Novel hydrogen production device
The hydrogen production unit, designed with composite electrodes and density-layered towers, achieves low-voltage water electrolysis and high-efficiency gas separation, solving the problem of high hydrogen production costs, reducing energy consumption, and improving safety and separation efficiency.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- 赵铁领
- Filing Date
- 2023-12-07
- Publication Date
- 2026-04-17
AI Technical Summary
The high cost of hydrogen production makes its development and utilization difficult to carry out on a large scale.
The hydrogen production unit, designed with composite electrodes and porous insulation layers, produces hydrogen and oxygen through low-voltage water electrolysis and uses a density stratification tower for gas separation. It also incorporates sensors and controllers to achieve real-time monitoring and fault handling.
It reduces energy consumption in hydrogen production, improves electrolysis and gas separation efficiency, ensures stable equipment operation and safety, and reduces the cost of hydrogen development and utilization.
Smart Images

Figure CN121874802A_ABST
Abstract
Description
Technical Field
[0001] This invention relates to the field of hydrogen production technology, specifically a novel hydrogen production device. Background Technology
[0002] Hydrogen is a diatomic gas with relatively high chemical reactivity. It is colorless, odorless, flammable, and explosive. Hydrogen is gaseous at room temperature and pressure, has the lowest density of all gases, and is sparingly soluble in water. While hydrogen is difficult to reduce under normal conditions, it can react chemically with other substances under high temperature or electrical conditions.
[0003] With the transformation of the global energy structure, hydrogen energy, as a clean, efficient, and renewable energy source, has attracted increasing attention from various countries. However, due to the high cost of hydrogen production, the development and utilization of hydrogen has remained in its infancy, making large-scale mining and utilization impossible. Therefore, a new type of hydrogen production device is proposed. Summary of the Invention
[0004] The purpose of this invention is to provide a novel hydrogen production apparatus to solve the problems mentioned in the background art.
[0005] To achieve the above objectives, the present invention provides the following technical solution: a novel hydrogen production device, comprising a base, a reaction chamber installed on the top of the base, a support frame installed on the bottom of the base, a gas collection chamber for mixing hydrogen and oxygen provided on one side of the reaction chamber, a first density stratification tower and a second density stratification tower for settling the hydrogen and oxygen mixture on one side of the gas collection chamber, and a composite electrode installed on the bottom of the inner wall of the reaction chamber.
[0006] The composite electrode includes a positive terminal, a number of porous insulating layers, a negative terminal, a positive relay, a negative relay, a number of positive electrodes, and a number of negative electrodes. The output terminal of the positive terminal is electrically connected to the input terminal of the positive relay, and the output terminal of the positive relay is electrically connected to the input terminals of the positive electrodes. The output terminal of the negative terminal is electrically connected to the input terminal of the negative relay, and the output terminal of the negative relay is electrically connected to the input terminals of the negative electrodes. One side of each of the positive and negative electrodes is connected to both sides of the porous insulating layer.
[0007] Preferably, a controller is installed on one side of the base, and an alarm is installed on the other side of the base.
[0008] Preferably, the composite electrode is fixed to a mounting bracket on its outer side, the porous insulating layer has a thickness of 0.1-1mm, the composite electrode can be configured as a single-panel, linear, or matrix structure according to actual needs, and the material used for the composite electrode can be carbon sheet, zinc sheet, copper sheet, silver sheet, platinum sheet, or stainless steel sheet, and the thickness of both the positive and negative electrodes is 0.1-1mm.
[0009] Preferably, a feeding pipe is installed on the top of the outer side of the reaction chamber, which can be opened and closed manually. A mixing chamber is provided on the inner side of the reaction chamber, and a first pressure sensor is installed on the top of the inner wall of the mixing chamber.
[0010] Preferably, the top of the reaction chamber is connected to the air inlet of the gas collecting chamber via a pipe, and the air outlet of the reaction chamber is equipped with a first electric ball valve.
[0011] Preferably, a first temperature sensor and a second pressure sensor are installed at the bottom of the inner wall of the gas collecting chamber, a first pressure relief valve is installed at the top of the gas collecting chamber, and the gas outlet of the gas collecting chamber is connected to a first density stratification tower and a second density stratification tower through pipelines.
[0012] Preferably, a second electric ball valve is installed at the inlet end of the first density stratification tower, a second temperature sensor and a third pressure sensor are respectively installed on the inner wall of the first density stratification tower, a third electric ball valve is installed at the oxygen outlet end of the first density stratification tower, a fourth electric ball valve is installed at the hydrogen outlet end of the first density stratification tower, and a second pressure relief valve is installed on one side of the top of the first density stratification tower.
[0013] Preferably, a fifth electric ball valve is installed at the inlet end of the second density stratification tower, a third temperature sensor and a fourth pressure sensor are installed on the inner wall of the second density stratification tower, a sixth electric ball valve is installed at the oxygen outlet end of the second density stratification tower, a seventh electric ball valve is installed at the hydrogen outlet end of the second density stratification tower, and a third pressure relief valve is installed on one side of the top of the second density stratification tower.
[0014] Preferably, the output terminals of the first temperature sensor, second temperature sensor, third temperature sensor, first pressure sensor, second pressure sensor, third pressure sensor, and fourth pressure sensor are electrically connected to the input terminal of the controller, and the output terminal of the controller is electrically connected to the input terminals of the first electric ball valve, second electric ball valve, third electric ball valve, fourth electric ball valve, fifth electric ball valve, sixth electric ball valve, seventh electric ball valve, positive relay, negative relay, and alarm.
[0015] The present invention also provides a production method for a novel hydrogen production device, comprising the following steps:
[0016] S1. Composite electrode fabrication: Take multiple positive electrodes, negative electrodes, and a porous insulating layer. Place the porous insulating layer between the positive and negative electrodes. Encapsulate the multiple positive electrodes, porous insulating layer, and negative electrodes together to obtain a composite electrode. Connect the multiple positive electrodes to a positive relay and a positive terminal, and connect the multiple negative electrodes to a negative terminal and a negative relay.
[0017] S2. Feeding and energizing: Add sodium hydroxide aqueous solution and distilled water into the mixing chamber inside the reaction chamber through the feeding pipe. The mixing concentration ratio of sodium hydroxide aqueous solution and distilled water is 1:10-1:200. Control the positive and negative relays to energize the positive and negative electrodes through the controller. The voltage is 1.15-1.25 volts.
[0018] S3. After the positive and negative electrodes are connected to the electrolyte in the water, a direct current is applied. An oxidation reaction occurs at the positive electrode, where water molecules lose electrons to produce oxygen. A reduction reaction occurs at the negative electrode, where water molecules gain electrons to produce hydrogen. Through this reaction, water electrolysis produces oxygen and hydrogen. The resulting hydrogen and oxygen mixture is transported through a pipeline to the inside of the gas collecting chamber. The two outlets of the gas collecting chamber respectively transport hydrogen and oxygen to the inside of the first and second density stratification towers through pipelines. The hydrogen and oxygen have different densities inside the first and second density stratification towers, and they will undergo a stratification process, with hydrogen on top and oxygen at the bottom. At this time, the outlets of the third and sixth electric ball valves supply oxygen to the outside, while the outlets of the fourth and seventh electric ball valves supply hydrogen to the outside.
[0019] Compared with the prior art, the present invention, employing the above technical solution, has the following technical effects:
[0020] This invention employs a unique design with positive and negative electrodes and a porous insulating layer in its composite electrode, enabling the hydrogen production device to perform water electrolysis at low voltage to produce hydrogen and oxygen. This design improves electrolysis efficiency, reduces energy consumption, and significantly lowers the cost of hydrogen development and utilization, paving the way for large-scale hydrogen development and utilization in the future. Simultaneously, through a first and second density separation tower, hydrogen and oxygen can undergo a separation process internally, with hydrogen on top and oxygen at the bottom, facilitating subsequent transportation and use and improving gas separation efficiency. Multiple temperature and pressure sensors are also installed to monitor the equipment's operating status in real time and transmit the information to the controller. The controller controls the opening and closing of each electric ball valve based on the information, ensuring stable operation of the equipment. When a malfunction occurs in the hydrogen production device, the first, second, and third pressure relief valves can promptly release pressure, improving equipment safety. Attached Figure Description
[0021] To more clearly illustrate the technical solutions in the embodiments of this application or the prior art, the drawings used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings described below are only some embodiments of this application. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.
[0022] Figure 1 This is a schematic diagram of the device connection of the present invention;
[0023] Figure 2 This is a schematic diagram of the controller connection of the present invention;
[0024] Figure 3 This is a schematic diagram of the first composite electrode structure of the present invention;
[0025] Figure 4 This is a schematic diagram of the second composite electrode structure of the present invention;
[0026] Figure 5 This is a schematic diagram of the porous insulating layer structure of the present invention;
[0027] Figure 6 This is a top view of the fixing frame structure of the present invention;
[0028] Figure 7 This is a schematic diagram of the main structure of the fixing frame of the present invention.
[0029] Explanation of reference numerals in the attached drawings: 1. Base; 2. Support frame; 3. Positive terminal; 4. Porous insulating layer; 5. Negative terminal; 6. Positive relay; 7. Negative relay; 8. Composite electrode; 9. Reaction chamber; 10. Feed pipe; 11. Mixing chamber; 12. First electric ball valve; 13. First pressure sensor; 14. Gas collection chamber; 15. First pressure relief valve; 16. First temperature sensor; 17. Second pressure sensor; 18. Second electric ball valve; 19. Positive electrode; 20. Negative electrode; 21. Second temperature sensor; 22. Third pressure sensor; 23. Third electric ball valve; 24. First density stratification tower; 25. Fourth electric ball valve; 26. Second pressure relief valve; 27. Fifth electric ball valve; 28. Controller; 29. Mounting bracket; 30. Third temperature sensor; 31. Sixth electric ball valve; 32. Fourth pressure sensor; 33. Second density stratification tower; 34. Seventh electric ball valve; 35. Third pressure relief valve; 36. Alarm. Detailed Implementation
[0030] The technical solutions of the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only some embodiments of the present invention, and not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those skilled in the art without creative effort are within the scope of protection of the present invention.
[0031] It should be noted that when a component is referred to as "fixed to" or "set on" another component, it can be directly on or indirectly set on the other component; when a component is referred to as "connected to" another component, it can be directly connected to or indirectly connected to the other component.
[0032] It should be understood that the terms "length", "width", "upper", "lower", "front", "rear", "first", "second", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are only for the convenience of describing this application and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this application.
[0033] Furthermore, the terms "first" and "second" are used for descriptive purposes only and should not be construed as indicating or implying relative importance or implicitly specifying the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of this application, "multiple" or "several" means two or more, unless otherwise explicitly specified.
[0034] It should be noted that the structures, proportions, sizes, etc., shown in the accompanying drawings of this specification are only for the purpose of assisting those skilled in the art in understanding and reading the content disclosed in the specification, and are not intended to limit the conditions under which this application can be implemented. Therefore, they have no substantial technical significance. Any modifications to the structure, changes in the proportions, or adjustments to the size should still fall within the scope of the technical content disclosed in this application, provided that they do not affect the effects and purposes that this application can produce.
[0035] Example
[0036] Please see Figure 1-7The present invention provides a technical solution: a novel hydrogen production device, including a base 1, a reaction chamber 9 installed on the top of the base 1, a support frame 2 installed at the bottom of the base 1, a gas collection chamber 14 for mixing hydrogen and oxygen is provided on one side of the reaction chamber 9, a first density stratification tower 24 and a second density stratification tower 33 for settling the hydrogen and oxygen mixture are respectively provided on one side of the gas collection chamber 14, and a composite electrode 8 is installed at the bottom of the inner wall of the reaction chamber 9.
[0037] The composite electrode 8 includes a positive terminal 3, several porous insulating layers 4, a negative terminal 5, a positive relay 6, a negative relay 7, several positive electrodes 19, and several negative electrodes 20. Multiple positive electrodes 19, negative electrodes 20, and porous insulating layers 4 are taken, and the porous insulating layers 4 are placed between the positive electrodes 19 and negative electrodes 20. The composite electrode 8 is obtained by encapsulating multiple positive electrodes 19, porous insulating layers 4, and negative electrodes 20 together. The output terminal of the positive terminal 3 is electrically connected to the input terminal of the positive relay 6, and the output terminal of the positive relay 6 is electrically connected to the input terminals of several positive electrodes 19. The output terminal of the negative terminal 5 is electrically connected to the input terminal of the negative relay 7, and the output terminal of the negative relay 7 is... The positive electrode 19 and negative electrode 20 are electrically connected to the input terminals of several negative electrodes 20 respectively. One side of the positive electrode 19 and negative electrode 20 are respectively connected to the two sides of the porous insulating layer 4. The negative terminal 5 and positive terminal 3 are used to transmit DC low voltage power. The multiple positive electrodes 19 are connected to the positive relay 6 and the positive terminal 3, and the multiple negative electrodes 20 are connected to the negative terminal 5 and the negative relay 7. The composite electrode 8 is fixed with a fixing bracket 29 on the outside. The thickness of the porous insulating layer 4 is 0.1-1mm. The composite electrode 8 can be set into a single-panel, linear, or matrix structure according to actual needs. The material used for the composite electrode 8 can be carbon sheet, zinc sheet, copper sheet, silver sheet, platinum sheet, or stainless steel sheet. The thickness of the positive electrode 19 and negative electrode 20 is 0.1-1mm.
[0038] To facilitate control of the hydrogen production unit, a controller 28 is installed on one side of the base 1, and an alarm 36 is also installed on one side of the base 1. A feed pipe 10 is installed on the top of the outer side of the reaction chamber 9, which can be manually opened and closed. A mixing chamber 11 is provided inside the reaction chamber 9, and a first pressure sensor 13 is installed on the top of the inner wall of the mixing chamber 11. The top of the reaction chamber 9 is connected to the inlet of the gas collecting chamber 14 via a pipe, and a first electric ball valve 12 is installed at the outlet of the reaction chamber 9. When the hydrogen production unit malfunctions, the first pressure relief valve 15, the second pressure relief valve 26, and the third pressure relief valve 35 can promptly release pressure, and the alarm 36 will generate sound and light prompts to actively inform the staff. At this time, the hydrogen production unit malfunctions, and the first temperature sensor 16, the second temperature sensor 21, the third temperature sensor 30, the first pressure sensor 13, the second pressure sensor 17, the third pressure sensor 22, and the fourth pressure sensor 32... The output terminals are electrically connected to the input terminals of the controller 28, and the output terminals of the controller 28 are electrically connected to the input terminals of the first electric ball valve 12, the second electric ball valve 18, the third electric ball valve 23, the fourth electric ball valve 25, the fifth electric ball valve 27, the sixth electric ball valve 31, the seventh electric ball valve 34, the positive relay 6, the negative relay 7, and the alarm 36, respectively. When the hydrogen production unit is working, the first temperature sensor 16, the second temperature sensor 21, the third temperature sensor 30, the first pressure sensor 13, the second pressure sensor 17, the third pressure sensor 22, and the fourth pressure sensor 32 will transmit information to the controller 28 in real time. The controller 28 controls the on / off state of each of the first electric ball valve 12, the second electric ball valve 18, the third electric ball valve 23, the fourth electric ball valve 25, the fifth electric ball valve 27, the sixth electric ball valve 31, the seventh electric ball valve 34, the positive relay 6, and the negative relay 7 according to the information.
[0039] To facilitate the stratification of the mixed hydrogen and oxygen, a first temperature sensor 16 and a second pressure sensor 17 are respectively installed at the bottom of the inner wall of the gas collecting chamber 14. A first pressure relief valve 15 is installed at the top of the gas collecting chamber 14. The gas outlet of the gas collecting chamber 14 is connected to a first density stratification tower 24 and a second density stratification tower 33 through pipes. A second electric ball valve 18 is installed at the inlet of the first density stratification tower 24. The two gas outlets of the gas collecting chamber 14 respectively transport hydrogen and oxygen to the inside of the first density stratification tower 24 and the second density stratification tower 33 through pipes. The hydrogen and oxygen have different densities inside the first density stratification tower 24 and the second density stratification tower 33. The hydrogen and oxygen will complete the stratification process in the first density stratification tower 24 and the second density stratification tower 33, with hydrogen on top and oxygen on the bottom. A second pressure sensor 17 is installed on the inner wall of the first density stratification tower 24. Temperature sensor 21 and third pressure sensor 22 are installed. A third electric ball valve 23 is installed at the oxygen outlet of the first density stratification tower 24. A fourth electric ball valve 25 is installed at the hydrogen outlet of the first density stratification tower 24. A second pressure relief valve 26 is installed on one side of the top of the first density stratification tower 24. A fifth electric ball valve 27 is installed at the gas inlet of the second density stratification tower 33. A third temperature sensor 30 and a fourth pressure sensor 32 are installed on the inner wall of the second density stratification tower 33. A sixth electric ball valve 31 is installed at the oxygen outlet of the second density stratification tower 33. A seventh electric ball valve 34 is installed at the hydrogen outlet of the second density stratification tower 33. A third pressure relief valve 35 is installed on one side of the top of the second density stratification tower 33. The gas outlets of the third electric ball valve 23 and the sixth electric ball valve 31 supply oxygen to the outside, and the gas outlets of the fourth electric ball valve 25 and the seventh electric ball valve 34 supply hydrogen to the outside.
[0040] The first temperature sensor 16, the second temperature sensor 21, and the third temperature sensor 30 are all model: temperature and humidity sensor RS485 acquisition module;
[0041] The first pressure sensor 13, the second pressure sensor 17, the third pressure sensor 22, and the fourth pressure sensor 32 are all of the following model: pressure sensor RS485 acquisition module;
[0042] The model of controller 28 is: PLC200smart;
[0043] The first electric ball valve 12, the second electric ball valve 18, the third electric ball valve 23, the fourth electric ball valve 25, the fifth electric ball valve 27, the sixth electric ball valve 31, and the seventh electric ball valve 34 are all of the following model: DN40.
[0044] Working principle: First, prepare the composite electrode 8. Take multiple positive electrodes 19, negative electrodes 20, and a porous insulating layer 4. Place the porous insulating layer 4 between the positive electrodes 19 and negative electrodes 20. Encapsulate the multiple positive electrodes 19, porous insulating layer 4, and negative electrodes 20 together to obtain the composite electrode 8. Connect the multiple positive electrodes 19 to the positive relay 6 and positive terminal 3, and connect the multiple negative electrodes 20 to the negative terminal 5 and negative relay 7. Add 500ml of sodium hydroxide aqueous solution and distilled water to the mixing chamber 11 inside the reaction chamber 9 through the feeding pipe 10. Control the positive relay 6 and negative relay 7 to energize the positive electrodes 19 and negative electrodes 20 through the controller 28. After electrode 20 is connected to the electrolyte in the water, an oxidation reaction occurs at the positive electrode, where water molecules lose electrons and produce oxygen. A reduction reaction occurs at the negative electrode, where water molecules gain electrons and produce hydrogen. Through this reaction, water electrolysis produces oxygen and hydrogen. The resulting mixture of hydrogen and oxygen is transported to the inside of the gas collecting chamber 14 through a pipe. Because the porous insulating layer 4 between the positive electrode 19 and the negative electrode 20 is very thin, only a very low DC voltage is needed to successfully electrolyze the electrolyte between the positive electrode 19 and the negative electrode 20, decomposing water molecules (H2O) into oxygen (O2) and hydrogen (H2) through electrolysis. An electrolyte, sodium hydroxide aqueous solution, is added to the water to enhance the conductivity of the electrolyte.
[0045] The two outlets of the gas collecting chamber 14 respectively transport hydrogen and oxygen to the inside of the first density stratification tower 24 and the second density stratification tower 33 through pipelines. Since the hydrogen and oxygen have different densities inside the first density stratification tower 24 and the second density stratification tower 33, they undergo a stratification process, with hydrogen on top and oxygen at the bottom. At this time, the outlets of the third electric ball valve 23 and the sixth electric ball valve 31 supply oxygen to the outside, while the outlets of the fourth electric ball valve 25 and the seventh electric ball valve 34 supply hydrogen to the outside. When the hydrogen production device is working, the first temperature sensor 16, the second temperature sensor 21, the third temperature sensor 30, and the first pressure sensor... Sensors 13, 17, 22, and 32 transmit information to controller 28 in real time. Controller 28 controls the opening and closing of each of the following electric ball valves: 12, 18, 23, 25, 27, 31, 34, 6, 7, 8, 8, 9, 10, 11, 12, 13, 25, 27, 31, 34, 6, and 7. When a malfunction occurs in the hydrogen production unit, the first pressure relief valve 15, 26, and 35 can release pressure in a timely manner. At the same time, alarm 36 generates sound and light prompts to actively inform the staff that a malfunction has occurred in the hydrogen production unit.
[0046] In summary, the composite electrode 8 employs a special design with positive and negative electrodes and a porous insulating layer 4, enabling the hydrogen production device to perform water electrolysis at low voltage to produce hydrogen and oxygen. This design improves electrolysis efficiency, reduces energy consumption, and significantly lowers the cost of hydrogen development and utilization, paving the way for large-scale hydrogen development and utilization in the future. Simultaneously, through the first density stratification tower 24 and the second density stratification tower 33, hydrogen and oxygen can undergo a stratification process internally, with hydrogen on top and oxygen at the bottom, facilitating subsequent transportation and use and improving gas separation efficiency. Multiple temperature and pressure sensors are also installed to monitor the equipment's operating status in real time and transmit the information to the controller 28. The controller 28 controls the opening and closing of each electric ball valve based on the information, ensuring stable operation of the equipment. When a malfunction occurs in the hydrogen production device, the first pressure relief valve 15, the second pressure relief valve, and the third pressure relief valve 35 can promptly release pressure, improving equipment safety.
[0047] The present invention also provides a production method for a novel hydrogen production device, comprising the following steps:
[0048] S1. Fabrication of composite electrode 8: Take multiple positive electrodes 19, negative electrodes 20 and porous insulating layer 4, place the porous insulating layer 4 between the positive electrodes 19 and negative electrodes 20, and encapsulate the multiple positive electrodes 19, porous insulating layer 4 and negative electrodes 20 together to obtain composite electrode 8. Connect the multiple positive electrodes 19 to positive relay 6 and positive terminal 3, and connect the multiple negative electrodes 20 to negative terminal 5 and negative relay 7.
[0049] S2. Feeding and energizing: Sodium hydroxide aqueous solution and distilled water are added to the mixing chamber 11 inside the reaction chamber 9 through the feeding pipe 10. The mixing concentration ratio of sodium hydroxide aqueous solution and distilled water is 1:200. The positive relay 6 and negative relay 7 are controlled by the controller 28 to energize the positive electrode 19 and negative electrode 20, with a voltage of about 1.2 volts.
[0050] S3. After the positive electrode 19 and negative electrode 20 are connected to the electrolyte in the water, a direct current is applied. An oxidation reaction occurs at the positive electrode, where water molecules lose electrons to produce oxygen. A reduction reaction occurs at the negative electrode, where water molecules gain electrons to produce hydrogen. Through this reaction, water electrolysis produces oxygen and hydrogen. The resulting hydrogen and oxygen mixture is transported through a pipeline to the inside of the gas collecting chamber 14. The two outlets of the gas collecting chamber 14 respectively transport hydrogen and oxygen to the inside of the first density stratification tower 24 and the second density stratification tower 33 through pipelines. The hydrogen and oxygen have different densities inside the first density stratification tower 24 and the second density stratification tower 33. Hydrogen and oxygen will complete the stratification process in the first density stratification tower 24 and the second density stratification tower 33, with hydrogen on top and oxygen at the bottom. At this time, the outlets of the third electric ball valve 23 and the sixth electric ball valve 31 supply oxygen to the outside, and the outlets of the fourth electric ball valve 25 and the seventh electric ball valve 34 supply hydrogen to the outside.
[0051] The embodiments of the present invention have been described in detail above with reference to the accompanying drawings. It should be noted that implementations not illustrated or described in the drawings or the main text of the specification are forms known to those skilled in the art and are not described in detail. Furthermore, the definitions of the components described above are not limited to the various specific structures, shapes, or methods mentioned in the embodiments, and those skilled in the art can easily modify or substitute them.
[0052] Those skilled in the art will understand that the features described in the various embodiments and / or claims of the present invention can be combined or combined in various ways, even if such combinations or combinations are not explicitly described in the present invention. In particular, the features described in the various embodiments and / or claims of the present invention can be combined or combined in various ways without departing from the spirit and teachings of the present invention. All such combinations and / or combinations fall within the scope of the present invention.
[0053] The specific embodiments described above further illustrate the purpose, technical solution, and beneficial effects of the present invention. It should be understood that the above descriptions are merely specific embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of the present invention should be included within the protection scope of the present invention.
Claims
1. A novel hydrogen production device, comprising a base (1), characterized in that: A reaction chamber (9) is installed on the top of the base (1), and a support frame (2) is installed on the bottom of the base (1). A gas collection chamber (14) for mixing hydrogen and oxygen is provided on one side of the reaction chamber (9). A first density stratification tower (24) and a second density stratification tower (33) for settling the hydrogen and oxygen mixture are respectively provided on one side of the gas collection chamber (14). A composite electrode (8) is installed on the bottom of the inner wall of the reaction chamber (9). The composite electrode (8) includes a positive terminal (3), a number of porous insulating layers (4), a negative terminal (5), a positive relay (6), a negative relay (7), a number of positive electrodes (19), and a number of negative electrodes (20). The output terminal of the positive terminal (3) is electrically connected to the input terminal of the positive relay (6). The output terminal of the positive relay (6) is electrically connected to the input terminals of the positive electrodes (19). The output terminal of the negative terminal (5) is electrically connected to the input terminal of the negative relay (7). The output terminal of the negative relay (7) is electrically connected to the input terminals of the negative electrodes (20). One side of the positive electrode (19) and the negative electrode (20) are respectively connected to both sides of the porous insulating layer (4).
2. A novel hydrogen production device according to claim 1, characterized by: A controller (28) is installed on one side of the base (1), and an alarm (36) is installed on one side of the base (1).
3. A novel hydrogen production device according to claim 1, characterized by: The composite electrode (8) is fixed with a fixing frame (29) on the outside. The thickness of the porous insulating layer (4) is 0.1-1mm. The composite electrode (8) can be configured as a single-panel, linear, or matrix structure according to actual needs. The material used for the composite electrode (8) can be carbon sheet, zinc sheet, copper sheet, silver sheet, platinum sheet, or stainless steel sheet. The thickness of the positive electrode (19) and the negative electrode (20) is 0.1-1mm.
4. A novel hydrogen production device according to claim 2, characterized by: A feeding pipe (10) is installed on the top of the outer side of the reaction chamber (9). The feeding pipe (10) can be opened and closed manually. A mixing chamber (11) is provided inside the reaction chamber (9). A first pressure sensor (13) is installed on the top of the inner wall of the mixing chamber (11).
5. A novel hydrogen production device according to claim 4, characterized by: The top of the reaction chamber (9) is connected to the air inlet of the gas collection chamber (14) via a pipe, and the air outlet of the reaction chamber (9) is equipped with a first electric ball valve (12).
6. A novel hydrogen production device according to claim 5, characterized by: The bottom of the inner wall of the gas collecting chamber (14) is equipped with a first temperature sensor (16) and a second pressure sensor (17). The top of the gas collecting chamber (14) is equipped with a first pressure relief valve (15). The gas outlet of the gas collecting chamber (14) is connected to the first density stratification tower (24) and the second density stratification tower (33) through pipes.
7. A novel hydrogen production device according to claim 6, characterized by: The first density stratification tower (24) is equipped with a second electric ball valve (18) at the gas inlet end, a second temperature sensor (21) and a third pressure sensor (22) are respectively installed on the inner wall of the first density stratification tower (24), a third electric ball valve (23) is installed at the oxygen outlet end of the first density stratification tower (24), a fourth electric ball valve (25) is installed at the hydrogen outlet end of the first density stratification tower (24), and a second pressure relief valve (26) is installed on one side of the top of the first density stratification tower (24).
8. A novel hydrogen production device according to claim 7, characterized by: The second density stratification tower (33) is equipped with a fifth electric ball valve (27) at the gas inlet end, a third temperature sensor (30) and a fourth pressure sensor (32) are respectively installed on the inner wall of the second density stratification tower (33), a sixth electric ball valve (31) is installed at the oxygen outlet end of the second density stratification tower (33), a seventh electric ball valve (34) is installed at the hydrogen outlet end of the second density stratification tower (33), and a third pressure relief valve (35) is installed on one side of the top of the second density stratification tower (33).
9. A novel hydrogen production device according to claim 8, characterized by: The output terminals of the first temperature sensor (16), the second temperature sensor (21), the third temperature sensor (30), the first pressure sensor (13), the second pressure sensor (17), the third pressure sensor (22), and the fourth pressure sensor (32) are electrically connected to the input terminal of the controller (28). The output terminal of the controller (28) is electrically connected to the input terminal of the first electric ball valve (12), the second electric ball valve (18), the third electric ball valve (23), the fourth electric ball valve (25), the fifth electric ball valve (27), the sixth electric ball valve (31), the seventh electric ball valve (34), the positive relay (6), the negative relay (7), and the alarm (36).
10. A production method of the novel hydrogen production apparatus according to any one of claims 1 to 9, characterized by: Includes the following steps: S1. Fabrication of composite electrode (8): Take multiple positive electrodes (19), negative electrodes (20) and porous insulating layer (4), place the porous insulating layer (4) between the positive electrodes (19) and negative electrodes (20), and encapsulate multiple positive electrodes (19), porous insulating layer (4) and negative electrodes (20) together to obtain composite electrode (8). Connect multiple positive electrodes (19) to positive relay (6) and positive terminal (3), and connect multiple negative electrodes (20) to negative terminal (5) and negative relay (7). S2. Adding and energizing: Add sodium hydroxide aqueous solution and distilled water to the mixing chamber (11) inside the reaction chamber (9) through the feeding pipe (10). The mixing concentration ratio of sodium hydroxide aqueous solution and distilled water is 1:10-1:
200. Control the positive relay (6) and negative relay (7) through the controller (28) to supply DC current to the positive electrode (19) and negative electrode (20). The voltage is 1.15-1.25 volts. S3. Hydrogen production: After the positive electrode (19) and negative electrode (20) are connected to the electrolyte in the water, direct current is applied. An oxidation reaction occurs at the positive electrode, where water molecules lose electrons and produce oxygen. A reduction reaction occurs at the negative electrode, where water molecules gain electrons and produce hydrogen. Through this reaction, water electrolysis produces oxygen and hydrogen. The resulting hydrogen and oxygen mixture is transported through a pipe to the inside of the gas collecting chamber (14). The two outlets of the gas collecting chamber (14) respectively transport hydrogen and oxygen to the first density stratification zone through pipes. Inside the first density stratification tower (24) and the second density stratification tower (33), the hydrogen and oxygen have different densities. The hydrogen and oxygen will complete the stratification process in the first density stratification tower (24) and the second density stratification tower (33), with hydrogen on top and oxygen on the bottom. At this time, the outlet of the third electric ball valve (23) and the sixth electric ball valve (31) supplies oxygen to the outside, and the outlet of the fourth electric ball valve (25) and the seventh electric ball valve (34) supplies hydrogen to the outside.