Apparatus for enhancing electron emission in active hydrogen production processes

Abstract

The application provides a device for enhancing electron release in an active hydrogen preparation process, and relates to the technical field of polar properties of polar materials, and comprises a water inlet spiral device, an inner threaded pipe, a water passing blade spiral device, an inner threaded pipe and a water outlet upper cover which are sequentially connected through a hoop assembly. The water inlet spiral device comprises an outer sleeve and an inner sleeve, the first end of the outer sleeve is connected with the first end of the inner sleeve, a water inlet is arranged on the side wall of the outer sleeve, the water inlet direction is parallel to the tangent line of the position corresponding to the outer sleeve, and the inner side wall of the outer sleeve is provided with first spiral blades. The water flow spirally rises from the water inlet and along the first spiral blades. In this way, vortex flow is formed when the water flow enters the water inlet spiral device. Meanwhile, the water passing blade spiral device is arranged to form strong spiral flow and increase the pressure, so as to solve the problems of the prior art, such as insignificant spiral flow intensity, insignificant vortex increase, limited rotational kinetic energy increase and limited pressure increase.

Description

Technical Field

[0001] This invention relates to the technical field of polar properties of polar materials, and in particular to a device for enhancing electron release during the preparation of active hydrogen. Background Technology

[0002] In existing technologies, although parameters such as rib height of 1-10mm, pitch of 2-20mm, and helix angle of 10-70° have been designed to manufacture inner rib tubes to increase the swirling effect, actual application results show that the swirling flow intensity generated by existing technology devices is not significant, and axial flow is still dominant, which leads to problems such as insignificant increase in vorticity, insignificant increase in rotational kinetic energy, and insignificant increase in pressure. Summary of the Invention

[0003] The purpose of this invention is to provide a device for enhancing electron release during the preparation of active hydrogen, thereby solving the technical problems of insignificant increases in vorticity, rotational kinetic energy, and pressure in existing technologies. The various technical effects of the preferred solutions among the many technical solutions provided by this invention are detailed below.

[0004] To achieve the above objectives, the present invention provides the following technical solution: This invention provides a device for enhancing electron release during the preparation of active hydrogen, comprising an inlet spiral, an internally threaded pipe, a water-passing blade spiral, and an outlet cover, all connectable by a clamp assembly. The internally threaded pipe is disposed between the inlet spiral, the water-passing blade spiral, between two adjacent water-passing blade spirals, and between the water-passing blade spiral and the outlet cover. The inlet spiral includes an outer sleeve and an inner sleeve, with the first end of the outer sleeve connected to the first end of the inner sleeve to form a closed structure. An inlet is provided on the side wall of the outer sleeve, with the water inlet direction parallel to the tangent at a corresponding position on the outer sleeve. A first spiral blade is provided on the inner side wall of the outer sleeve, allowing water to flow from the inlet and spiral upward along the first spiral blade. A drain is provided at the first end of the inlet spiral and is connected to the inner sleeve. The outlet cover is located on the top of the water-passing blade spiral.

[0005] Preferably, the water-passing blade auger includes a cylindrical outer cylinder, a mounting part, and a second auger blade, wherein the inner side of the second auger blade is mounted on the mounting part and the outer side is mounted on the cylindrical outer cylinder.

[0006] Preferably, the inner threaded tube is provided with a combination of materials with piezoelectric properties to form a material layer, and stainless steel filter screens are provided at the second end of the outer tube and at both the upper and lower ends of the water-passing blade spiral.

[0007] Preferably, the first end of the outer sleeve and the first end of the inner sleeve are provided with an annular connecting part, the major diameter of the annular connecting part is equal to the diameter of the outer sleeve and is connected to the first end of the outer sleeve, and the inner diameter of the annular connecting part is less than or equal to the diameter of the inner sleeve and is connected to the first end of the inner sleeve.

[0008] Preferably, the diameter ratio of the inner sleeve to the outer sleeve is 0.4-0.6.

[0009] Preferably, the width of the first helical blade is 2-10 mm.

[0010] Preferably, there are six internally threaded tubes and five water-passing blade spirals, arranged in the order of internally threaded tubes.

[0011] Preferably, the two ends of the internally threaded pipe, the two ends of the water-passing blade spiral, and the second end of the outer sleeve are provided with annular protrusions, the clamp assembly is installed on two adjacent annular protrusions, and a sealing gasket is provided between the two adjacent annular protrusions.

[0012] Preferably, the ratio of the diameter of the mounting portion to the diameter of the cylindrical outer cylinder is 0.3-0.7.

[0013] The technical solution provided in this application document has the following beneficial effects: This invention provides a device for enhancing electron release during the preparation of active hydrogen, comprising an inlet spiral, an internally threaded pipe, a water-passing blade spiral, and an outlet cover connected in sequence by a clamp assembly. The device includes six internally threaded pipes and five water-passing blade spirals, with the inlet spiral at the lowest point. The internally threaded pipes and water-passing blade spirals are arranged in a cyclical pattern above each other, with the internally threaded pipes at the highest point. The outlet cover is installed on top of the internally threaded pipes, thus forming the active hydrogen preparation device. Specifically, the inlet spiral device includes an outer sleeve and an inner sleeve. The first end of the outer sleeve is connected to the first end of the inner sleeve to form a closed structure. An inlet is provided on the side wall of the outer sleeve, and the water inlet's direction is parallel to the tangent at the corresponding position on the outer sleeve. A first spiral blade is provided on the inner side wall of the outer sleeve. Water flows from the inlet and spirals upward along the first spiral blade. That is, water enters from the inlet. Since the water inlet's direction is parallel to the tangent at the inlet position on the outer sleeve, This design allows water to enter by pressing against the sidewall. Guided by the first helical blades, the water forms a vortex along these blades, flowing upwards into the internal threaded pipe and the water-passing blade spiral. The first end of the inlet spiral has a drain outlet connected to the inner sleeve. Because the inner sleeve is located inside the outer sleeve, it forces the water to move only along the direction of the first helical blades. A switch valve is located outside the drain outlet, and it is generally closed. A water outlet cover is located at the top of the water-passing blade spiral. This tangential flow design of the inlet spiral has the advantage of concentrated spiral flow energy, effectively transferring energy. Furthermore, the water-passing blade spiral creates a high-intensity spiral flow at each spiral outlet, with the rotational kinetic energy reaching its maximum within 100mm-300mm of the outlet section. Within this range, the pressure gradually increases. Based on fundamental principles of fluid mechanics, this design addresses issues such as insignificant helical flow intensity, insignificant vortex increase, limited increase in rotational kinetic energy, and limited increase in pressure. Furthermore, it influences the piezoelectric ceramic composite material housed within the internally threaded tube connected to the rear end of the helical outlet, enhancing electron release performance and improving the efficiency of active hydrogen production.

[0014] Table 1 shows a comparison of the hydrogen detection data of the present invention and existing equipment after experiments.

[0015] Table 1: Active hydrogen detection data from two different devices Attached Figure Description

[0016] To more clearly illustrate the technical solutions in the embodiments of the present invention 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 the present invention. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0017] Figure 1 This is a schematic diagram of the overall structure of the device for enhancing electron release during the active hydrogen preparation process provided in Embodiment 1 of the present invention; Figure 2 This is a cross-sectional view of an inlet screw conveyor according to an exemplary embodiment; Figure 3 This is a top view of an inlet spiral device removing a filter screen, according to an exemplary embodiment; Figure 4 This is an exploded structural diagram of a water-passing blade auger according to an exemplary embodiment; Figure 5 This is a cloud map of the circumferential velocity distribution at the rear end section of the water-passing blade auger. Figure 6 This is a radial velocity distribution cloud map of the rear section of the water-passing blade auger; Figure 7 This is a cloud map of the axial velocity distribution at the rear end section of the water-passing blade auger. Figure 8 This is a pressure distribution cloud map of the rear section of the water-passing blade auger.

[0018] In the diagram: 1. Inlet spiral; 11. Outer sleeve; 12. Inner sleeve; 13. First spiral blade; 14. Annular connection; 15. Inlet; 16. Outlet; 2. Internally threaded pipe; 21. Material layer; 3. Water-passing blade spiral; 31. Cylindrical outer cylinder; 32. Mounting part; 33. Second spiral blade; 4. Outlet cover; 5. Annular protrusion; 6. Clamp assembly. Detailed Implementation

[0019] To make the objectives, technical solutions, and advantages of this invention clearer, the technical solutions of this invention will be described in detail below. Obviously, the described embodiments are merely some embodiments of this invention, and not all embodiments. Based on the embodiments of this invention, all other implementation methods obtained by those skilled in the art without creative effort are within the scope of protection of this invention.

[0020] This specific embodiment provides a device for enhancing electron release during the preparation of active hydrogen, which solves the technical problems of insignificant increase in vorticity, insignificant increase in rotational kinetic energy, and insignificant increase in pressure in the prior art.

[0021] Hereinafter, embodiments will be described with reference to the accompanying drawings. Furthermore, the embodiments shown below do not limit the scope of the invention as described in the claims. Additionally, the complete contents of the configurations represented in the embodiments below are not limited to those necessary for the solution of the invention described in the claims.

[0022] Reference Figures 1-8 This invention provides a device for enhancing electron release during the preparation of active hydrogen, comprising an inlet spiral 1, an internally threaded pipe 2, a water-passing blade spiral 3, and an outlet cover 4, which can be connected by a clamp assembly 6. The internally threaded pipe 1 is disposed between the inlet spiral 1 and the water-passing blade spiral 3, between two adjacent water-passing blade spiral 3, and between the water-passing blade spiral 3 and the outlet cover 4. In this embodiment, there are six internally threaded pipes 2 and five water-passing blade spiral 3, wherein the inlet spiral 1 is disposed at the lowest end, and the internally threaded pipe 2 and the water-passing blade spiral 3 are disposed sequentially above it, and the internally threaded pipe 2 and the water-passing blade spiral 3 are arranged in a cycle, with the internally threaded pipe 2 disposed at the highest end. The outlet cover 4 is installed on the top of the internally threaded pipe 2, thus forming an active hydrogen preparation device. Specifically, the water inlet spiral device 1 includes an outer sleeve 11 and an inner sleeve 12. The first end of the outer sleeve 11 is connected to the first end of the inner sleeve 12, so that one end of the outer sleeve 11 and the first end of the inner sleeve 12 form a closed structure. A water inlet 15 is provided on the side wall of the outer sleeve 11, and the water inlet direction of the water inlet 15 is parallel to the tangent of the corresponding position of the outer sleeve 11. A first spiral blade 13 is provided on the inner side wall of the outer sleeve 11, and the width of the first spiral blade 13 is 2-10 mm. The water flows from the water inlet 15 and spirals upward along the first spiral blade 13, that is, the water flows in from the water inlet 15. Since the water inlet direction is parallel to the tangent of the outer sleeve 12, the water inlet 11 is connected to the first sleeve 12. The inlet is positioned tangentially to allow water to flow in against the sidewall. Guided by the first helical blade 13, the water forms a vortex along the blade, then flows upwards into the internal threaded pipe and the water-passing blade spiral 3. The first end of the inlet spiral 1 has a drain outlet 16 connected to the inner sleeve 12. Because the inner sleeve 12 is located inside the outer sleeve 11, the water flow is forced to move only along the direction of the first helical blade. A switch valve is located outside the drain outlet 16, and it is generally closed. A water outlet cover 4 is located at the top of the water-passing blade spiral 3. This configuration creates a vortex as soon as the water enters the inlet spiral 1, facilitating water flow and addressing issues in existing technologies such as insignificant spiral flow intensity, insignificant vortex increase, limited increase in rotational kinetic energy, and limited increase in pressure. The advantage of the tangential inlet method of the inlet spiral 1 is the concentrated energy of the spiral flow, effectively achieving energy transfer.

[0023] Further optimization of the scheme: Since the energy of water flow decreases during the flow process, the effect of eddies will also decrease. In order to form a larger eddy when the water flows through the internally threaded pipe 2, the water-passing blade spiral device 3 includes a cylindrical outer cylinder 31, a mounting part 32, and a second spiral blade 33. The inner side of the second spiral blade 33 is mounted on the mounting part 32, and the outer side is mounted on the cylindrical outer cylinder 31. Thus, the second spiral blade 33 is set between the two internally threaded pipes 2. In order to facilitate the installation of the second spiral blade 33, the second spiral blade 33 is first installed on the mounting part 32, and then the second spiral blade 33 is installed on the cylindrical outer cylinder 31 by spot welding. The ratio of the diameter of the mounting part 32 to the diameter of the cylindrical outer cylinder 31 is 0.3-0.7. The water flows in a relatively small passage, increasing the flow velocity. At the same time, due to the setting of the second spiral blade 33, the energy of generating eddies is increased, which facilitates the movement of materials inside the internally threaded pipe 2.

[0024] Further optimization involves incorporating a piezoelectric material layer within the internally threaded tube 2. The height of this material layer is 0.3-0.35 times the height of the internally threaded tube 2. The piezoelectric material comprises composite piezoelectric ceramic balls and aluminum, nickel-aluminum, or other electrode metal strips. The material layer is formed by the stacking of particles. As water flows through the internally threaded tube 2, it enters the tube and undergoes a thorough swirling and frictional mixing process. In the presence of this spiral flow, some of the water's kinetic energy is converted into pressure energy, resulting in an increase in water pressure. Combined with the polarity of the piezoelectric ceramic composite, this enhances the electron release capability and improves the efficiency of active hydrogen production. To facilitate the placement of the material layer, stainless steel filter screens 7 are welded to the second end of the outer sleeve 11 and the upper and lower ends of the water-passing blade spiral device 3. The diameter of the mesh of the filter screen 77 is smaller than the diameter of the material combination with piezoelectric properties placed inside the inner threaded tube 2. Therefore, since the filter screens 7 are provided on the components connected to the upper and lower ends of the inner threaded tube 2, the material can be kept in the space of the inner threaded tube 2.

[0025] To further optimize the design, in order to facilitate the connection between the outer sleeve 11 and the inner sleeve 12, an annular connecting part 14 is provided at the first end of the outer sleeve 11 and the first end of the inner sleeve 12. The major diameter of the annular connecting part 14 is equal to the diameter of the outer sleeve 11 and is connected to the first end of the outer sleeve 11. The inner diameter of the annular connecting part 14 is less than or equal to the diameter of the inner sleeve 12 and is connected to the first end of the inner sleeve 12. In this way, the water flow can have enough space to form a vortex. The drain pipe 16 is installed at the position of the inner diameter of the annular connecting part 14.

[0026] To further optimize the design, in order to have enough space to form vortices while ensuring the size of the vortices, the diameter ratio of the inner sleeve 12 to the outer sleeve 11 is 0.4-0.6.

[0027] To further optimize the design, in order to facilitate the connection between two adjacent components, namely the connection between the inlet screw and the internal threaded pipe 2, and the connection between the internal threaded pipe 2 and the water-passing vane screw 3, annular protrusions 5 are provided on the outer periphery of both ends of the internal threaded pipe 2, both ends of the water-passing vane screw 3, and the second end of the outer sleeve 11. The clamp assembly 6 is installed on two adjacent annular protrusions 5 at the same time, and a sealing gasket is provided between the two adjacent annular protrusions 5. That is, a sealing gasket is provided between the end face of the inlet screw and the internal threaded pipe 2, and between the end face of the internal threaded pipe 2 and the water-passing vane screw 3, thereby ensuring the overall sealing performance.

[0028] Specifically, to illustrate the effect intuitively, the water flow, after being deflected circumferentially by the auger 3 with its impeller blades, forms a spiral flow with a large circumferential velocity. Since the auger 3 has a large influence range on the rear end and the circumferential velocity distribution is complex, to better understand the flow field distribution of the circumferential velocity at the rear end section of the auger 3 outlet, a simulation is performed using an auger 3 with a second helical blade height of 40mm and an inner diameter of 110mm. The circumferential velocity distribution of the spiral flow is analyzed at cross-sections 10mm, 50mm, 100mm, and 150mm from the rear end of the auger 3 outlet, given an inlet flow velocity of 40m. 3 / h.

[0029] The sign of the circumferential velocity is determined by the right-hand rule: the direction in which the thumb points is positive and the direction in which the four fingers point is positive, and vice versa (i.e., in the cross-sectional contour diagram, the counterclockwise direction is positive and the counterclockwise direction is negative); the radial velocity is positive in the direction toward the pipe wall and negative in the opposite direction; the axial velocity is positive along the pipe axis in the direction of water flow and negative in the opposite direction.

[0030] a) Explanation of the circumferential velocity of water flow in an internally threaded pipe To understand the flow field distribution of the circumferential velocity at the rear end section of the hydrocyclone, Figure 5 This is a contour map of the circumferential velocity distribution at the rear section of the hydrocyclone. Figure 5 It can be known that: (1) At the rear end of the outlet of the water-passing blade auger 3, there are three regions with positive and relatively large circumferential velocities near the wall of the internally threaded pipe 2. In particular, at the outlet section of the water-passing blade auger 3, the maximum circumferential velocity can reach 0.35 m / s. This shows that the second helical blade 33 plays a significant role in initiating the swirl, and there is a high-intensity helical flow at the rear end of the water-passing blade auger 3. The shape of the helical flow in the section of the internally threaded pipe 2 at the rear end changes significantly along the flow path, gradually changing from an initial fan shape to a long strip shape. This indicates that the constraint effect of the second helical blade 33 on the water flow at the rear end gradually weakens. In addition, the value of the counterclockwise circumferential velocity also decreases along the flow path, and the intensity of the helical flow decreases along the rear end.

[0031] (2) In the central area of ​​the pipeline, there are three regions with negative circumferential velocities, and the maximum circumferential velocity is about 0.16 m / s, which is much lower than the maximum positive circumferential velocity. The reason for the negative velocities is that at the position of the second spiral blade 33 inside the water-passing blade auger 3, the pressure on the water-facing side of the second spiral blade 33 is higher, and the pressure on the water-returning side of the second spiral blade 33 is lower. The water flow on the water-facing side of the second spiral blade 33 will flow along the outer edge of the second spiral blade 33 to the water-returning side of the second spiral blade 33. As a result, at the rear end of the water-passing blade auger 3, at the position corresponding to the outer edge of the second spiral blade 33 inside the water-passing blade auger 3, three regions with clockwise water flow velocities are also formed.

[0032] b) Explanation of the radial flow velocity of water in an internally threaded pipe When water flows through the water-passing blade auger 3 to form a spiral flow, it will flow between the pipe wall and the pipe axis, thereby generating a radial velocity. The radial velocity of the spiral flow at the rear end section of the water-passing blade auger will be analyzed below, still using the above structure as an example.

[0033] To understand the flow field distribution of radial velocity at the rear end section of a hydrocyclone, the distribution law of radial velocity of helical flow at its rear end section was studied. Figure 6 This is a contour map of the radial velocity distribution at the rear section of the hydrocyclone, from... Figure 6 It can be known that: (1) In the radial velocity distribution of the rear section of the water-passing blade auger 3, there are three regions with positive radial velocity and three regions with negative radial velocity. They appear in pairs on the cross section of the internally threaded pipe 2, with similar values, and are distributed at the same radius of the cross section. This is because there is flow around the second helical blade 33 inside the water-passing blade auger 3. The water flow on the water-facing side of the second helical blade 33 will flow towards the pipe axis, forming a region with negative radial velocity; after "flipping" through the outer edge of the second helical blade 33, it flows towards the back side of the second helical blade 33 towards the pipe wall, forming a region with positive radial velocity.

[0034] (2) As the cross section moves further away from the second helical blade 33, the water flow in the internally threaded pipe 2 is less affected by the flow around the second helical blade 33, and the radial velocity shows a more obvious decreasing trend along the cross section.

[0035] (3) From the distribution of radial velocity at each cross section of the water-passing blade spiral device 3, it can be found that the area of ​​radial velocity pointing towards the pipe wall is larger than the area pointing towards the pipe axis. This is because the water flow in the internally threaded pipe 2 rotates and there is centrifugal force, so the water flow as a whole tends to flow towards the pipe wall.

[0036] c) Explanation of the axial velocity of water flow in an internally threaded pipe When water flows through the water-passing blade auger 3 to form a spiral flow, the axial velocity will be redistributed. The axial velocity of the spiral flow at the rear end section of the water-passing blade auger 3 will be analyzed below.

[0037] To understand the flow field distribution of the axial velocity at the rear end of the turbine blade 3, the distribution of the axial velocity of the helical flow at its rear end is studied. Figure 7 This is a circumferential velocity distribution cloud map of the rear section of the water-passing blade propeller 3, from... Figure 7 It can be known that: (1) The axial velocity distribution at the rear end of the water-passing blade auger 3 is rotationally symmetrical about the axis of the internally threaded tube 2 at 120°. The overall distribution of axial velocity in the internally threaded tube 2 is similar to that of turbulent flow in a circular tube. The axial velocity is high and the velocity gradient is small near the axis of the internally threaded tube 2; while near the tube wall, the axial velocity drops sharply and the velocity gradient is large. This is mainly because the liquid has viscosity, and the internal friction shear stress near the tube wall is large, while the influence on the axial region of the internally threaded tube 2 is small.

[0038] (2) At the rear section of the water-passing blade spiral 3, there are three regions with very low axial velocity. This is caused by the obstruction of the second spiral blade 33. In addition, there is a wake vortex at the trailing edge of the second spiral blade 33, which also affects the distribution of axial velocity. The axial velocity in these three regions gradually increases along the pipe, and the increase in axial velocity is faster on the side of the pipe wall. The originally elongated region forms a closed shape near the pipe wall, and the shape tends to be circular. This is because the circumferential velocity is larger in the region near the pipe wall, and the replenishment speed of the water flow in the region originally blocked by the second spiral blade 33 is faster, so the axial velocity of the water flow in the region near the pipe wall increases accordingly.

[0039] d) Explanation of water pressure in internally threaded pipes After the water flow is deflected by the second helical blade 33 of the water-passing blade auger 3, its pressure distribution will change. The pressure characteristics of the helical flow at the rear section of the water-passing blade auger 3 are analyzed below.

[0040] To understand the flow field distribution of pressure at the rear end of the water-passing blade auger 3, we will take the water-passing blade auger 3 with a second helical blade 33 height of 40 mm as an example and study the distribution law of helical flow pressure at its rear end. Figure 8 This is a pressure distribution cloud map of the rear section of the water-passing blade auger 3, from... Figure 8 It can be known that: (1) At the outlet section of the water-passing blade spiral device 3, there are three regions with low pressure. Especially at the section with Z = 10 mm, the area of ​​the low pressure region is larger. As the spiral flow develops along the path, under the influence of water flow viscosity, the distribution of water flow pressure at each section gradually tends to be annular. The pressure of these three low pressure regions increases along the path and gradually connects into one region.

[0041] (2) Before the Z=150mm section, the pressure of each section of the pipe increases. This is because at the trailing edge of the second helical blade 33, the flow area of ​​the water increases, the average flow velocity of the water section decreases, and part of the kinetic energy of the water flow is converted into pressure energy, so the pressure of the water flow will increase.

[0042] It should be noted that the terms "center," "longitudinal," "lateral," "length," "width," "thickness," "upper," "lower," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," "clockwise," and "counterclockwise," etc., used herein to indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings, are only for the convenience of describing the invention 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, and therefore should not be construed as a limitation of the invention. Furthermore, the terms "first," "second," and "third," etc., are used for descriptive purposes only and should not be construed as indicating or implying relative importance.

[0043] In the description herein, it should also be noted that, unless otherwise explicitly specified and limited, the terms "installation," "connection," and "linking" should be interpreted broadly. For example, they can refer to fixed connections, detachable connections, or integral connections; they can refer to mechanical connections or electrical connections; they can refer to direct connections or indirect connections through an intermediate medium. Those skilled in the art can understand the specific meaning of the above terms in this invention according to the specific circumstances.

[0044] The above description is merely a specific embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Any variations or substitutions that can be easily conceived by those skilled in the art within the technical scope disclosed in the present invention should be included within the scope of protection of the present invention. Therefore, the scope of protection of the present invention should be determined by the scope of the claims.

[0045] It is understood that the same or similar parts in the above embodiments can be referred to each other, and the content not described in detail in some embodiments can be referred to the same or similar content in other embodiments. The multiple solutions provided in this application contain their own basic solutions, are independent of each other, and do not restrict each other, but they can also be combined with each other without conflict to achieve multiple effects.

[0046] Although embodiments of this application have been shown and described above, it is understood that the above embodiments are exemplary and should not be construed as limiting this application. Those skilled in the art can make changes, modifications, substitutions and variations to the above embodiments within the scope of this application.

Claims

1. A device for enhancing electron release during the preparation of active hydrogen, characterized in that, The system includes an inlet spiral (1), an internally threaded pipe (2), a water-passing vane spiral (3), and an outlet cover (4) that can be connected via a clamp assembly (6). There are six internally threaded pipes (2) and five water-passing vane spirals (3). The inlet spiral (1) is located at the lowest end, with the internally threaded pipe (2) and the water-passing vane spiral (3) arranged sequentially above it. The internally threaded pipe (2) and the water-passing vane spiral (3) are arranged in a cyclic arrangement, with the internally threaded pipe (2) located at the highest end. The outlet cover (4) is installed on top of the internally threaded pipe (2). The inlet spiral (1) includes an outer sleeve (11) and an inner sleeve (12). The first end of the outer sleeve (11) is connected to the first end of the inner sleeve (12) so that one end of the outer sleeve (11) and the first end of the inner sleeve (12) form a closed structure. A water inlet (15) is provided on the side wall of the outer sleeve (11). The water inlet (15) is parallel to the tangent at the corresponding position of the outer sleeve (11). A first spiral blade (13) is provided on the inner side wall of the outer sleeve (11). The water flows from the water inlet (15) and spirals upward along the first spiral blade (13). A drain outlet (16) is provided at the first end of the water inlet spiral device (1) and the drain outlet (16) is connected to the inner sleeve (12). The water-passing blade auger (3) includes a cylindrical outer cylinder (31), a mounting part (32), and a second auger blade (33), wherein the inner side of the second auger blade (33) is mounted on the mounting part (32), and the outer side is mounted on the cylindrical outer cylinder (31); The inner threaded tube (2) is provided with a combination of materials with piezoelectric properties to form a material layer, and the second end of the outer tube (11) and the upper and lower ends of the water-passing blade spiral (3) are provided with stainless steel filter screens.

2. The apparatus for enhancing electron release during the preparation of active hydrogen according to claim 1, characterized in that, The first end of the outer sleeve (11) and the first end of the inner sleeve (12) are provided with an annular connecting part (14). The major diameter of the annular connecting part (14) is equal to the diameter of the outer sleeve (11) and is connected to the first end of the outer sleeve (11). The inner diameter of the annular connecting part (14) is less than or equal to the diameter of the inner sleeve (12) and is connected to the first end of the inner sleeve (12).

3. The apparatus for enhancing electron release during the preparation of active hydrogen according to claim 2, characterized in that, The diameter ratio of the inner sleeve (12) to the outer sleeve (11) is 0.4-0.

6.

4. The apparatus for enhancing electron release during the preparation of active hydrogen according to claim 1, characterized in that, The width of the first helical blade (13) is 2-10 mm.

5. The apparatus for enhancing electron release during the preparation of active hydrogen according to claim 1, characterized in that, The two ends of the internal threaded pipe (2), the two ends of the water-passing blade spiral (3), and the second end of the outer sleeve (11) are provided with annular protrusions (5). The clamp assembly (6) is installed on two adjacent annular protrusions (5) at the same time, and a sealing gasket is provided between the two adjacent annular protrusions (5).

6. The apparatus for enhancing electron release during the preparation of active hydrogen according to claim 1, characterized in that, The ratio of the diameter of the mounting part (32) to the diameter of the cylindrical outer cylinder (31) is 0.3-0.7.

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