A COMPACT HYDROGEN-OXYGEN GENERATOR

Abstract

The present invention discloses a compact vehicle-mounted hydrogen-oxygen generator. In the fluid path, the water circulation outlet of the water tank is in communication via one of the two one-way throttle valves with the water pump, which is in communication with the electrolytic tank of the hydrogen-oxygen generator, which is in communication with the water circulation inlet of the water tank through the other one-way throttle valve, and the gas outlet of the water tank is in communication with an engine air-inlet via the steam-water separator and the dry flame arrester in turn. In the circuit, the water pump and the electrolytic tank of the hydrogen-oxygen generator are connected in parallel to the ends of the positive and negative electrodes of the vehicle power supply, respectively; the switch, the fuse and the electrolytic tank of the hydrogen-oxygen generator are connected in series to the vehicle power supply. The present invention realizes high-efficiency electrolysis through a porous electrode rod with high specific surface area, high catalytic activity, high electrical conductivity and high surface energy (being hydrophilic and air-repellent), as well as the compact design of tightly nested stainless steel sleeves; on the premise of meeting the gas production requirements, the present invention reduces the volume and weight of the electrolytic tank; the present invention realizes the single electrolytic chamber assembly of the vehicle-mounted hydrogen-oxygen generator, and allows direct connection to a single sealed electrolytic chamber in the circuit and the fluid path, effectively avoiding the problem with the serial connection of multiple electrolytic chambers.

Claims

1. A compact vehicle-mounted hydrogen-oxygen generator, comprising a box, a water tank, an electrolytic tank of the hydrogen-oxygen generator, a water pump, a working characteristic detection module, a fuse, a switch, a steam-water separator, a dry flame arrester and two one-way throttle valves, characterized in that: the water tank is provided on the top with a liquid injection port, and on the side with a water circulation outlet, a water circulation inlet and a gas outlet; in the fluid path, the water circulation outlet of the water tank is in communication via one of the two one-way throttle valves with the water pump, which is in communication with the electrolytic tank of the hydrogen-oxygen generator, which is in communication with the water circulation inlet of the water tank through the other one-way throttle valve, and the gas outlet of the water tank is in communication with an engine air-inlet via the steam-water separator and the dry flame arrester in turn; in the circuit, the water pump and the electrolytic tank of the hydrogen-oxygen generator are connected in parallel to the ends of the positive and negative electrodes of the vehicle power supply, respectively; the switch, the fuse and the electrolytic tank of the hydrogen-oxygen generator are connected in series to the vehicle power supply; with the working characteristic detection module having five terminals in total, the first terminal is connected to the negative electrode of the electrolytic tank of the hydrogen-oxygen generator, the second terminal is connected to the negative electrode of the power supply, the third terminal is connected to the positive electrode of the electrolytic tank of the hydrogen-oxygen generator, the fourth terminal is suspended and not connected, and the fifth terminal is connected to the positive electrode of the power supply; in the electrolytic tank of the hydrogen-oxygen generator, a sealed electrolytic chamber is formed by an upper cover plate, a stainless steel sleeve and a lower cover plate, and is provided inside with a stainless steel tube as a cathode and a porous electrode rod as an anode; the porous electrode rod passes through the upper cover plate to serve as a positive electrode terminal, and the limit bolt connected to the stainless steel tube passes through the lower cover plate to serve as a negative electrode terminal; the upper cover plate and the lower cover plate are respectively provided with a water inlet and a water outlet to connect to the sealed electrolytic chamber; the porous electrode rod is prepared through the following steps: 1) dissolving FeCl.sub.3.6H.sub.2O and Na.sub.2S.sub.2O.sub.8 in deionized water, and stirring to obtain solution A; 2) selecting iron-based alloy (containing 40% to 60% by mass of nickel, less than 0.03% by mass of S, and less than 0.03% by mass of P, with iron for the balance), and fully polishing its surface to remove the surface oxide scale; 3) adding the polished iron-based alloy obtained in step 2) to solution A, and reacting while stirring; and 4) taking out the iron-based alloy after the reaction, and washing and drying it.

2. The compact vehicle-mounted hydrogen-oxygen generator according to claim 1, characterized in that: the diameter of the anode porous electrode rod is 8-11.5 mm.

3. The compact vehicle-mounted hydrogen-oxygen generator according to claim 1, characterized in that: the stainless steel tube is a 304 stainless steel tube with an inner diameter of 12-14 mm and an outer diameter of 14-16 mm.

4. The compact vehicle-mounted hydrogen-oxygen generator according to claim 1, characterized in that: in step 1), the mass ratio of Na.sub.2S.sub.2O.sub.8, FeCl.sub.3.6H.sub.2O and water is (2 to 4):(5 to 7):25, and the stirring is done magnetically at a rotating speed of 50-150 rpm for 5-10 min.

5. The compact vehicle-mounted hydrogen-oxygen generator according to claim 1, characterized in that: 180-360 mesh SiC sandpaper is used for polishing in step 2), with the polishing time of 5-15 min.

6. The compact vehicle-mounted hydrogen-oxygen generator according to claim 1, characterized in that: the stirring in step 3) is done magnetically at a rotating speed of 50-150 rpm for 2-12 h; and in step 4), the washing is done by washing with water and ethanol for 3-5 times, respectively, and the drying is done by drying in an oven for 0.5-2 h at the temperature of 40° C. to 80° C.

7. The compact vehicle-mounted hydrogen-oxygen generator according to claim 1, characterized in that: the upper cover plate is provided at the center of the lower surface with an upper circular groove, and the lower cover plate is provided at the center of the upper surface with a lower circular groove, with a stainless steel sleeve embedded between the upper circular groove and the lower circular groove; the porous electrode rod has its top threaded through the threaded through hole of the upper cover plate, and its bottom embedded in the small groove of the lower cover plate, so as to get fastened; the stainless steel tube is respectively embedded into the upper large groove of the upper cover plate and the lower large groove of the lower cover plate, so as to get fastened.

8. The compact vehicle-mounted hydrogen-oxygen generator according to claim 1, characterized in that: the upper cover plate is provided in the upper circular groove with an upper large groove, which is provided inside with a threaded through hole; a water inlet is arranged between the upper circular groove and the upper large groove; the lower cover plate is provided in the lower circular groove with a lower large groove, which is provided inside with a small groove, with a water outlet and a threaded through hole arranged between the lower circular groove and the lower large groove; the porous electrode rod has its top threaded through the threaded through hole of the upper cover plate, and its bottom embedded in the small groove of the lower cover plate, so as to get fastened; the stainless steel tube is respectively embedded into the upper large groove of the upper cover plate and the lower large groove of the lower cover plate, so as to get fastened; a limit bolt passes through a conductive plate in connection with the stainless steel tube of the cathode material, and then passes through the threaded through hole of the lower cover plate to fit with a nut to serve as the negative electrode terminal of the electrolytic tank; a water inlet pipe joint is embedded in the water inlet of the upper cover plate, and a water outlet pipe joint is embedded in the water outlet of the lower cover plate.

9. The compact vehicle-mounted hydrogen-oxygen generator according to claim 1, characterized in that: an electrolyte (0.03-0.5 M caustic potassium solution) flows into the compact sealed electrolytic chamber through the water inlet, and the generated hydrogen-oxygen mixture gas quickly flows out of the water outlet together with the electrolyte.

10. The compact vehicle-mounted hydrogen-oxygen generator according to claim 1, characterized in that: the upper cover plate and the lower cover plate are fastened through four limit bolts.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0039] FIG. 1 is a schematic structural diagram of the compact vehicle-mounted hydrogen-oxygen generator of the present invention;

[0040] FIG. 2 is an outline view of the water tank in the compact vehicle-mounted hydrogen-oxygen generator of the present invention;

[0041] FIG. 3 is a schematic diagram of gas-liquid flow of the compact vehicle-mounted hydrogen-oxygen generator of the present invention in operation;

[0042] FIG. 4 is a schematic diagram of circuit connection of the compact vehicle-mounted hydrogen-oxygen generator of the present invention in operation;

[0043] FIG. 5 is a three-dimensional structural diagram of the electrolytic tank of the present invention;

[0044] FIG. 6 is a three-dimensional structural diagram of the upper cover plate of the electrolytic tank of the present invention;

[0045] FIG. 7 is a three-dimensional structural diagram of the lower cover plate of the electrolytic tank of the present invention;

[0046] FIG. 8 is an exploded view of the electrolytic tank of the present invention;

[0047] FIG. 9 shows a scanning electron micrograph of the original iron-based alloy in Example 1 for the preparation of porous electrodes;

[0048] FIG. 10 shows a scanning electron micrograph of the porous iron-based alloy prepared in Example 1, in which (a) shows the electron micrograph with an magnification of 2,000 times, and (b) shows the electron micrograph with an magnification of 10,000 times;

[0049] FIG. 11 shows the comparison of the scanning electron micrograph and electrical conductivity of the porous iron-based alloy prepared in Example 1, in which (a) is an electron micrograph of a cross section, and (b) shows the comparison of electrical conductivity between the porous iron-based alloy electrode and a commercial porous electrode;

[0050] FIG. 12 shows an XRD diffraction pattern of the iron-based alloy in Example 1 before and after the dealloying treatment;

[0051] FIG. 13 shows a photo of the wetting angle of the iron-based alloy in Example 1 before and after the dealloying treatment, in which (a) shows the photo of the wetting angle before the dealloying treatment, and (b) shows the photo of the wetting angle after the dealloying treatment;

[0052] FIG. 14 shows a polarization curve of the porous iron-based alloy, the original iron-based alloy, and the austenitic stainless steel in Example 1 for the preparation of porous electrodes;

[0053] FIG. 15 is a diagram showing the Tafel slope of the porous iron-based alloy and the original iron-based alloy in Example 1 for the preparation of porous electrodes;

[0054] FIG. 16 shows a scanning electron micrograph of the porous iron-based alloy prepared through the dealloying treatment with the FeCl.sub.3+Na.sub.2S.sub.2O.sub.8 solution in Example 2 for the preparation of porous electrodes, in which (a) shows the electron micrograph with an magnification of 2,000 times, and (b) shows the electron micrograph with an magnification of 10,000 times;

[0055] FIG. 17 shows a scanning electron micrograph of the porous iron-based alloy prepared through the dealloying treatment with the FeCl.sub.3+Na.sub.2S.sub.2O.sub.8 solution in Example 3 for the preparation of porous electrodes, in which (a) shows the electron micrograph with an magnification of 2,000 times, and (b) shows the electron micrograph with an magnification of 10,000 times.

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0056] In order to better understand the technical solution of the present invention, the present invention will be described in more detail below in conjunction with examples and drawings, but the embodiments of the present invention are not limited thereto.

[0057] A compact vehicle-mounted hydrogen-oxygen generator is shown in FIGS. 1-4, comprising a water tank 1, a box 2, an electrolytic tank 3 of the hydrogen-oxygen generator, a water pump 4, a working characteristic detection module 5, a switch 6, a fuse 7, a one-way throttle valve 8, a steam-water separator 9 and a dry flame arrester 10; the water tank 1 is arranged outside the box 2, which is made of aluminum alloy with high strength, light weight and good thermal conductivity; the electrolytic tank 3 of the hydrogen-oxygen generator and the water pump 4 are fastened in the box 2 by limit bolts, and the working characteristic detection module 5, the switch 6 and the fuse 7 are embedded in the box 2 by clamping.

[0058] As shown in FIG. 2, the water tank 1 is provided with a liquid injection port 101, a water circulation outlet 102, a water circulation inlet 103, and a gas outlet 104; when the device is in operation, the water tank 1 is filled with 0.1M caustic potassium solution as the electrolyte through the liquid injection port 101.

[0059] In the fluid path, the water circulation outlet 102 of the water tank 1 is in communication via one of the two one-way throttle valves 8 with the water pump 4, which is in communication with the electrolytic tank 3 of the hydrogen-oxygen generator, which is in communication with the water circulation inlet 103 of the water tank 1 through the other one-way throttle valve 8, and the gas outlet 104 of the water tank 1 is in communication with the engine air-inlet 11 via the steam-water separator 9 and the dry flame arrester 10 in turn.

[0060] In the circuit, the water pump 4 and the electrolytic tank 3 of the hydrogen-oxygen generator are connected in parallel to the ends of the positive and negative electrodes of the vehicle power supply 12, respectively; the switch 6, the fuse 7 and the electrolytic tank 3 of the hydrogen-oxygen generator are connected in series to the vehicle power supply 12; with the working characteristic detection module 5 having five terminals in total, the first terminal 501 is connected to the negative electrode of the electrolytic tank of the hydrogen-oxygen generator, the second terminal 502 is connected to the negative electrode of the power supply, the third terminal 503 is connected to the positive electrode of the electrolytic tank of the hydrogen-oxygen generator, the fourth terminal 504 is suspended and not connected, and the fifth terminal 505 is connected to the positive electrode of the power supply.

[0061] A one-way throttle valve 8 is respectively arranged between the water circulation outlet 102 and the water pump 4, and between the electrolytic tank 3 of the hydrogen-oxygen generator and the water circulation inlet 103 to prevent gas-liquid backflow; besides, a steam-water separator 9 and a dry flame arrester 10 are arranged between the gas outlet 104 and the engine air-inlet, so as to dry the mixture gas and prevent backfire.

[0062] The electrolyte enters the water tank 1 through the liquid injection port 101, then flows out of the water tank 1 through the water circulation outlet 102 of the water tank 1, and then flows into the electrolytic tank 3 of the hydrogen-oxygen generator through the one-way throttle valve 8 under the action of the water pump 4; the generated hydrogen-oxygen mixture gas returns to the water tank 1 via the water circulation inlet 103 through another one-way throttle valve 8 along with the circulating flow of the electrolyte, then passes through the gas outlet 104, and then passes through the steam-water separator 9 and the dry flame arrester 10 in turn to enter the engine air-inlet 11.

[0063] The switch 6 and fuse 7 control and protect the electrolytic tank of the hydrogen-oxygen generator; the water pump 4 and the electrolytic tank 3 of the hydrogen-oxygen generator are connected in parallel to the vehicle power supply, working independently without interfering with each other; the working characteristic detection module 5 can monitor the voltage, current and other characteristics of the electrolytic tank 3 of the hydrogen-oxygen generator in real time.

[0064] As shown in FIGS. 5-8, the electrolytic tank of the hydrogen-oxygen generator is provided at the top and bottom with a cover plate, namely the upper cover plate 301 and the lower cover plate 302; the upper cover plate 301 is provided at the center of the lower surface with an upper circular groove 3015, and the lower cover plate 302 is provided at the center of the upper surface with a lower circular groove 3025, with a stainless steel sleeve 303 embedded between the upper circular groove 3015 and the lower circular groove 3025; the first limit bolt 308 penetrates the first upper through hole 3011 of the upper cover plate 301 and the first lower through hole 3021 of the lower cover plate 302; the second limit bolt 309 penetrates the second upper through hole 3012 of the upper cover plate 301 and the second lower through hole 3022 of the lower cover plate 302; the third limit bolt 310 penetrates the third upper through hole 3013 of the upper cover plate 301 and the third lower through hole 3023 of the lower cover plate 302; the fourth limit bolt 311 penetrates the fourth upper through hole 3014 of the upper cover plate 301 and the fourth lower through hole 3024 of the lower cover plate 302; and the first limit bolt 308, the second limit bolt 309, the third limit bolt 310 and the fourth limit bolt 311 are fastened with nuts at the bottom of the lower cover plate 302, so that the upper cover plate 301, the stainless steel sleeve 303 and the lower cover plate 302 form a sealed electrolytic chamber.

[0065] The sealed electrolytic chamber is provided inside with a stainless steel tube 312 as the cathode and a porous electrode rod 306 as the anode material. The porous electrode rod 306 has micron-scale three-dimensional pores in communication with each other, which is conducive to the mass transfer process and gas diffusion during electrolysis; besides, there are many nano-scale steps on the micron-scale pore wall; the pores of this micro-nano structure greatly increase the specific surface area of the electrode and expose more active sites, improving the thermodynamic and kinetic conditions in the electrolysis process, thereby effectively reducing the use of the electrode material. Therefore, in the present invention, the stainless steel tube 312 preferably has an inner diameter of 12-14 mm and an outer diameter of 14-16 mm; and the porous electrode rod 306 preferably has a diameter of 8-11.5 mm. The upper cover plate 301 is provided in the upper circular groove 3015 with an upper large groove 3016, which is provided inside with a threaded through hole 3017; a water inlet 3018 is arranged between the upper circular groove 3015 and the upper large groove 3016; the lower cover plate 302 is provided in the lower circular groove 3025 with a lower large groove 3026, which is provided inside with a small groove 3027, with a water outlet 3028 and a threaded through hole 3029 arranged between the lower circular groove 3025 and the lower large groove 3026; the porous electrode rod 306 has its top threaded through the threaded through hole 3017 of the upper cover plate 301, and its bottom embedded in the small groove 3027 of the lower cover plate 302, so as to get fastened; the stainless steel tube 312 is respectively embedded into the upper large groove 3016 of the upper cover plate 301 and the lower large groove 3026 of the lower cover plate 302, so as to get fastened; the stainless steel tube and the porous electrode rod are in close cooperation with each other in the electrolytic tank, and the distance between them is extremely small, which can effectively reduce the solution impedance and improve the electrolysis efficiency. The porous electrode rod 306 of the anode material passes through the threaded through hole 3017 and fits with the nut to serve as the positive electrode terminal of the electrolytic tank; a limit bolt 307 passes through a conductive plate 313 in connection with the stainless steel tube 312 of the cathode material, and then passes through the threaded through hole 3029 of the lower cover plate 302 to fit with a nut to serve as the negative electrode terminal of the electrolytic tank; the water inlet pipe joint 304 is embedded in the water inlet 3018 of the upper cover plate 301, and the water outlet pipe joint 305 is embedded in the water outlet 3028 of the lower cover plate 302. By optimizing the electrode material and electrolytic tank structure, the present invention reduces the volume and weight of the hydrogen-oxygen generator; the electrolyte flows through the water inlet 3018 into the compact sealed electrolytic chamber at a higher flow rate, which can accelerate the diffusion of substances in the sealed electrolytic chamber; the generated hydrogen-oxygen mixture gas quickly flows with the electrolyte out of the water outlet 3028, which can significantly reduce the concentration potential caused by the local pH change due to electrolysis; in addition, the accumulation of bubbles at active sites is avoided, which hinders the contact of electrolyte ions with the active sites, resulting in an increase in electric potential.

EXAMPLES FOR THE PREPARATION OF POROUS ELECTRODE RODS

Example 1

[0066] (1) Dissolving 7 parts by weight of FeCl.sub.3.6H.sub.2O and 3 parts by weight of Na.sub.2S.sub.2O.sub.8 in 25 parts by weight of deionized water, and magnetically stirring at a rotating speed of 150 rpm for 5 min to obtain solution A;

[0067] (2) selecting the original iron-based alloy (containing 40% by mass of nickel, less than 0.03% by mass of S, and less than 0.03% by mass of P, provided by Wuxi Shenggang Superhard Material Co., Ltd.), and polishing its surface with 180 mesh SiC sandpaper for 5 min to remove the surface oxide scale;

[0068] (3) adding the polished iron-based alloy obtained in step (2) to solution A, and reacting for 4 h while magnetically stirring at a rotating speed of 100 rpm; and

[0069] (4) taking out the porous iron-based alloy after the reaction, then washing it with water and ethanol respectively for 3 times, then drying the porous iron-based alloy in an oven at 50° C. for 1 h, and finally taking it out to obtain the porous electrode rod.

[0070] The scanning electron micrograph of the original iron-based alloy was shown in FIG. 9, exhibiting a flat surface without pore structure.

[0071] The scanning electron micrograph of the iron-based alloy after the dealloying treatment was shown in FIG. 10. It can be seen in FIG. 10(a) at a magnification of 2,000 times that micron-scale three-dimensional pores in communication with each other (having a pore diameter of 10-20 μm) were formed on the surface of the alloy, conducive to the mass transfer process of the electrolyte and intermediates and the diffusion of the produced gas in the electrolysis process; it can be seen in FIG. 10(b) at a magnification of 10,000 times that many nano-scale steps were formed on the micron-scale pore wall; the pores of this micro-nano structure greatly increased the specific surface area of the electrode and exposed more active sites, improving the thermodynamic and kinetic conditions in the electrolysis process.

[0072] The scanning electron micrograph of the cross section of the iron-based alloy after the dealloying treatment was shown in FIG. 11(a), exhibiting that the porous iron-based alloy electrode had a porous surface and a dense core; the dense core could provide a fast electron transfer channel for the porous layer on the surface and improve the electrical conductivity of the porous iron-based alloy electrode; as shown in FIG. 11.(b), the electrical conductivity of the porous iron-based alloy electrode was significantly higher than that of the commercial porous electrode, which could effectively reduce the contact impedance of the hydrogen-oxygen generator.

[0073] The XRD diffraction pattern of the iron-based alloy after the dealloying treatment was shown in FIG. 12; the strongest diffraction peak moved from the (111) plane before the dealloying treatment to the (220) plane after the dealloying treatment, and the exposed (220) plane was a non-closely packed plane and had the characteristics of high surface energy; in addition, the unique micro-nano pore structure of the surface of the alloy destroyed the gas-liquid-solid three-phase contact line, which could significantly enhance the hydrophilic and gas-repellent properties of the electrode. As shown in FIG. 13, the contact angle of the iron-based alloy before and after the dealloying treatment was reduced from 50.8° to 24.5°, such that the porous surface of the iron-based alloy could better achieve wetting contact with the electrolyte, the active sites on the surface could be fully utilized, and the gas generated by the reaction could be more easily dissipated. Therefore, the mass transfer process and gas diffusion during electrolysis could be promoted while the compact design of the hydrogen-oxygen generator was realized, improving the electrolysis efficiency.

[0074] With a three-electrode system adopted, the porous iron-based alloy prepared in this example, the original iron-based alloy, and the austenitic stainless steel were respectively used as the working electrode, the platinum sheet was used as the counter electrode, and the Hg/HgO electrode was used as the reference electrode; the electrochemical test was performed on the Gamry electrochemical workstation to characterize the electrolytic-water catalytic performance of the porous iron-based alloy, taking the specific test parameters as follows: using the linear sweep voltammetry, with the scanning speed at 5 mV/s and the scanning voltage at 0.2-0.7 V (vs. Hg/HgO); after the test, the voltage was converted into the electrode potential relative to the reversible hydrogen electrode according to the conversion formula, E.sub.RHE=E.sub.Hg/HgO+0.059*pH+0.098.

[0075] It can be seen from FIG. 14 that the present invention used the iron-based alloy as the electrode material, whose electrochemical performance was far superior to that of the traditional austenitic stainless steel. It can be seen from FIGS. 14 and 15 that after the iron-based alloy was dealloyed to form a porous structure, the overpotential at 10 mA.Math.cm.sup.−2 dropped from 346 mV to 309 mV, and the Tafel slope dropped from 87 mV/dec to 53 mV/dec, indicating that the thermodynamic and kinetic conditions in the electrolysis process had been improved, and the electrochemical performance had been further improved. Therefore, using the porous iron-based alloy as the porous electrode material of the hydrogen-oxygen generator effectively improved the electrolysis efficiency, reducing the use of electrode material on the premise of ensuring the gas production; on this basis, the structure of the electrolytic tank of the hydrogen-oxygen generator was optimized, so that the volume and weight of the device were reduced. The volume and weight of the electrolytic tank of the hydrogen-oxygen generator prepared in this example did not exceed 0.2 L and 0.5 kg, respectively, and the electrolytic tank per unit volume could produce at least 1.875 L of the mixture gas per minute.

Example 2

[0076] (1) Dissolving 5 parts by weight of FeCl.sub.3.6H.sub.2O and 4 parts by weight of Na.sub.2S.sub.2O.sub.8 in 25 parts by weight of deionized water, and magnetically stirring at a rotating speed of 50 rpm for 10 min to obtain solution A;

[0077] (2) selecting the iron-based alloy (containing 40% by mass of nickel, less than 0.03% by mass of S, and less than 0.03% by mass of P, provided by Wuxi Shenggang Superhard Material Co., Ltd.), and polishing its surface with 360 mesh SiC sandpaper for 15 min to remove the surface oxide scale;

[0078] (3) adding the polished iron-based alloy obtained in step (2) to solution A, and reacting for 2 h while magnetically stirring at a rotating speed of 150 rpm; and

[0079] (4) taking out the porous iron-based alloy after the reaction, then washing it with water and ethanol respectively for 3 times, then drying the porous iron-based alloy in an oven at 80° C. for 0.5 h, and finally taking it out to obtain the porous electrode rod for the device.

[0080] The scanning electron micrograph of the iron-based alloy after the dealloying treatment was shown in FIG. 16. It can be seen in FIG. 16(a) at a magnification of 2,000 times that the micron-scale three-dimensional pores in communication with each other (having a pore diameter of 10-20 μm) were still formed on the surface of the alloy; it can be seen in FIG. 16(b) at a magnification of 10,000 times that many nano-scale steps were formed on the micron-scale pore wall; the three-dimensional communicated micro-nano pores could effectively improve the thermodynamic and kinetic conditions in the electrolysis process, and reduce the overpotential and Tafel slope of the oxygen evolution reaction, with the corresponding test results similar to Example 1.

Example 3

[0081] (1) Dissolving 6 parts by weight of FeCl.sub.3.6H.sub.2O and 3 parts by weight of Na.sub.2S.sub.2O.sub.8 in 25 parts by weight of deionized water, and magnetically stirring at a rotating speed of 100 rpm for 8 min to obtain solution A;

[0082] (2) selecting the iron-based alloy (containing 40% by mass of nickel, less than 0.03% by mass of S, and less than 0.03% by mass of P, provided by Wuxi Shenggang Superhard Material Co., Ltd.), and polishing its surface with 270 mesh SiC sandpaper for 10 min to remove the surface oxide scale;

[0083] (3) adding the polished iron-based alloy obtained in step (2) to solution A, and reacting for 12 h while magnetically stirring at a rotating speed of 150 rpm; and

[0084] (4) taking out the porous iron-based alloy after the reaction, then washing it with water and ethanol respectively for 3 times, then drying the porous iron-based alloy in an oven at 40° C. for 2 h, and finally taking it out to obtain the porous electrode rod for the device.

[0085] The scanning electron micrograph of the iron-based alloy after the dealloying treatment was shown in FIG. 17. It can be seen in FIG. 17(a) at a magnification of 2,000 times that the micron-scale three-dimensional pores in communication with each other (having a pore diameter of 10-20 μm) were still formed on the surface of the alloy; it can be seen in FIG. 17(b) at a magnification of 10,000 times that the nano-scale steps were formed on the micron-scale pore wall; the three-dimensional communicated micro-nano pores could effectively improve the thermodynamic and kinetic conditions in the electrolysis process, and reduce the overpotential and Tafel slope of the oxygen evolution reaction, with the corresponding test results similar to Example 1.