie, water vapor), which is called a hydrogen-oxygen fuel stack.
陽極:H2 →2H++2e- Ea:0VAnode: H 2 → 2H + + 2e - Ea: 0V
陰極:O2+4H++4e- →2H2O Ec:1.22PVCathode: O 2 +4H + +4e - → 2H 2 O Ec: 1.22PV
反電解全反應:2H2+O2 →2H2O+熱 Ec-Ea=1.22PVReverse electrolysis: 2H 2 +O 2 → 2H 2 O+heat Ec-Ea=1.22PV
其中電解(Electrolysis)是一種化學反應,表示在能量作用於電解質時,在陰極、陽極上引起的氧化還原反應的過程。當電解金屬-空氣燃料電堆時,以不同金屬當電極者為酸性、單一金屬為電極者為鹼性。請參閱圖一。本發明以鹼性的鋅-空氣燃料電堆為例;Electrolysis is a chemical reaction that represents the process of redox reactions on the cathode and anode when energy is applied to the electrolyte. When electrolyzing a metal-air fuel stack, it is alkaline when the electrodes are acidic and the single metal is the electrode. Please refer to Figure 1. The invention takes an alkaline zinc-air fuel stack as an example;
陽極:Zn+2OH- →ZnO+H2O+2e- Ea:0VAnode: Zn+2OH - → ZnO+H 2 O+2e - Ea: 0V
陰極:O2+2H2O+4e- →4OH- Ec:1.22PVCathode: O 2 +2H 2 O+4e - → 4OH - Ec: 1.22PV
充電反應:2Zn+O2 →2ZnO Ec-Ea=1.22PVCharging reaction: 2Zn+O 2 → 2ZnO Ec-Ea=1.22PV
此化學反應產生電動勢外,還產生純水與熱。其中,電解液10為氫氧化鉀溶液(KOH);另還會吸收二氧化碳(CO2),導致燃料電池無法持續運作。圖一中作為陽極的為鋅板11,作為陰極的為碳棒12。圖一中,編號為K的為陰極;編號為A為陽極;標號為13的箭頭係表示電子流的方向。This chemical reaction produces electromotive force and also produces pure water and heat. Among them, the electrolyte 10 is a potassium hydroxide solution (KOH); it also absorbs carbon dioxide (CO 2 ), which causes the fuel cell to fail to operate continuously. In Fig. 1, the zinc plate 11 is used as the anode and the carbon rod 12 is used as the cathode. In Figure 1, the number K is the cathode; the number A is the anode; the arrow numbered 13 indicates the direction of the electron flow.
本發明所提供之以氧化還原反應產生電位的電池裝置,其包含:一電池槽裝置、一電性觸媒裝置、一緩衝電池裝置,一整流充電裝置。該電池槽裝置鹽類水溶液為電解液,且其陽極為不會與電解液產生化學反應的金屬,其陰極為具有導電性與呼吸孔隙的碳材料;該碳材料可呼吸空氣並在空氣溶解於電解液中時釋出含有氫氧根的負離子。該電性觸媒裝置,其為電化學阻尼效應的催化劑,用以催化電池槽裝置內的氧化反應與還原反應的進行,而使電池槽裝置做氧化充電與還原放電的反應。該整流充電裝置能夠將電池槽裝置所輸出的交流型態的電位轉成直流型態,並對緩衝電池裝置充電。The battery device for generating a potential by a redox reaction according to the present invention comprises: a battery cell device, an electrical catalyst device, a buffer battery device, and a rectifying charging device. The battery tank device salt aqueous solution is an electrolyte, and the anode thereof is a metal that does not chemically react with the electrolyte, and the cathode thereof is a carbon material having conductivity and respiratory pores; the carbon material can breathe air and dissolve in the air. An anion containing hydroxide is released in the electrolyte. The electrical catalyst device is an electrochemical damping effect catalyst for catalyzing the oxidation reaction and the reduction reaction in the battery cell device, and the battery cell device is oxidized and reduced. The rectification charging device can convert the AC type potential output from the battery cell device into a DC mode and charge the buffer battery device.
本發明所提供之以氧化還原反應產生電位的電池裝置,其中,緩衝電池裝置為具有可重複充、放電能力的二次電池。該緩衝電池裝置可為酸性二次電池、鹼性二次電池其中之一,亦可為酸性二次電池、鹼性二次電池串/並聯使用的共振電池。The battery device for generating a potential by a redox reaction according to the present invention, wherein the buffer battery device is a secondary battery having reproducible charge and discharge capabilities. The buffer battery device may be one of an acidic secondary battery and an alkaline secondary battery, and may be a resonance secondary battery used in an acidic secondary battery or an alkaline secondary battery string/parallel connection.
本發明所提供之以氧化還原反應產生電位的電池裝置,其中,該電性觸媒裝置包含設置有脈衝產生器,以及電子釋出迴路與電荷釋出迴路。該脈衝產生器能夠產生正、負脈衝,以分別令電荷釋出迴路釋出電荷,電子釋出迴路釋出電子。該電性觸媒裝置對電池槽裝置釋出電子時,能夠使電池槽裝置內產生反電解的還原反應,而在電池槽裝置的陽極與陰極之間產生電位差。該電性觸媒裝置對電池槽裝置釋出電荷時,能夠使電池槽裝置內產生電解的氧化反應,而在電池槽裝置的陽極與陰極之間產生電位差。The invention provides a battery device for generating a potential by a redox reaction, wherein the electrical catalyst device comprises a pulse generator, and an electron release circuit and a charge release circuit. The pulse generator is capable of generating positive and negative pulses to cause the charge release loop to release charge and the electron release loop to release electrons. When the electrical catalyst device discharges electrons to the battery cell device, a reduction reaction of reverse electrolysis can be generated in the battery cell device, and a potential difference is generated between the anode and the cathode of the battery cell device. When the electric catalyst device discharges electric charge to the battery cell device, an electrolytic oxidation reaction can be generated in the battery cell device, and a potential difference is generated between the anode and the cathode of the battery cell device.
本發明所提供之以氧化還原反應產生電位的電池裝置,其中,該電性觸媒裝置所產生的電荷與電子的相位相差為180度。負電化學阻尼效應用來產生還原反應,使電池槽裝置的內部構成物理之共振封閉迴路,達到百分之百零污染、零排放的綠色能源。The battery device for generating a potential by a redox reaction according to the present invention, wherein the electric charge generated by the electrical catalyst device differs from the phase of the electron by 180 degrees. The negative electrochemical damping effect is used to generate a reduction reaction, so that the internal structure of the battery cell device constitutes a physical resonance closed loop, achieving 100% pollution and zero emission of green energy.
請參閱圖三、圖四。本發明係有關一種以金屬-空氣燃料電堆為再生能主體之電池裝置,亦為一種以氧化還原反應產生電位的電池裝置。本發明的裝置結構如圖三所示,其包含:電池槽裝置30、電性觸媒裝置40、整流充電裝置50、緩衝電池裝置60。Please refer to Figure 3 and Figure 4. The present invention relates to a battery device using a metal-air fuel stack as a main body of regenerative energy, and a battery device for generating a potential by a redox reaction. The device structure of the present invention is shown in FIG. 3, and includes a battery cell device 30, an electrical catalyst device 40, a rectifying charging device 50, and a buffer battery device 60.
其中,電池槽裝置30係以鹽類水溶液為電解液31,且其陽極32為不會與電解液31產生化學反應的金屬,其陰極33為具有導電性與呼吸孔隙的碳材料。該碳材料可呼吸空氣並在空氣溶解於電解液31中時釋出含有氫氧根的負離子。Among them, the battery tank device 30 has a salt aqueous solution as the electrolytic solution 31, and the anode 32 is a metal that does not chemically react with the electrolytic solution 31, and the cathode 33 is a carbon material having conductivity and respiratory pores. The carbon material can breathe air and release negative ions containing hydroxide when the air is dissolved in the electrolyte 31.
配合圖五。該電性觸媒裝置40,其為電化學阻尼效應的催化劑,用以催化電池槽裝置30內的氧化反應與還原反應的進行。該電性觸媒裝置40係對電池槽裝置30分別釋出電子與電荷,以催化電池槽裝置30內的氧化反應與還原反應的進行。該電性觸媒裝置40對電池槽裝置30釋出電荷時,能夠使電池槽裝置30內產生電解的氧化反應,而在電池槽裝置30的陽極32與陰極33之間產生電位差。該電性觸媒裝置40釋出電子時,產生負電化學阻尼效應,能夠使電池槽裝置30內產生反電解的還原反應,而在電池槽裝置30的陽極32與陰極33之間產生電位差。負電化學阻尼效應產生還原反應,能夠使電池槽裝置30的內部構成物理之共振封閉迴路,達到百分之百零污染、零排放的綠色能源。該電性觸媒裝置40所產生的電荷與電子的相位相差為180度者Match Figure 5. The electrical catalyst device 40 is a catalyst for electrochemical damping effect for catalyzing the progress of the oxidation reaction and the reduction reaction in the battery cell device 30. The electrical catalyst device 40 releases electrons and charges to the battery cell device 30 to catalyze the progress of the oxidation reaction and the reduction reaction in the battery cell device 30. When the electric catalyst device 40 discharges electric charge to the battery cell device 30, an electrolytic oxidation reaction can be generated in the battery cell device 30, and a potential difference is generated between the anode 32 and the cathode 33 of the battery cell device 30. When the electron catalyst device 40 emits electrons, a negative electrochemical damping effect is generated, and a reduction reaction of reverse electrolysis can be generated in the battery cell device 30, and a potential difference is generated between the anode 32 and the cathode 33 of the battery cell device 30. The negative electrochemical damping effect produces a reduction reaction, which enables the internal structure of the battery cell device 30 to form a physical resonance closed loop, achieving 100% pollution and zero emission of green energy. The electric charge generated by the electrical catalyst device 40 is different from the phase of the electron by 180 degrees.
該緩衝電池裝置60,其為具有可重複充、放電能力的二次電池。該整流充電裝置50,其能夠將電池槽裝置30所輸出的交流型態的電位轉成直流型態,並對緩衝電池裝置60充電。The buffer battery device 60 is a secondary battery having reproducible charging and discharging capabilities. The rectifying and charging device 50 is capable of converting the electric potential of the AC type output from the battery tank device 30 into a DC mode and charging the buffer battery device 60.
以前述昔知的鋅-空氣燃料電堆為例,如圖一表示的反電解的氧化反應為充電反應:Taking the aforementioned zinc-air fuel stack as an example, the oxidation reaction of the reverse electrolysis shown in FIG. 1 is a charging reaction:
2Zn+O2 →2ZnO Ec-Ea=1.22PV2Zn+O 2 → 2ZnO Ec-Ea=1.22PV
如圖二表示的電解的還原反應為充電反應:The reduction reaction of electrolysis shown in Figure 2 is a charging reaction:
2H2O→2H2+O2 2H 2 O → 2H 2 +O 2
本發明係將以上兩者結合成再同一電池槽裝置30內作用,如圖四所示。該電解液31改成中性的海水,並將氧化與還原之化學反應(電解),改為物理反應的電離方式,亦即充電與放電相位相差180度,並且在同一電池槽裝置30作用。茲以鋅-空氣燃料電堆為例,陽極32為鋅金屬,陰極33為可吸入氧氣(O2)的碳材料。當電池槽裝置30獲得電子時,能夠使電池槽裝置30內產生反電解的還原反應,則可再電池槽裝置30的陰、陽極33、32之間產生電位差。其反應方程式為:In the present invention, the above two are combined to function in the same battery cell device 30, as shown in FIG. The electrolyte 31 is changed to neutral seawater, and the chemical reaction (electrolysis) of oxidation and reduction is changed to the ionization mode of the physical reaction, that is, the phase of charge and discharge is 180 degrees out of phase, and acts on the same battery cell device 30. Taking a zinc-air fuel stack as an example, the anode 32 is zinc metal and the cathode 33 is a carbon material that can absorb oxygen (O 2 ). When the battery cell device 30 obtains electrons, a reduction reaction of the reverse electrolysis can be generated in the battery cell device 30, and a potential difference is generated between the cathode and the anodes 33 and 32 of the re-sink device 30. The reaction equation is:
陽極:Zn+2OH- →ZnO+H2O+2e- Ea:0VAnode: Zn+2OH - → ZnO+H 2 O+2e - Ea: 0V
陰極:O2+2H2O+4e- →4OH- Ec:1.22PVCathode: O 2 +2H 2 O+4e - → 4OH - Ec: 1.22PV
放電反應:2Zn+O2 →2ZnO Ec-Ea=1.22PVDischarge reaction: 2Zn+O 2 → 2ZnO Ec-Ea=1.22PV
當電池槽裝置30獲得電荷(正電)時,能夠使電池槽裝置30內產生反電解的氧化反應,則可再電池槽裝置30的陰、陽極33、32產生電位差。其反應方程式為:When the battery cell device 30 obtains a charge (positive charge), an oxidation reaction of the reverse electrolysis can be generated in the battery cell device 30, and a potential difference is generated between the cathode and the anode 33, 32 of the re-battery cell device 30. The reaction equation is:
陽極:ZnO+H+ →Zn+H2O+2c+ Ea:1.22PVAnode: ZnO+H + → Zn+H 2 O+2c + Ea: 1.22PV
陰極:O2+H2O+c+ →H+ Ec:0VCathode: O 2 +H 2 O+c + → H + Ec: 0V
充電反應:2ZnO→Zn+O2 Ec-Ea=-1.22PVCharging reaction: 2ZnO → Zn+O 2 Ec-Ea=-1.22PV
前述中,該電性觸媒裝置40可對電池槽裝置30釋出電子或電荷,以觸發電池槽裝置30內的氧化反應或還原反應。故該電性觸媒裝置40所釋出的電子與電荷分別為前述氧化反應與還原反應的催化劑。In the foregoing, the electrical catalyst device 40 can release electrons or charges to the battery cell device 30 to trigger an oxidation reaction or a reduction reaction in the battery cell device 30. Therefore, the electrons and charges released by the electrical catalyst device 40 are the catalysts for the oxidation reaction and the reduction reaction, respectively.
前述之放電反應與充電反應的催化過程中,都會放電且極性相反,且充電與放電相位相差180度(由電性觸媒裝置40控制),即產生交流電堆。在將電堆經該整流充電裝置50轉換成直流後,可對該緩衝電池裝置60充電。In the catalytic process of the foregoing discharge reaction and charging reaction, the discharge is reversed and the polarity is opposite, and the phases of charge and discharge are 180 degrees out of phase (controlled by the electrical catalyst device 40), that is, the alternating current stack is generated. After the stack is converted to DC by the rectifying charging device 50, the buffer battery device 60 can be charged.
本發明著重於物理反應(電離),需要以一離子產生裝置來完成反應。該電性觸媒裝置40即為一離子產生器。該電性觸媒裝置40,其可產生電荷(正離子)於電池槽裝置30內,產生充電作用;其可產生電子(負離子)於電池槽裝置30內,產生放電作用。該電性觸媒裝置40可稱之為電化學阻尼器。該電性觸媒裝置40包含一脈衝(Pulse)產生器41,以及電子釋出迴路43與電荷釋出迴路42。脈衝(Pulse)產生器41能夠產生正、負脈衝。其中,正脈衝可啟動電荷釋出迴路而是出電荷,負脈衝可啟動電子釋出迴路而是出電子。該電子釋出迴路43包含設置可將頻率轉成電子的電晶體431、電性阻尼共振艙432、升壓變壓器433。該電荷釋出迴路42包含設置可將頻率轉成電荷的電晶體421、電性阻尼共振艙422、升壓變壓器423。該電子釋出迴路43與該電荷釋出迴路42的變壓器433、423能夠分別於負離子輸出端434輸出電子,於正離子輸出端424輸出電荷,以及於中子電位端44輸出中性電位。由於電化學之充電與放電之氧化還原反應必須達到電荷守恆,等效於物理的共振效應,而其共振艙更需要本發明人的中華民國第098128110號「無窮級共振艙的超級電感器」的無窮級共振艙技術。將電化學阻尼器422、432完成正電化反應與負電化反應,稱之為電性觸媒。電性觸媒裝置40所需的電源可來自於緩衝電池裝置60之P及N處。該電性觸媒裝置40所輸出的電子當強氧化劑,所輸出的電荷當強還原劑。該電性觸媒裝置40的電子與電荷的輸出端係延伸至伸入該電池槽裝置30內,且其電極34係選擇強電子流介電材料的奈米碳管。當正、負升壓變壓器OFF時,會有反電動勢產生,藉由共振艙與正、負脈衝產生器構成共振,並借以控制離子產生量;同時共振艙可以將脈衝產生器所產生的反電動勢吸收,致使電子與電荷輸出迴路的運作更穩定。The present invention focuses on physical reactions (ionization) and requires an ion generating device to complete the reaction. The electrical catalyst device 40 is an ion generator. The electrical catalyst device 40 generates charge (positive ions) in the battery cell device 30 to generate a charging function; it can generate electrons (negative ions) in the battery cell device 30 to generate a discharge. The electrical catalyst device 40 can be referred to as an electrochemical damper. The electrical catalyst device 40 includes a pulse generator 41, and an electron release circuit 43 and a charge release circuit 42. The pulse generator 41 is capable of generating positive and negative pulses. Among them, the positive pulse can initiate the charge release circuit but the charge, and the negative pulse can activate the electron release circuit but the electron. The electron emission circuit 43 includes a transistor 431, an electrically damped resonance chamber 432, and a step-up transformer 433 that are configured to convert a frequency into electrons. The charge release circuit 42 includes a transistor 421, an electrically damped resonance chamber 422, and a step-up transformer 423 that are configured to convert a frequency into an electric charge. The electron release circuit 43 and the transformers 433, 423 of the charge release circuit 42 are capable of outputting electrons at the negative ion output terminal 434, outputting charge at the positive ion output terminal 424, and outputting a neutral potential at the neutron potential terminal 44. Since the electrochemical redox reaction of charge and discharge must reach the conservation of charge, which is equivalent to the physical resonance effect, the inventor of the present invention needs the inventor's Republic of China No. 098128110 "super inductor of infinite-order resonance cabin". Infinite level resonance cabin technology. The electrochemical dampers 422, 432 complete the positive and negative electrolysis reactions, which are called electrical catalysts. The power required by the electrical catalyst device 40 can come from the P and N of the buffer battery device 60. The electrons output by the electrical catalyst device 40 are strong oxidants, and the outputted charges are strong reducing agents. The electron and charge output of the electrical catalyst device 40 extends into the cell slot device 30, and the electrode 34 is a carbon nanotube that selects a strong electron flow dielectric material. When the positive and negative step-up transformers are OFF, there is a counter electromotive force generated by the resonance chamber to form a resonance with the positive and negative pulse generators, thereby controlling the amount of ion generation; and the resonance chamber can generate the counter electromotive force generated by the pulse generator. Absorption, resulting in more stable operation of the electron and charge output loop.
前述緩衝電池裝置60可為圖六所示的酸性二次電池61。該酸性二次電池61由等效的電感器611,電容器612所組成,為並聯諧振型態。緩衝電池裝置60可為圖七所示的鹼性二次電池62。該鹼性二次電池62由等效的電感器621,電容器622所組成,為串聯諧振諧振型態。可將圖六所示的酸性二次電池61與圖七鹼性二次電池62作並聯使用的共振電池63,做為緩衝電池裝置60,如圖八所示者。The aforementioned buffer battery device 60 may be the acidic secondary battery 61 shown in FIG. The acidic secondary battery 61 is composed of an equivalent inductor 611 and a capacitor 612, and is a parallel resonance type. The buffer battery device 60 may be the alkaline secondary battery 62 shown in FIG. The alkaline secondary battery 62 is composed of an equivalent inductor 621 and a capacitor 622, and is a series resonant resonance type. The resonant battery 63 used in parallel with the acidic secondary battery 61 shown in Fig. 6 and the alkaline secondary battery 62 of Fig. 7 can be used as the buffer battery device 60, as shown in Fig. 8.
昔知的鋅-空氣電池充電與放電行為,皆屬化學行為,故電解與反電解無法同時在同一個電池槽裝置內進行。在氧化與還原反應進行過程中,電解水溶液(如KOH)直接參與反應,如吸收CO2,造成電堆本身中毒而無法運作,如將電解水溶液直接換成氯化鈉水溶液,會產生毒氣(氯氣)及NaOH。本發明的氧化充電與還原放電的反應過程中,電解液31只用於物理反應而不參與化學反應。電解液31除了不用純水外,可選擇中性的海水溶液。由於電解液31不做化學反應(即電解),故不會有害的氣體產生。至於陰極33的電極材料選擇不參與反應的材料,如石墨、碳棒、奈米碳管、碳纖維等。金屬電極32部份,排除容易與海水產生化學反應的鋰金屬(Li)以外的其他金屬。該金屬電極部份亦可為鋰合金。採物理反應時,容量密度由離子決定,因此,只要離子溶度增加,即使體積縮小,容量密度也是提高。The charging and discharging behavior of the zinc-air battery is a chemical behavior, so the electrolysis and the reverse electrolysis cannot be carried out in the same battery tank device at the same time. During the oxidation and reduction reaction, the electrolytic aqueous solution (such as KOH) directly participates in the reaction, such as absorbing CO 2 , causing the reactor itself to be poisoned and unable to operate. For example, if the electrolytic aqueous solution is directly changed into an aqueous solution of sodium chloride, toxic gas (chlorine gas) is generated. ) and NaOH. In the reaction process of the oxidative charging and the reduction discharge of the present invention, the electrolytic solution 31 is used only for physical reaction without participating in a chemical reaction. The electrolyte 31 can be selected from neutral sea water solutions in addition to pure water. Since the electrolyte 31 does not undergo a chemical reaction (ie, electrolysis), no harmful gas is generated. As the electrode material of the cathode 33, a material which does not participate in the reaction, such as graphite, carbon rod, carbon nanotube, carbon fiber or the like, is selected. The metal electrode 32 portion excludes metals other than lithium metal (Li) which are liable to chemically react with seawater. The metal electrode portion may also be a lithium alloy. In the case of a physical reaction, the capacity density is determined by ions. Therefore, as long as the ion solubility increases, the capacity density increases even if the volume is reduced.
綜合上述,本發明所提供之以氧化還原反應產生電位的電池裝置,其運用電性觸媒裝置所產生的負電化學阻尼效應所產生還原反應,能夠使電池槽裝置的內部構成物理之共振封閉迴路,以物理反應取代化學變化,達到百分之百零污染、零排放的綠色能源。又,本發明的氧化放電、還原充電所產生的交流型態的電位,能夠通過整流充電裝置,轉換成直流型態而充入緩衝電池裝置內,提高本發明自體發電的效益。In summary, the battery device for generating a potential by a redox reaction according to the present invention generates a physical resonance closed loop by using a negative electrochemical damping effect generated by an electrical catalyst device to generate a reduction reaction. Replacing chemical changes with physical reactions to achieve 100% pollution and zero-emissions of green energy. Further, the potential of the alternating current type generated by the oxidation discharge and the reduction charging of the present invention can be converted into a direct current type by a rectifying and charging device and charged into the buffer battery device, thereby improving the efficiency of the self-generated power of the present invention.
以上說明對本發明而言只是說明性的,而非限制性的,本領域普通技術人員理解,在不脫離所附說明書所限定的精神和範圍的情况下,可做出許多修改、變化或等效,但都將落入本發明的保護範圍内。The above description is intended to be illustrative, and not restrictive, and many modifications, variations and equivalents may be made without departing from the spirit and scope of the invention. However, they all fall within the scope of protection of the present invention.
10...電解液10. . . Electrolyte
11...陽極11. . . anode
12...陰極12. . . cathode
13...電子流方向13. . . Electron flow direction
20...純水20. . . Pure water
21...氧化鋅twenty one. . . Zinc oxide
22...碳棒twenty two. . . Carbon rod
23...電荷流方向twenty three. . . Charge flow direction
30...電池槽裝置30. . . Battery slot device
31...電解液31. . . Electrolyte
32...陽極32. . . anode
33...陰極33. . . cathode
34...電極34. . . electrode
40...電性觸媒40. . . Electrical catalyst
41...正、負脈衝產生器41. . . Positive and negative pulse generator
42...電荷產生迴路42. . . Charge generation loop
421...電晶體421. . . Transistor
422...電化學阻尼器422. . . Electrochemical damper
423...變壓器423. . . transformer
424...電荷輸出端424. . . Charge output
43...電子產生迴路43. . . Electronic generation loop
431...電晶體431. . . Transistor
432...電化學阻尼器432. . . Electrochemical damper
423...變壓器423. . . transformer
434...電子輸出端434. . . Electronic output
44...中子輸出端44. . . Neutron output
50...整流充電裝置50. . . Rectification charging device
60...緩衝電池裝置60. . . Buffer battery device
61...酸性二次電池61. . . Acid secondary battery
611...電感器611. . . Inductor
612...電容器612. . . Capacitor
62...鹼性二次電池62. . . Alkaline secondary battery
621...電感器621. . . Inductor
622...電容器622. . . Capacitor
63...共振電池63. . . Resonant battery
P...陽極P. . . anode
N...陰極N. . . cathode
A...陽極A. . . anode
K...陰極K. . . cathode
圖一為鋅-空氣燃料電堆的示意圖。Figure 1 is a schematic diagram of a zinc-air fuel stack.
圖二為昔知氫氧產生器的示意圖。Figure 2 is a schematic diagram of a known oxyhydrogen generator.
圖三為本發明的結構圖。Figure 3 is a structural view of the present invention.
圖四為本發明電池槽裝置的示意圖。Figure 4 is a schematic view of the battery cell device of the present invention.
圖五為電性觸媒裝置實施例的電路圖。Figure 5 is a circuit diagram of an embodiment of an electrical catalyst device.
圖六為酸性二次電池的等效電路結構圖。Fig. 6 is an equivalent circuit structure diagram of an acidic secondary battery.
圖七為鹼性二次電池的等效電路結構圖。Figure 7 is an equivalent circuit structure diagram of an alkaline secondary battery.
圖八為共振電池的等效電路結構圖。Figure 8 is an equivalent circuit structure diagram of a resonant battery.
30...電池槽裝置30. . . Battery slot device
40...電性觸媒裝置40. . . Electrical catalyst device
50...整流充電裝置50. . . Rectification charging device
60...緩衝電池裝置60. . . Buffer battery device
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