A portable electrolytic product output device

Abstract

The application discloses a portable electrolysis product output device, which comprises a containing space provided with a driving agent and electrolysis raw water, and an output module in selective communication with the containing space, wherein the driving agent drives the electrolysis raw water to flow when the output module is in communication with the containing space; and the electrolysis device further comprises an electrolysis module arranged on the water outlet flow path of the electrolysis raw water when the output module is in communication with the containing space. The portable electrolysis product output device has the advantages that the electrolysis raw water is driven to flow by the driving agent, and the electrolysis module is arranged on the water outlet flow path of the electrolysis raw water, so that the continuous output of electrolysis products with sterilization capacity is realized, the miniaturization and convenience of the portable electrolysis product output device are considered, the application scenarios are wide, and the device is more user-friendly.

Description

Technical Field

[0001] This application belongs to the field of disinfection technology and relates to an output device, specifically a portable electrolysis product output device. Background Technology

[0002] With rising living standards and increased health awareness, outdoor activities have become the primary choice for daily leisure for more and more families. However, outdoor activities inevitably involve contact with public facilities, insect bites, or accidental injuries; consequently, disinfection and sterilization have become an essential part of outdoor activities. Currently, common disinfection methods for outdoor activities include hand sanitizer and disinfectant wipes. However, hand sanitizers pose a safety hazard due to the high concentration of volatile alcohol, which may ignite upon contact with an open flame; while disinfectant wipes have limited sterilization effects and are disposable, which is not environmentally friendly.

[0003] Meanwhile, the anolyte generated during water electrolysis, due to its high redox potential, is often used for indoor disinfection and sterilization. If it could be applied to outdoor disinfection, it would not only have excellent sterilization effects, but also provide readily available electrolyzed water with disinfecting and sterilizing properties simply by adding water – an environmentally friendly and convenient solution. However, existing electrolysis equipment is typically bulky and inconvenient to carry, preventing this disinfection method from being widely adopted in outdoor settings.

[0004] To address the aforementioned issues, the applicant conducted relevant research. Among them, invention patent application 2024111702213 discloses an electrolysis assembly, including an electrolytic cell, an electrolysis chamber housing the electrolytic cell, and a control circuit board. The electrolysis chamber is formed by a liquid inlet chamber, an exhaust chamber, and an outlet pipe connected in sequence. A reciprocating extrusion device is connected to the exhaust chamber. When the reciprocating extrusion device is in a compression state, gas in the exhaust chamber is discharged, and the control circuit board controls the operation of the electrolytic cell. When the reciprocating extrusion device is in a rebound state, liquid is injected into the exhaust chamber through the liquid inlet chamber under air pressure. This invention patent application not only solves the problem of miniaturizing electrolysis product output equipment but also allows for reasonable control of the electrolysis timing, resulting in energy savings and extended electrolytic cell lifespan.

[0005] However, in the aforementioned technical solutions, users need to continuously press and reciprocate the squeezing device to achieve a continuous output of electrolytic products. This operation method inevitably leads to finger fatigue, which is unfriendly to users, especially the elderly and those who need disinfection. Therefore, how to achieve a portable device with simple and labor-saving operation for electrolytic product output is a technical problem that urgently needs to be solved in practical applications. Currently, there are no reports on solutions to the aforementioned problems. Utility Model Content

[0006] The technical problem to be solved by this application is to provide a portable electrolysis product output device. This portable electrolysis product output device drives the flow of electrolyzed raw water using a driving agent, and an electrolysis module is installed in the outlet flow path of the electrolyzed raw water. This not only achieves continuous output of electrolysis products with bactericidal capabilities, but also takes into account the miniaturization and convenience of the electrolysis product output device, making it more user-friendly.

[0007] This application provides the following technical solution:

[0008] A portable electrolysis product output device includes a containment space with a driving agent and electrolyzed raw water, and an output module that can be selectively connected to the containment space. When the output module is connected to the containment space, the driving agent drives the electrolyzed raw water to flow.

[0009] It also includes an electrolysis module, which is disposed on the outlet flow path of the electrolyzed raw water when the output module is connected to the containment space.

[0010] The portable electrolysis product output device described in this application uses a driving agent to drive the flow of electrolyzed raw water. That is, when the user presses the output module, the electrolyzed raw water continuously enters the electrolysis module under the action of the driving agent, and the output module continuously outputs electrolyzed products with bactericidal capabilities. Compared to existing technologies where users need to press repeatedly to achieve continuous output of electrolyzed products, the portable electrolysis product output device of this application combines miniaturization and convenience, and has more significant beneficial effects.

[0011] Furthermore, the electrolysis space within the electrolysis module is divided into a cathode chamber and an anode chamber by a first separator, the first separator being an ion channel for cations;

[0012] The inlet and outlet of the electrolysis space are both located on one side of the anode chamber.

[0013] To improve the redox potential of the output electrolysis products, existing technologies often output the cathode and anode products separately, using ion exchange membranes to distinguish the anode and cathode chambers. However, due to the selectivity of ion exchange membranes, taking cation exchange membranes as an example, even if the raw water entering the cathode chamber participates in electrolysis at the cathode, the generated hydroxide ions cannot pass through the cation exchange membrane. Therefore, in this structural configuration, some of the raw water entering the electrolysis space does not participate in electrolysis, but only serves to dissolve the electrolysis products and prevent the electrodes from drying out.

[0014] The electrolysis module used in this application places the water inlet only on one side of the anode chamber. By utilizing the water carried by ions during migration, it avoids dry burning during electrolysis, overcoming the technical bias of prior art which requires water inlets on both sides of the chamber. With this structure, most of the raw water for electrolysis can participate in electrolysis at the anode. Compared to prior art where water flow does not participate in electrolysis, the conversion ratio of electrolysis products to raw water inlet volume is significantly improved in this application.

[0015] Furthermore, the driving agent and the electrolyzed raw water are arranged in layers within the containment space, and the output module has an inlet pipe extending into the containment space, the inlet pipe extending in a direction away from the driving agent.

[0016] The water inlet of the electrolysis module is connected to the containment space, and the water outlet is located near the water inlet pipe;

[0017] Alternatively, the electrolysis module may be installed on the water inlet pipe.

[0018] To prevent the driving agent from being directly discharged through the output module during the expansion process, this application also includes a water inlet pipe within the containment space, extending in a direction away from the driving agent to the electrolytic raw water layer. Therefore, the driving agent is surrounded by the perimeter wall of the containment space and the electrolytic raw water. When pressure fluctuates within the containment space or the driving agent expands in volume, the expansion pressure can only be released by driving the electrolytic raw water, thus ensuring a continuous supply of the electrolytic raw water to the electrolysis module for electrolysis. The electrolysis products are ultimately discharged through the output module.

[0019] Furthermore, the cathode chamber is provided with a gas outlet communicating with the outside of the accommodating space, and the first partition is provided with a gas-blocking structure.

[0020] This application restricts hydrogen diffusion across the membrane into the anode chamber by setting a gas-blocking structure, reducing the unnecessary consumption of hydrogen in the anode products. Furthermore, by providing an additional gas outlet at the cathode chamber to release hydrogen, which diffuses into the external environment on its own, no additional user intervention is required. Therefore, this application achieves an increase in the redox potential of the output electrolysis products without increasing user operation steps, demonstrating significant beneficial effects.

[0021] Furthermore, a second partition is provided within the containing space, which divides the containing space into a first chamber and a second chamber. Electrolyzed raw water is provided in the first chamber, and a driving agent is provided in the second chamber.

[0022] The electrolysis module is located in the first chamber, with the inlet connected to the first chamber and the outlet connected to the output module.

[0023] When the output module is connected to the first chamber, the pressure in the second chamber is greater than that in the first chamber, so as to squeeze the electrolyzed raw water in the first chamber into the electrolysis module, and finally discharge it through the output module.

[0024] The containment space described in this application separates the driving agent from the electrolyzed raw water through a second separator, so that the driving agent can be only a gas with a large pressure. The gas can be non-flammable or more environmentally friendly to drive the electrolyzed raw water, thereby increasing the flexibility and selection space of the driving agent.

[0025] Furthermore, a first gap is provided between the first separator and the peripheral wall of the electrolysis module, and the cathode chamber is connected to the anode chamber through the first gap;

[0026] The first separator is equipped with a water-blocking structure.

[0027] By incorporating a water-blocking structure and placing the water inlet of the electrolysis module solely on one side of the anode chamber, the amount of water entering the cathode chamber is reduced. Due to the limited water volume, less hydrogen dissolves in the water within the cathode chamber, and the probability of gaseous hydrogen reacting with the liquid anode products when diffusing into the anode chamber through the first gap is low. Therefore, although this structure outputs electrolysis products in a mixed-flow manner, it still reduces the unnecessary consumption of anode products, ensuring a sufficient quantity of the required electrolysis products output, thereby guaranteeing the disinfection capability of the output electrolysis products.

[0028] Furthermore, the anode is disposed adjacent to the first separator, and the area of ​​the anode is smaller than the area of ​​the first separator;

[0029] A third gap is provided between the anode and the peripheral wall of the anode chamber, and / or a third gap is provided between the anode and the first partition;

[0030] The third gap is connected to the first gap.

[0031] Considering that the continuous accumulation of hydrogen in the cathode chamber may cause a significant impact on the first separator, causing it to expand towards the anode chamber, this application positions the anode and the first separator relatively close to each other to support the first separator and limit its expansion towards the anode chamber. Furthermore, it is necessary to ensure that the area of ​​the anode is smaller than the area of ​​the first separator so that hydrogen ions generated at the anode can pass through the first separator via the shortest path to the cathode to continue participating in electrolysis, reducing the electrolysis voltage required for ion migration. On the other hand, a third gap can also be provided between the anode and the first separator, and / or between the anode and the peripheral wall of the anode chamber, to achieve communication between the cathode chamber and the anode chamber, ensuring the smooth discharge of hydrogen generated at the cathode.

[0032] Furthermore, a second gap is provided between the cathode and the peripheral wall of the cathode chamber, and / or a second gap is provided between the cathode and the first partition;

[0033] The second gap is connected to the first gap.

[0034] The presence of a second gap between the cathode and the first separator indicates that the distance between them is close. Hydrogen ions generated at the anode enter the cathode chamber through the first separator and can directly participate in electrolysis at the cathode. Therefore, the electrolysis required to drive ion migration in this application requires a smaller voltage. On the other hand, when second gaps are provided between the cathode and the peripheral wall of the cathode chamber, and between the cathode and the first separator, the rate at which hydrogen diffuses into the anode chamber increases, reducing the impact on the first separator as its volume increases, and extending the service life of the first separator.

[0035] Furthermore, the electrolysis module described in this application, through the combination of the first gap, the second gap, and the third gap, enables the smooth diffusion of hydrogen from the cathode chamber to the anode chamber, and further improves the efficiency of the electrolysis reaction from a kinetic perspective.

[0036] Furthermore, the output module includes a water outlet pipe connected to the outside, a first transition cavity, and a second transition cavity connected to the receiving space, wherein the first transition cavity is disposed between the water outlet pipe and the second transition cavity;

[0037] The water outlet pipe is slidably connected to the first transition cavity. When the water inlet end of the water outlet pipe is in the first transition cavity, the water inlet end is blocked by the inner wall of the first transition cavity.

[0038] The inner diameter of the first transition cavity is smaller than the inner diameter of the second transition cavity.

[0039] Furthermore, the electrolysis module is located at the water outlet pipe;

[0040] The inlet and outlet of the anode chamber are both connected to the outlet pipe.

[0041] Since the electrolysis module is located at the water outlet pipe, it can employ a structure with an additional gas outlet in the cathode chamber, allowing hydrogen to diffuse into the external environment. Alternatively, the electrolysis module can utilize a combination of a first gap, a second gap, and a third gap to facilitate the smooth diffusion of hydrogen from the cathode chamber to the anode chamber.

[0042] The portable electrolysis product output device of this application shortens the distance between the outlet of the electrolysis module and the outside by setting the electrolysis module at the water outlet pipeline, reducing the unnecessary consumption of electrolysis products during transportation, and thus more fully ensuring the oxidation-reduction potential of the output electrolysis products to ensure their disinfection ability.

[0043] After adopting the above technical solution, this application has the following beneficial effects:

[0044] 1. The portable electrolysis product output device described in this application drives the flow of electrolyzed raw water through a driving agent and sets an electrolysis module in the outlet flow path of the electrolyzed raw water. While realizing the continuous output of electrolysis products with bactericidal ability, it also takes into account the miniaturization and convenience of the portable electrolysis product output device.

[0045] 2. The electrolysis module used in this application not only improves the conversion ratio of electrolysis products to influent water while avoiding dry burning, but also greatly improves the oxidation-reduction potential of the output electrolysis products; thus fully ensuring the sterilization capability of the portable electrolysis product output device of this application.

[0046] 3. The electrolysis module used in this application reduces the consumption of anode products by the cathode products by setting both the inlet and outlet in the anode chamber and providing a water-blocking structure and / or a gas-blocking structure on the first partition. This overcomes the technical prejudice of those skilled in the art that the cathode products and anode products must be separated to improve the oxidation-reduction potential, and achieves unexpected technical effects.

[0047] 4. The portable electrolysis product output device described in this application has multiple options for the structure and location of the electrolysis module, as well as the structure of the accommodating space. Different structures can be adopted according to different application scenarios, making it widely applicable. Attached Figure Description

[0048] The accompanying drawings, which are incorporated in and form part of this specification, illustrate embodiments consistent with this application and, together with the description, serve to explain the principles of this application.

[0049] 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, for those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0050] Figure 1 This is a cross-sectional view of a portable electrolysis product output device according to one embodiment of this application;

[0051] Figure 2 This is a schematic diagram of a portable electrolysis product output device in one embodiment of this application;

[0052] Figure 3 This is a cross-sectional view of a portable electrolysis product output device according to another embodiment of this application;

[0053] Figure 4This is a schematic diagram of an electrolysis module in one embodiment of this application;

[0054] Figure 5 This is a cross-sectional view of the electrolysis module in one embodiment of this application;

[0055] Figure 6 This is a cross-sectional view of the electrolysis module from another angle in one embodiment of this application;

[0056] Figure 7 This is a partially enlarged schematic diagram of Part A of this application.

[0057] Explanation of reference numerals in the attached figures:

[0058] 1. Receiving space; 101. First chamber; 102. Second chamber; 103. Water inlet pipe; 2. Output module; 201. Water outlet pipe; 202. Second transition chamber; 203. Reset module; 204. Water inlet end; 3. Electrolysis module; 301. Water inlet; 302. Water outlet; 303. Anode chamber; 304. Cathode chamber; 305. Anode; 306. Cathode; 307. First separator; 308. Gas outlet; 309. First gap; 310. Second gap; 311. Third gap; 312. Conductive component; 313. Diffuser hole. Detailed Implementation

[0059] To enable those skilled in the art to better understand the present application, the technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only some embodiments of the present application, and not all embodiments. Based on the embodiments in the present application, all other embodiments obtained by those of ordinary skill in the art without creative effort should fall within the scope of protection of the present application.

[0060] It should be noted that the terms "first," "second," etc., in the specification, claims, and accompanying drawings of this application are used to distinguish similar objects and are not necessarily used to describe a specific order or sequence. It should be understood that such data can be interchanged where appropriate so that the embodiments of this application described herein can be implemented in orders other than those illustrated or described herein. Furthermore, the terms "comprising" and "having," and any variations thereof, are intended to cover non-exclusive inclusion; for example, a process, method, system, product, or apparatus that comprises a series of steps or units is not necessarily limited to those steps or units explicitly listed, but may include other steps or units not explicitly listed or inherent to such processes, methods, products, or apparatus.

[0061] Existing miniaturized outdoor disinfection equipment requires users to press it repeatedly to ensure the continuous output of electrolytic products, which is not user-friendly, especially for the elderly and frail.

[0062] In view of this, such as Figure 1-7 As shown, this utility model provides a portable electrolytic product output device that can continuously output electrolytic products, so that users can use it outdoors.

[0063] The portable electrolysis product output device of this application includes a containment space 1 containing a driving agent and electrolyzed raw water, and an output module 2 optionally connected to it. When the output module 2 is connected to the containment space 1, the containment space 1, which was originally in a closed state, can be connected to the outside world through the output module 2, and its internal pressure changes accordingly; as the internal pressure of the containment space 1 changes, the driving agent drives the electrolyzed raw water to flow.

[0064] The output module 2 includes a water outlet pipe 201 connected to the outside, a first transition cavity, and a second transition cavity 202 connected to the receiving space 1. The first transition cavity is located between the water outlet pipe 201 and the second transition cavity 202, and the inner diameter of the first transition cavity is smaller than the inner diameter of the second transition cavity 202.

[0065] To enable selectable connection between the output module 2 and the receiving space 1, the water outlet pipe 201 and the first transition cavity are preferably slidably connected. When the user presses the output module 2, the water inlet end 204 of the water outlet pipe 201, which is located in the first transition cavity, gradually moves into the second transition cavity 202.

[0066] Specifically, the water inlet 204 located in the first transition chamber is blocked by the inner wall of the first transition chamber. At this time, the water outlet 201 is not connected to the second transition chamber 202, the accommodating space 1 is in a closed state, and the driving agent inside cannot generate driving force for electrolyzing the raw water.

[0067] When the user presses the output module 2, the water inlet 204 slides from the first transition cavity to the second transition cavity 202. Since the inner diameter of the second transition cavity 202 is larger than that of the first transition cavity, the water inlet 204, which was blocked by the inner wall of the first transition cavity, becomes open in the second transition cavity 202. At this time, the containing space is connected to the outside through the water outlet pipe 201, and the pressure inside changes accordingly. The driving agent generates driving force for electrolyzing the raw water.

[0068] Compared to devices that require repeated pressing by the user to output electrolytic products, in this application, the user only needs to keep the output module 2 pressed to keep the water inlet 204 of the water outlet pipe 201 in the second transition cavity 202, so that the driving agent can generate a continuous driving force on the electrolyzed raw water, so that it is output through the output module after participating in electrolysis.

[0069] When it is necessary to shut down the output of electrolytic products, the water inlet 204, which is located in the second transition chamber 202, needs to be retracted into the first transition chamber. As the inner wall of the first transition chamber re-blocks the water inlet 204, the containing space 1 becomes closed, and the output of electrolytic products stops.

[0070] To enable the water outlet pipe 201 to automatically return to its original position when the user releases their grip, this application also provides a reset module 203. One end of the reset module 203 is fixed in position, and the other end is connected to the water outlet pipe 201 and moves with the movement of the water outlet pipe 201.

[0071] Specifically, when the reset module 203 is located on the displacement path of the user press output module 2 and the water outlet pipe 201, it can be set as an elastic element such as a spring that generates force due to compression. In this case, the reset module 203 can be located in the second transition cavity 202.

[0072] Alternatively, when the water outlet pipe 201 moves away from the reset module 203 as the user presses, the reset module 203 can be set as an elastic element such as rubber that generates force due to stretching.

[0073] To facilitate user operation, the portable electrolysis product output device of this application is also equipped with a power supply module (not shown in the figure) corresponding to the electrolysis module 3. The power supply module can be rechargeable or a replaceable battery. However, considering the limited quantity of driving agent, the power supply module is preferably set to a battery to ensure its replacement flexibility and reduce user operating costs. The power supply module can be directly connected to the anode 305 and cathode 306, or it can be connected to the anode 305 and cathode 306 through the conductive component 312.

[0074] Example 1: Optimizing the internal structure of the containment space to achieve continuous driving of electrolyzed raw water.

[0075] like Figure 1 and Figure 2 As shown, in this embodiment, the interior of the containment space 1 is a single unit, with the driving agent and the electrolyzed raw water arranged in layers within the containment space 1. When the containment space 1 is connected to the outside, as the air pressure inside the containment space 1 changes, the driving agent changes from a liquid state to a larger gaseous state; and due to the limited space inside the containment space 1, as the volume of the driving agent increases, the electrolyzed raw water is squeezed into the electrolysis module 3 by the driving agent to participate in electrolysis, and is finally output through the output module 2.

[0076] To prevent the driving agent from being directly discharged through the output module 2 during the volume increase process, thus failing to drive the electrolyzed raw water, in this embodiment, the output module 2 extends into the containing space 1 with a water inlet pipe 103. The water inlet pipe 103 extends to the electrolyzed raw water layer in a direction away from the driving agent. That is, the driving agent is surrounded by the perimeter wall of the containing space 1 and the electrolyzed raw water. When its volume increases, it can only release the pressure of volume expansion by driving the electrolyzed raw water. The electrolyzed raw water then enters the electrolysis module 2 to participate in electrolysis under the action of the driving agent.

[0077] The driving agent can be a substance such as propane or butane that changes from a liquid to a gaseous state when pressure changes. On the other hand, although the driving agent and the raw water for electrolysis are in direct contact within the containment space 1 in this embodiment, such substances are relatively stable and do not react with the raw water for electrolysis.

[0078] To ensure that the output from output module 2 consists entirely of electrolytic products with disinfection capabilities, electrolysis module 3 needs to be positioned on the outlet flow path of the electrolytic raw water when the driving agent drives the electrolytic raw water to move. In this embodiment, electrolysis module 3 can be positioned within the accommodating space 1, near the inlet of water inlet pipe 103, or electrolysis module 3 can be directly positioned at water inlet pipe 103.

[0079] When the electrolysis module 3 is positioned at the end of the accommodating space 1 away from the driving agent, in order to reduce the consumption of the cathode product on the anode product and ensure the redox potential of the output electrolysis product, the electrolysis space in the electrolysis module 3 in this embodiment includes a cathode chamber 304 with a cathode 306 and an anode chamber 303 with an anode 305. The cathode chamber 304 and the anode chamber 303 are separated by a first separator 307.

[0080] Furthermore, in this embodiment, the water inlet 301 and water outlet 302 of the electrolysis space are both located at the anode chamber 303, and the gas outlet 308 is separately located at the cathode chamber 304.

[0081] It should be noted that in this structural form, the anode chamber 303 can be set open. Although there is no clear boundary between the inlet 301 and the outlet 302, the open part of the anode chamber 303 can realize the function of water intake, which is the inlet 301, and the part of the area near the inlet of the water inlet pipe 103 can realize the function of outputting electrolytic products, which is the outlet 302.

[0082] When the electrolysis module 3 is located at the water inlet pipe 103, its outer side is surrounded by the driving agent or the raw water for electrolysis. Even if a gas outlet 308 is provided, the raw water for electrolysis may still permeate into the cathode chamber 304 through the gas outlet 308. On the other hand, since the driving agent drives the raw water for electrolysis, the pressure is relatively high, which will also restrict the smooth discharge of electrolysis products in the cathode chamber 304. Therefore, the electrolysis module 3 at this location preferably does not have a gas outlet 304 in the cathode chamber 304. Correspondingly, a first gap 309 is provided between the first separator 307 and the peripheral wall of the electrolysis module 3, and the cathode chamber 304 is connected to the anode chamber 303 through the first gap 309. Compared with the cathode products being discharged through the gas outlet 304, the cathode products in this structure diffuse into the anode chamber 303 through the first gap and are finally discharged through the water outlet 302 of the anode chamber 303.

[0083] Example 2: Another structural form within the containment space to achieve continuous driving of the electrolyzed raw water.

[0084] In the above embodiments, the driving agent and the raw water for electrolysis are in direct contact within the containment space 1. Therefore, the type of driving agent needs to be restricted. It must change from a liquid to a gaseous state when the pressure decreases, and it must also avoid reacting with the raw water for electrolysis. The driving agent selected under the above constraints needs to be considered for its flammability. On the other hand, when using Freon-based compounds as the driving agent, it is also necessary to avoid environmental pollution.

[0085] like Figure 3 As shown, in this embodiment, the internal structure of the accommodating space 1 is further optimized. A second partition is provided in the accommodating space 1, which divides the accommodating space 1 into a first chamber 101 and a second chamber 102. The first chamber 101 is optionally connected to the output module 3 and contains electrolyzed raw water. The second chamber 102 contains a driving agent.

[0086] Since the electrolyzed raw water is separated from the driving agent by the second separator, the driving agent in this embodiment only needs to have a large pressure. When the first chamber 101 is connected to the outside, a pressure difference is generated, which can squeeze the electrolyzed raw water to the output module 2. Therefore, compressed air, nitrogen, carbon dioxide, or other gases can be directly selected.

[0087] The specific working principle is as follows:

[0088] When the user does not press the output module 2, the water inlet 204 of the water outlet pipe 201 is blocked by the inner wall of the first transition chamber, and the first chamber 101 is in a closed state.

[0089] When the user presses the output module 2, the water inlet 204 enters the second transition chamber 202, and the first chamber 101 is connected to the outside world through the output module 2. At this time, the pressure in the second chamber 102 is greater than the pressure in the first chamber 101. Under the action of the pressure difference, the high-pressure gas in the second chamber 102 compresses the volume of the first chamber 101, squeezing the electrolyzed raw water inside into the electrolysis module 3. After this part of the electrolyzed raw water participates in electrolysis, it is finally output through the output module 2.

[0090] In this embodiment, the electrolysis module 3 is disposed in the first chamber 101. The electrolysis space in the electrolysis module 3 includes a cathode chamber 304 with a cathode 306 disposed therein and an anode chamber 303 with an anode 305 disposed therein. The cathode chamber 304 and the anode chamber 303 are separated by a first separator 307.

[0091] In this embodiment, the inlet 301 and outlet 302 of the electrolysis space are both located at the anode chamber 303. The inlet 301 is connected to the first chamber 101, and the outlet 302 is connected to the output module 2.

[0092] On the other hand, in this embodiment, since the electrolysis module 3 is located inside the first chamber 101 and is surrounded by the raw water for electrolysis, even if a gas outlet 308 is provided in the cathode chamber 304, hydrogen cannot be discharged to the outside of the first chamber 101. Furthermore, the hydrogen discharged into the first chamber 101 may still participate in electrolysis again with the water flow, consuming the anode product. Therefore, in this embodiment, the first partition 307 of the electrolysis module 3 preferably has a first gap 309 between it and the peripheral wall of the electrolysis space. The cathode chamber 304 is connected to the anode chamber 303 through the first gap 309. Compared to the cathode product being discharged through the gas outlet 304, in this structural form, the cathode product diffuses into the anode chamber 303 through the first gap 309 and is finally discharged through the outlet 302 of the anode chamber 303.

[0093] Example 3: Optimizing the position of the electrolysis module to ensure the concentration of output electrolysis products.

[0094] like Figure 3 As shown, in this embodiment, the electrolysis module 3 is located at the outlet pipe 201 of the output module 2. Compared with the above embodiment, the electrolysis module 3 in this embodiment is closer to the output end of the output module 2, reducing the unnecessary consumption of electrolysis products during the transportation process.

[0095] Specifically, in this embodiment, the electrolysis space within the electrolysis module 3 includes a cathode chamber 304 with a cathode 306 and an anode chamber 303 with an anode 305. The cathode chamber 304 and the anode chamber 303 are separated by a first separator 307.

[0096] The inlet 301 and outlet 302 of the electrolysis space are both located at the anode chamber 303, and both the inlet 301 and outlet 302 are connected to the outlet pipe 201.

[0097] In this embodiment, the cathode chamber 304 is connected to the anode chamber 303 through the first gap 309, allowing the cathode products to diffuse into the anode chamber 303 through the first gap 309 and finally be discharged through the outlet 302 located in the anode chamber 303. However, under this structure, some hydrogen still enters the anode chamber 303 with the water flow, consuming the anode products. Therefore, to further improve the redox potential of the output electrolysis products, in this embodiment, the cathode chamber 304 is preferably provided with a gas outlet 308 communicating with the outside of the anode chamber 303 to output the cathode products generated during electrolysis and reduce their consumption of the anode products; correspondingly, to prevent the transmembrane diffusion of hydrogen at the cathode 306, the first separator 307 is preferably provided with a gas-blocking structure, so that hydrogen can only be discharged from the gas outlet 308.

[0098] To increase the contact area between the anode 305 and the water flow, in this embodiment, the anode 305 is preferably a closed or semi-closed enclosure structure for the electrolyzed raw water. Driven by the driving agent, the electrolyzed raw water in the containing space 1 enters the electrolysis module 3 at a relatively high flow rate; that is, the electrolyzed raw water enters the anode chamber 303 in a turbulent flow. Under the influence of the turbulent and irregular flow field, the electrolyzed raw water continuously impacts the anode 305, participating in electrolysis. Therefore, the electrolysis efficiency of the electrolysis module 3 can be guaranteed under this structure.

[0099] Correspondingly, the cathode chamber 304 is fitted outside the anode chamber 303, and several gas outlets 308 are opened on its outer side.

[0100] Example 4: Optimize the structure of the electrolysis module to improve the redox potential of the output electrolysis products.

[0101] like Figure 4-7 As shown, in this embodiment, the cathode chamber 304 of the electrolysis module 3 does not have a gas outlet 308.

[0102] Specifically, in this embodiment, the electrolysis space within the electrolysis module 3 includes a cathode chamber 304 with a cathode 306 and an anode chamber 303 with an anode 305. The cathode chamber 304 and the anode chamber 303 are separated by a first separator 307.

[0103] The inlet 301 and outlet 302 of the electrolysis module 3 are both located on one side of the anode chamber 303. Since the raw water undergoes electrolysis at the anode 305 first, the first separator 307 is correspondingly configured as an ion channel for cations and is equipped with a water-blocking structure.

[0104] During the electrolysis process, the raw water enters the anode chamber 303 through the inlet and participates in electrolysis at the anode 305. The generated hydrogen ions and other cations then enter the cathode chamber 304 through the first separator 307 and continue to participate in electrolysis at the cathode 306, generating cathode products such as hydrogen gas.

[0105] The specific reaction formula is as follows:

[0106] At 305°C (anode): 4H₂O - 4e - →O2↑+2H2O+4H + ;

[0107] At cathode 306: 2H + +2e - →H2↑;

[0108] Since no additional water inlet is provided at the cathode chamber 304, and the cathode chamber 304 and the anode chamber 303 are separated by the first partition 307, the water volume in the cathode chamber 304 is limited during the electrolysis process. To prevent the cathode 306 from burning out during electrolysis, a first gap 309 is provided between the first partition 307 and the peripheral wall of the electrolysis space in this invention. The cathode chamber 304 and the anode chamber 303 are connected through the first gap 309, allowing water from the anode chamber 303 to enter the cathode chamber 304 through the first gap 309. This water flow can prevent the cathode 306 from burning out.

[0109] The inventors unexpectedly discovered that although the cathode chamber 304 and the anode chamber 303 are connected through the first gap 309, and the cathode products can diffuse into the anode chamber 303 through the first gap 309, causing consumption of the anode products, the actual output oxidation-reduction potential of the electrolytic products of this invention is still improved compared with the mixed flow structure.

[0110] The inventors speculate that because the electrolysis module 3 of this invention does not have an additional water inlet in the cathode chamber 304, and the cathode chamber 304 and the anode chamber 303 are separated by the first separator 307, the amount of water in the cathode chamber 304 is limited during electrolysis. Due to the limited water volume, only a small portion of the hydrogen generated at the cathode 306 dissolves in the water and diffuses into the anode chamber 303 through the first gap 309 with the water flow, causing unnecessary consumption of the anode product; the majority of the remaining hydrogen diffuses into the anode chamber 303 in a gaseous state through the first gap 309. Compared with hydrogen dissolved in water, the probability of gaseous hydrogen reacting with the liquid anode product is smaller. Therefore, most of this hydrogen is directly discharged through the water outlet 302, thus resulting in a significant increase in the redox potential of the output electrolysis product even though this invention outputs the electrolysis product in a similar mixed-flow manner. In the mixed-flow structure, since the amount of water in the cathode chamber 304 is relatively large or can be replenished in time, most of the hydrogen generated at the cathode 306 dissolves in the water. The hydrogen dissolved in the water has a high probability of contacting the anode products, thus causing more consumption of the anode products and limiting the redox potential of the output electrolytic products.

[0111] On the other hand, after the gaseous hydrogen is discharged through the outlet 302 of the electrolysis module 3, it can diffuse into the external environment on its own without requiring additional treatment by the user. Therefore, this invention greatly improves the redox potential of the output electrolysis product without increasing the user's usage steps, achieving unexpected technical effects.

[0112] Furthermore, it should be noted that the first partition 307 with a water-blocking structure in this utility model can limit most of the water flow in the anode chamber 303 from diffusing into the cathode chamber 304. However, since the hydrogen ions and other cations generated at the anode 305 need to pass through the first partition 307 to enter the cathode chamber 304 and continue to participate in electrolysis, and water is required as a medium during the migration of ions, the first partition 307 can allow ions to carry some water through during the migration process. This water can also prevent the cathode 306 from burning dry during the electrolysis process.

[0113] The first separator 307 can function as a water barrier and allow cations to pass through. If the first separator 307 allows hydrogen to diffuse across the membrane, since the hydrogen generated during the electrolysis process exists in the form of hydrogen negative ions, and since hydrogen negative ions have an extra electron, they are more active and have a higher probability of diffusing into the anode chamber 303 and reacting with the anode products. Therefore, it may still cause unnecessary consumption of the anode products.

[0114] Therefore, in this embodiment, the first separator 307 is preferably also provided with a gas-blocking structure to restrict hydrogen gas from directly diffusing through the first separator 307 into the anode chamber 303.

[0115] Due to the gas-blocking structure, the hydrogen anions generated during electrolysis in this embodiment can only diffuse into the anode chamber 303 through the first gap 309. Because hydrogen anions are relatively active, they lose excess electrons during diffusion into the first gap 309, transforming into inactive hydrogen gas. Even if this hydrogen gas diffuses into the anode chamber 303, the probability of it reacting with the anode product is low. Therefore, by setting a gas-blocking structure on the first separator 307, the unnecessary consumption of anode products can be further reduced, thereby further improving the redox potential of the output electrolytic product. Specifically, under the same other electrolysis conditions, the redox potential of the output electrolytic product of this invention can be increased from 700mV in the mixed-flow form to 820mV.

[0116] Specifically, the first separator 307 may be a cation exchange membrane, a polytetrafluoroethylene (PTFE) composite membrane, a multilayer hydrophobic coating membrane, or other structural forms.

[0117] The working principle of the polytetrafluoroethylene composite membrane is to disperse the perfluorosulfonic acid membrane in the porous polytetrafluoroethylene framework, and to use the hydrophobicity and density of polytetrafluoroethylene to block various gases, including hydrogen.

[0118] The working principle of the multilayer hydrophobic coating membrane is to coat the surface of the cation exchange layer with an ultrathin polyvinylidene fluoride layer to block liquid water and gas from passing through.

[0119] Considering that cations such as hydrogen ions enter the cathode chamber 304 through the first separator 307 and continue to participate in electrolysis at the cathode 306, the closer the cathode 306 is to the first separator 307, the smaller the voltage required to drive ion migration. Therefore, the cathode 306 is preferably disposed in close contact with the first separator 307.

[0120] When the cathode 306 is installed in close contact with the first separator 307, a second gap 310 needs to be provided between the cathode 306 and the peripheral wall of the cathode chamber 304. The second gap 310 is connected to the first gap 309 to ensure that the hydrogen generated at the cathode 306 can enter the anode chamber 303 through the second gap 310 and the first gap 309, and be discharged through the outlet 302.

[0121] Alternatively, with the cathode 306 and the first separator 307 in close contact, the cathode 306 and the first separator 307 can be adjusted to be in a gap configuration, that is, a second gap 310 is still left between the cathode 306 and the first separator 307. In this case, the hydrogen gas generated at the cathode 306 can enter the anode chamber 303 through the second gap 310 and the first gap 309 between the cathode 306 and the first separator 307.

[0122] It should be noted that in this embodiment, there is a difference between gap setting and interval setting. Gap setting leaves a gap between the two while keeping them in close contact, and the size of the gap is small. Interval setting, on the other hand, makes the distance between the two more obvious.

[0123] Due to the limited size of the second gap 310, the rate at which hydrogen diffuses from the cathode chamber 304 to the anode chamber 303 is relatively slow. Hydrogen accumulates continuously in the cathode chamber 304, its volume increasing until it impacts the first separator 307, causing it to bulge out towards the anode chamber 303. Therefore, in this embodiment, it is preferable to provide second gaps 310 between the cathode 306 and the peripheral wall of the cathode chamber 304, and between the cathode 306 and the first separator 307, to ensure the diffusion rate of hydrogen and reduce its impact on the first separator 307.

[0124] Since hydrogen ions enter the cathode chamber 304 through the first separator 307, if the area of ​​the cathode 306 is equal to the area of ​​the first separator 307, the hydrogen ions only contact the cathode 306 on the side facing the first separator 307 and cannot be utilized on the other side of the cathode 306, resulting in low utilization of the cathode 306. Alternatively, when a second gap 310 is provided between the cathode 306 and the peripheral wall of the cathode chamber 304, although the cathode chambers 304 on both sides of the cathode 306 can be connected through the second gap 310, allowing water flow to participate in electrolysis at the cathode 306 on the side away from the first separator 307, the diffusion rate of hydrogen to the cathode chamber 304 on the other side of the cathode 306 is slow due to the size limitation of the second gap 310. Most of the hydrogen generated during electrolysis still accumulates between the first separator 307 and the cathode 306, causing a greater impact on the first separator 307.

[0125] Therefore, in this embodiment, the area of ​​the cathode 306 is preferably smaller than the area of ​​the first separator 307. For example, multiple cathodes 306 are spaced apart, or at least one diffusion hole 313 is provided through the cathode 306. In this case, hydrogen ions entering the cathode chamber 304 through the first separator 307 can enter the cathode chamber 304 on the other side of the cathode 306 through the gap between adjacent cathodes 306 or the diffusion hole 313, and participate in electrolysis at the cathode 306 on the side away from the first separator 307, thus utilizing the cathode 306 at this location. On the other hand, the cathode chamber 304 at this location can also be used to contain hydrogen gas that has not yet diffused into the anode chamber 303, so as to reduce the impact of hydrogen gas on the first separator 307 and extend the service life of the first separator 307.

[0126] Furthermore, compared to cathodes 306 with multiple spaced intervals, providing diffusion holes 313 on cathode 306 allows cathode 306 to remain as a single unit, resulting in better stability and easier assembly.

[0127] Furthermore, to limit the cathode 306 and create a gap between it and the first separator 307, a conductive element 312 is provided in the cathode chamber 304 in this embodiment. The conductive element 312 has a hollow frame structure to allow space for hydrogen gas. One side of the conductive element 312 is attached to the cathode 306, and the opposite side is attached to the inner wall of the cathode chamber 304 to support the cathode 306. The conductive element 312 extends to the outside of the electrolysis space with a terminal for connection to the power supply module.

[0128] In the above embodiment, the hydrogen generated at the cathode 306 can be output to the anode chamber 303 due to the second gap 310. However, due to the size limitations of the second gap 310 and the first gap 309, the output efficiency of the hydrogen is slow. Therefore, the hydrogen in the cathode chamber 304 will cause greater pressure on the first partition 307.

[0129] In this embodiment, the anode 305 needs to be closely attached to the first partition 307 so that the anode 305 can limit the first partition 307 from another direction. At this time, a third gap 311 needs to be provided between the anode 305 and the peripheral wall of the anode chamber 303, and the third gap 311 is connected to the first gap 309 so that the hydrogen in the cathode chamber 304 can diffuse into the anode chamber 303 and finally be discharged through the outlet 302.

[0130] And / or, in this embodiment, the anode 305 and the first separator 307 can be adjusted to be spaced apart while being tightly attached. A third gap 311 can be provided between them, and the third gap 311 is connected to the first gap 309. At this time, the anode 305 can still limit the first separator 307 from another direction, thereby offsetting the pressure of hydrogen on the first separator 307.

[0131] If the area of ​​the anode 305 is equal to the area of ​​the first separator 307, considering that the anode 305 needs to limit the first separator 307, the two are set close together or a third gap 311 is left. The water flow in the anode chamber 303 on the side away from the first separator 307 participates in electrolysis at the anode 305 to generate hydrogen ions. However, the generated hydrogen ions cannot pass through the first separator 307 due to the obstruction of the anode 305 and continue to participate in electrolysis at the cathode 306. They can only go around from the first gap 309 to the cathode 306 to continue to participate in electrolysis. As the ion migration path increases, the voltage required for electrolysis increases accordingly.

[0132] Therefore, in this embodiment, the area of ​​the anode 305 is preferably smaller than the area of ​​the first separator 307, so that the hydrogen ions generated at the anode 305 can pass through the first separator 307 and continue to participate in electrolysis at the cathode 306 along a shorter path.

[0133] For example, multiple anodes 305 can be provided, with adjacent anodes 305 spaced apart, or at least one diffusion hole 313 can be provided through the anode 305. Compared with multiple spaced anodes 305, providing a diffusion hole 313 on the anode 305 allows the anode 305 to remain a single unit, resulting in better stability and easier installation.

[0134] Furthermore, to limit the position of the anode 305, the electrolysis module 3 in this embodiment has a conductive element 312 with a frame structure on the side of the anode 305 away from the first separator 307. The conductive element 312 is hollow to accommodate the water flow participating in electrolysis. One side of the conductive element 312 abuts against the anode 305, and the opposite side abuts against the inner wall of the anode chamber 303 to support the anode 305. The conductive element 312 extends to the outside of the electrolysis space with a connecting end for connection to the power supply module.

[0135] Example 5: Further optimization of the electrolysis module structure

[0136] Although the above embodiments reduce the probability of hydrogen reacting with the anode products, some water-soluble hydrogen still diffuses into the anode chamber 303 through the first gap 309, causing consumption of the anode products.

[0137] In view of this, such as Figure 1 and Figure 2 As shown, in this embodiment, instead of the first gap 309 for hydrogen evacuation, a gas outlet 308 is provided at the cathode chamber 304, connecting the cathode chamber 304 to the outside of the anode chamber 303. By directly venting the hydrogen, the consumption of hydrogen for the anode products is further reduced. Correspondingly, to ensure that the hydrogen is vented through the gas outlet 308 and to prevent its transmembrane diffusion, the first separator 307 also needs to be provided with a gas-blocking structure to block the hydrogen.

[0138] The first separator 307 can be configured as an ultrafiltration membrane, a hydrophilic cation exchange membrane, a negatively charged nanofiltration membrane, or a mixed matrix membrane, etc., which allows water to flow through while blocking the diffusion of hydrogen generated at the cathode 306 across the membrane.

[0139] The hydrophilic cation membrane adsorbs water molecules through hydrophilic groups such as sulfonic acid groups to form a hydration layer, providing a transport channel for cations and water. Non-polar gas molecules are blocked because they cannot form hydrogen bonds or electrostatic interactions with the hydration layer, thus achieving the function of gas anti-reverse flow.

[0140] Negatively charged nanofiltration membranes have a negatively charged surface, and their pore size can block gases while allowing cations and water to pass through. By incorporating hydrophilic groups, a dynamic hydration layer can be formed, enhancing water transport. Gases, due to their hydrophobicity, nonpolarity, and low solubility, are trapped, thus achieving a gas anti-reverse function.

[0141] The hybrid matrix membrane uses organic polymers as the matrix and inorganic nanomaterials such as zeolite and metal-organic frameworks (MOFs) are uniformly dispersed inside. The surface charge and hydrophilicity of the materials can promote the transport of cations and water, and the gas anti-reverse function can be achieved by controlling the pore size distribution.

[0142] Furthermore, to prevent the remaining reducing substances in the cathode products from diffusing into the anode chamber 303 with the water flow, the first separator 307 is preferably provided with a water-blocking structure. It should be noted that while the first separator 307 in this invention can limit the diffusion of most of the water flow from the anode chamber 303 into the cathode chamber 304, since cations such as hydrogen ions generated at the anode 305 need to pass through the first separator 307 to enter the cathode chamber 304 and continue participating in electrolysis, and water is required as a medium during ion migration, the first separator 307 can allow ions to carry some water through during migration. This water can also prevent the cathode 306 from drying out during electrolysis.

[0143] Specifically, the first separator 307 can be configured as a cation exchange membrane, a hydrophobic MOF (metal-organic framework) membrane, a hydrophobic COF (covalent organic framework) membrane, or a hydrophobic mixed matrix membrane. This configuration allows hydrogen ions to carry some water into the cathode chamber 304, preventing the cathode 306 from burning dry, while also preventing the cathode products from consuming the anode products. The cation exchange membrane is preferably a proton exchange membrane.

[0144] Hydrophobic MOF and COF membranes form low surface energy interfaces by introducing hydrophobic functional groups such as fluorinated groups, which block the permeation of polar water molecules and gases; their pore surfaces are modified with negatively charged groups to promote cation migration.

[0145] The hydrophobic hybrid matrix membrane uses hydrophobic polymers such as polyvinylidene fluoride as the matrix and embeds hydrophilic inorganic nanoparticles such as zeolite and sulfonated carbon nanotubes. It forms a continuous ion transport channel through hydrophilic fillers, allowing cations and their hydrated ions to pass through, while preventing gas diffusion across the membrane through the hydrophobic matrix.

[0146] When all other electrolysis conditions are the same, the redox potential of the output electrolysis product in this embodiment can be increased from 820mV in the above embodiment to more than 1000mV.

[0147] As hydrogen ions carry water into the cathode chamber 304, to prevent water from overflowing from the gas outlet 308, a gas-liquid separation unit such as a polytetrafluoroethylene membrane can be installed at the gas outlet 308. This ensures that the gas outlet 308 only outputs hydrogen gas, while the water is trapped in this chamber. As the chamber fills with water, the electrolysis reaction can still proceed normally. When hydrogen ions carry water into this chamber, the original water flow in the chamber flows back to the anode 305 to participate in electrolysis. Therefore, in this embodiment, most of the water flow can participate in electrolysis at the anode 305.

[0148] In existing electrolysis modules, to ensure the redox potential of the output electrolysis products, separate cathode and anode products are output. In this structure, to prevent electrode dry-burning, inlets and outlets are provided in both chambers. However, due to the selectivity of ion exchange membranes (taking cation exchange membranes as an example), even if the raw water entering the cathode chamber participates in electrolysis at the cathode, the generated hydroxide ions cannot pass through the cation exchange membrane. Therefore, in this structure, a portion of the raw water entering the electrolysis space does not participate in electrolysis; it only dissolves the electrolysis products and prevents electrode dry-burning in this area. This portion of the raw water that does not participate in electrolysis results in a low inflow rate of both electrolysis products and raw water.

[0149] Compared with the traditional diversion method, in this application, most of the raw water entering the electrolysis space can participate in electrolysis at the anode chamber 303, and the conversion ratio of the required electrolysis products to the actual influent is significantly improved.

[0150] The electrodes in this application may be made of conductive diamond or other conductive materials, such as one or a combination of ceramic, titanium, platinum, gold, titanium alloy, nickel foam, palladium, platinum-ruthenium alloy or stainless steel.

[0151] In existing technologies, electrodes used for electrolysis often employ precious metals such as platinum and ruthenium-iridium. However, the limited availability of precious metal resources restricts the development prospects of this type of electrolysis. This application utilizes electrodes made of conductive diamond, reducing the electrolysis module's dependence on precious metal resources. Furthermore, since carbon resources for preparing conductive diamond are more abundant, this application has better development prospects.

[0152] The portable electrolytic product output device of this application can be used for disinfection during outdoor activities, as well as for application in scenarios such as nasal spray, oral spray, and tonsil spray. For example, when using the portable electrolytic product output device of this application to spray the oral cavity, the strong oxidizing ability of the electrolytic product can be used to decompose odor molecules in the oral cavity, ensuring fresh breath; when spraying the nose and tonsils, the electrolytic product can be used to reduce inflammation in the nose and tonsils.

[0153] The above are merely preferred embodiments of this application. It should be noted that those skilled in the art can make various improvements and modifications without departing from the principles of this application, and these improvements and modifications should also be considered within the scope of protection of this application.

Claims

1. A portable electrolysis product output device, characterized in that, It includes a container space containing a driving agent and electrolyzed raw water, and an output module that can be selectively connected to it. When the output module is connected to the container space, the driving agent drives the electrolyzed raw water to flow. It also includes an electrolysis module, which is disposed on the outlet flow path of the electrolyzed raw water when the output module is connected to the containment space.

2. The portable electrolysis product output device according to claim 1, characterized in that, The electrolysis space within the electrolysis module is divided into a cathode chamber and an anode chamber by a first separator, which is an ion channel for cations. The inlet and outlet of the electrolysis space are both located on one side of the anode chamber.

3. The portable electrolysis product output device according to claim 2, characterized in that, The driving agent and the electrolyzed raw water are arranged in layers within the containment space. The output module has an inlet pipe extending into the containment space, and the inlet pipe extends in a direction away from the driving agent. The water inlet of the electrolysis module is connected to the containment space, and the water outlet is located near the water inlet pipe; Alternatively, the electrolysis module may be installed on the water inlet pipe.

4. The portable electrolysis product output device according to claim 3, characterized in that, The cathode chamber is provided with a gas outlet communicating with the outside of the containment space, and the first partition is provided with a gas-blocking structure.

5. The portable electrolysis product output device according to claim 2, characterized in that, The containment space is provided with a second partition, which divides the containment space into a first chamber and a second chamber. Electrolyzed raw water is provided in the first chamber, and a driving agent is provided in the second chamber. The electrolysis module is located in the first chamber, with the inlet connected to the first chamber and the outlet connected to the output module.

6. The portable electrolysis product output device according to claim 3 or 5, characterized in that, A first gap is provided between the first separator and the peripheral wall of the electrolysis space, and the cathode chamber is connected to the anode chamber through the first gap; The first separator is equipped with a water-blocking structure.

7. The portable electrolysis product output device according to claim 6, characterized in that, The anode is disposed adjacent to the first separator, and the area of ​​the anode is smaller than the area of ​​the first separator; A third gap is provided between the anode and the peripheral wall of the anode chamber, and / or a third gap is provided between the anode and the first partition; The third gap is connected to the first gap.

8. The portable electrolysis product output device according to claim 6, characterized in that, A second gap is provided between the cathode and the peripheral wall of the cathode chamber, and / or a second gap is provided between the cathode and the first partition; The second gap is connected to the first gap.

9. The portable electrolysis product output device according to claim 2, characterized in that, The output module includes a water outlet pipe connected to the outside, a first transition cavity, and a second transition cavity connected to the receiving space. The first transition cavity is disposed between the water outlet pipe and the second transition cavity. The water outlet pipe is slidably connected to the first transition cavity. When the water inlet end of the water outlet pipe is in the first transition cavity, the water inlet end is blocked by the inner wall of the first transition cavity. The inner diameter of the first transition cavity is smaller than the inner diameter of the second transition cavity.

10. The portable electrolysis product output device according to claim 9, characterized in that, The electrolysis module is located at the water outlet pipe; The inlet and outlet of the anode chamber are both connected to the outlet pipe.

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