阅读说明：本技术 自动加压混合溶氢装置 (Automatic pressurizing mixed hydrogen dissolving device ) 是由 陈渭涛 田丰 宗卫峰 周杰 张宇宙 于 2021-07-23 设计创作，主要内容包括：本发明提供一种自动加压混合溶氢装置,包括承压电解槽、三通阀、水泵、氢气溶解器、溶氢罐、压力传感器和自动泄压阀；溶氢罐的下部设置有含氢水出口；三通阀与氢气出口、氢气溶解器和水泵经循环管路相连通；氢气溶解器的另一端与溶氢罐的上部相连通,水泵背离的另一端与溶氢罐的下部相连通,压力传感器和自动泄压阀均与溶氢罐的顶部相连通；氢气溶解器包括若干个混合器及收缩管,且收缩管位于与溶氢罐相邻的一端,收缩管与溶氢罐相邻一端的尺寸小于与混合器相邻一端的尺寸。本发明通过水泵驱动,气水在循环管路内不断循环,随着循环次数增加,可以显著提高水中氢的浓度和氢气的溶解均匀性,且溶解的氢气在水中更稳定,不容易再度析出。(The invention provides an automatic pressurization mixed hydrogen dissolving device, which comprises a pressure-bearing electrolytic tank, a three-way valve, a water pump, a hydrogen dissolver, a hydrogen dissolving tank, a pressure sensor and an automatic pressure relief valve, wherein the pressure-bearing electrolytic tank is connected with the three-way valve; the lower part of the hydrogen dissolving tank is provided with a hydrogen-containing water outlet; the three-way valve is communicated with the hydrogen outlet, the hydrogen dissolver and the water pump through a circulating pipeline; the other end of the hydrogen dissolver is communicated with the upper part of the hydrogen dissolving tank, the other end of the water pump, which deviates from the water pump, is communicated with the lower part of the hydrogen dissolving tank, and the pressure sensor and the automatic pressure release valve are both communicated with the top of the hydrogen dissolving tank; the hydrogen dissolver comprises a plurality of mixers and a contraction pipe, the contraction pipe is positioned at one end adjacent to the hydrogen dissolving tank, and the size of the contraction pipe at one end adjacent to the hydrogen dissolving tank is smaller than that of the end adjacent to the mixers. According to the invention, the water pump is used for driving, the gas and water are continuously circulated in the circulating pipeline, the concentration of hydrogen in water and the dissolving uniformity of hydrogen can be obviously improved along with the increase of the circulating times, and the dissolved hydrogen is more stable in water and is not easy to separate out again.)

1. An automatic pressurizing and mixing hydrogen dissolving device is characterized by comprising a pressure-bearing electrolytic tank, a three-way valve, a water pump, a hydrogen dissolver, a hydrogen dissolving tank, a pressure sensor and an automatic pressure relief valve; the pressure-bearing electrolytic tank is provided with a water inlet, an oxygen-containing water outlet and a hydrogen outlet, and the lower part of the hydrogen dissolving tank is provided with a hydrogen-containing water outlet; the three-way valve is communicated with the hydrogen outlet, the hydrogen dissolver and the water pump through a circulating pipeline; the other end of the hydrogen dissolver, which is far away from the three-way valve, is communicated with the upper part of the hydrogen dissolving tank, the other end of the water pump, which is far away from the three-way valve, is communicated with the lower part of the hydrogen dissolving tank, and the pressure sensor and the automatic pressure release valve are communicated with the top of the hydrogen dissolving tank; the hydrogen dissolver comprises a plurality of mixers and a contraction pipe communicated with the mixers, the contraction pipe is positioned at one end adjacent to the hydrogen dissolving tank, and the size of the contraction pipe at one end adjacent to the hydrogen dissolving tank is smaller than that of the end adjacent to the mixers.

2. The automatic pressurizing and mixing hydrogen dissolving device according to claim 1, wherein the number of the hydrogen dissolvers is two or more, and the two or more hydrogen dissolvers are connected in series and/or in parallel.

3. The automatic pressurized mixed hydrogen dissolving device according to claim 1, wherein the hydrogen dissolver structure comprises one or a combination of a forward and reverse spiral structure and a cross insertion plate structure.

4. The automatic pressurized and mixed hydrogen dissolving device according to claim 1, wherein the pipe diameters of the hydrogen dissolver and the circulation pipeline are greater than or equal to 0.5cm and less than 1cm, and the outlet diameter of the contraction pipe at one end adjacent to the hydrogen dissolving tank is greater than 0.1cm and less than or equal to 0.5 cm.

5. The automatic pressurized mixing hydrogen dissolving device according to claim 1, wherein the total length of the hydrogen dissolver is 5cm or more, the length of the mixer is 4cm or more, and the length of the shrinkage tube is 1cm or less.

6. The automatic pressurizing and mixing hydrogen dissolving device according to claim 1, wherein the water pump is communicated with the bottom of the hydrogen dissolving tank, and the upper part of the hydrogen dissolving tank is further provided with a water inlet valve.

7. The automatic pressurizing and mixing hydrogen dissolving device according to claim 1, further comprising a pressure relief tank, wherein the pressure relief tank is communicated with the hydrogen-containing water outlet through a water outlet valve.

8. The automatic pressurized and mixed hydrogen dissolving device according to claim 1, wherein valves are disposed on the circulation pipeline between the three-way valve and the hydrogen dissolver and between the hydrogen dissolver and the hydrogen dissolving tank.

9. The automatic pressurizing and mixing hydrogen dissolving device according to claim 1, wherein the outlet pressure of the pressure-bearing electrolytic cell is not lower than 0.1MPa, and the gas output is not less than 50 mL/min; the pressure in the hydrogen dissolving tank is less than or equal to 0.5MPa, the volume of the hydrogen dissolving tank is not more than 1L, and the internal structure of the hydrogen dissolving tank comprises one or more of hollow and filling porous fillers.

10. The automatic pressurized mixed hydrogen dissolving device according to any one of claims 1 to 9, further comprising an atmospheric communication valve, wherein the atmospheric communication valve is communicated with the top of the hydrogen dissolving tank.

Technical Field

The invention relates to the technical field of water treatment, in particular to a hydrogen-containing water preparation device, and particularly relates to an automatic pressurizing and mixing hydrogen dissolving device.

Background

In recent years, various researchers of various countries find that hydrogen has obvious curative effects on nearly one hundred common diseases, and the popular view is that hydrogen molecules have selective antioxidant effect and can actively select to combine with harmful free radicals to generate water so as to eliminate the harmful free radicals. One of the ways of using hydrogen by human body is to dissolve hydrogen into water, the hydrogen uses water as carrier to enter the digestive system of human body, and after being absorbed, the hydrogen enters the blood system and reaches each organ of human body, thereby realizing the reduction of harmful free radicals in human body, providing a new treatment method for diseases generated by oxidative damage, and more importantly providing a prevention measure for preventing the occurrence of diseases and aging of human body. Among them, the concentration of hydrogen in water, that is, the dosage, is the most important index for determining the oxidation resistance of hydrogen water. The hydrogen is the lightest element of all elements, exists in a gas form at normal temperature and normal pressure, and has the solubility of about 1.6ppm in water under the condition of standard atmospheric pressure, so that the hydrogen is difficult to meet the treatment requirement. Therefore, the hydrogen is quickly and fully dissolved in the water to become a core technology for preparing the hydrogen water, and the hydrogen water preparation method has important practical value for instant hydrogen water drinking machines, high-concentration beauty instruments and other requirements. However, the existing hydrogen dissolving water preparation device is generally complex in structure and operation, the hydrogen content in the prepared hydrogen water is still low, the hydrogen distribution is uneven and unstable, and the water consumption in the preparation process is very large, so that the waste of water resources is caused.

Disclosure of Invention

In view of the above drawbacks of the prior art, an object of the present invention is to provide an automatic pressurized mixed hydrogen dissolving device, which is used to solve the problems that the hydrogen dissolving water preparation device in the prior art is generally complicated in structure and operation, the hydrogen content in the prepared hydrogen water is still relatively low, the hydrogen distribution is uneven and unstable, and the water consumption in the preparation process is large, which causes waste of water resources.

In order to achieve the above and other related objects, the present invention provides an automatic pressurizing and mixing hydrogen dissolving device, which comprises a pressure-bearing electrolytic tank, a three-way valve, a water pump, a hydrogen dissolver, a hydrogen dissolving tank, a pressure sensor and an automatic pressure relief valve; the pressure-bearing electrolytic tank is provided with a water inlet, an oxygen-containing water outlet and a hydrogen outlet, and the lower part of the hydrogen dissolving tank is provided with a hydrogen-containing water outlet; the three-way valve is communicated with the hydrogen outlet, the hydrogen dissolver and the water pump through a circulating pipeline; the other end of the hydrogen dissolver, which is far away from the three-way valve, is communicated with the upper part of the hydrogen dissolving tank, the other end of the water pump, which is far away from the three-way valve, is communicated with the lower part of the hydrogen dissolving tank, and the pressure sensor and the automatic pressure release valve are communicated with the top of the hydrogen dissolving tank; the hydrogen dissolver comprises a plurality of mixers and a contraction pipe communicated with the mixers, the contraction pipe is positioned at one end adjacent to the hydrogen dissolving tank, and the size of the contraction pipe at one end adjacent to the hydrogen dissolving tank is smaller than that of the end adjacent to the mixers.

Optionally, the hydrogen dissolvers are two or more, and the connection mode of the two or more hydrogen dissolvers comprises series connection and/or parallel connection.

Optionally, the structure of the hydrogen dissolver comprises one or a combination of a forward and reverse spiral structure and a cross-insertion plate structure.

Optionally, the pipe diameters of the hydrogen dissolver and the circulation pipeline are greater than or equal to 0.5cm and less than 1cm, and the outlet diameter of the end, adjacent to the hydrogen dissolving tank, of the contraction pipe is greater than 0.1cm and less than or equal to 0.5 cm.

Optionally, the total length of the hydrogen dissolver is greater than or equal to 5cm, the length of the mixer is greater than or equal to 4cm, and the length of the shrink tube is less than or equal to 1 cm.

Optionally, the water pump is communicated with the bottom of the hydrogen dissolving tank, and a water inlet valve is further arranged at the upper part of the hydrogen dissolving tank.

Optionally, the automatic pressurizing, mixing and hydrogen dissolving device further comprises a pressure relief tank, and the pressure relief tank is communicated with the hydrogen-containing water outlet through a water outlet valve.

Optionally, valves are arranged on the circulating pipelines between the three-way valve and the hydrogen dissolver and between the hydrogen dissolver and the hydrogen dissolving tank.

Optionally, the outlet pressure of the pressure-bearing electrolytic cell is not lower than 0.1MPa, and the gas output is not less than 50 mL/min.

Illustratively, the pressure in the hydrogen dissolving tank is less than or equal to 0.5 MPa.

By way of example, the volume of the hydrogen dissolving tank is not more than 1L, and the internal structure of the hydrogen dissolving tank comprises one or more of hollow and filling porous fillers.

Optionally, the automatic pressurization mixed hydrogen dissolving device further comprises an atmospheric communication valve, and the atmospheric communication valve is communicated with the top of the hydrogen dissolving tank.

As described above, the automatic pressurized mixed hydrogen dissolving device of the present invention has the following beneficial effects: through the improved structural design, the gas-water circulation device is driven by the water pump, the gas-water is continuously circulated in the circulation pipeline, the concentration of hydrogen in water and the dissolution uniformity of the hydrogen can be obviously improved along with the increase of the circulation times, and the dissolved hydrogen is more stable in water and is not easy to separate out again. Meanwhile, the invention can realize the recycling of water and reduce the consumption of water resources. The whole device has simple structure and very convenient operation.

Drawings

Fig. 1 is a schematic structural diagram of an automatic pressurized mixed hydrogen dissolving device provided by the invention.

Fig. 2-5 are schematic diagrams showing the hydrogen dissolver of fig. 1 in different examples.

Description of the element reference numerals

1 pressure-bearing electrolytic tank

2 Water pump

3 dissolve hydrogen jar

4 water outlet valve

5 pressure relief tank

6 valve

7 hydrogen dissolver

8 three-way valve

9 water inlet valve

10 atmosphere communicating valve

11 automatic pressure relief valve

12 pressure sensor

13 circulation pipeline

Detailed Description

The embodiments of the present invention are described below with reference to specific embodiments, and other advantages and effects of the present invention will be easily understood by those skilled in the art from the disclosure of the present specification. The invention is capable of other and different embodiments and of being practiced or of being carried out in various ways, and its several details are capable of modification in various respects, all without departing from the spirit and scope of the present invention. As in the detailed description of the embodiments of the present invention, the cross-sectional views illustrating the device structures are not partially enlarged in general scale for convenience of illustration, and the schematic views are only examples, which should not limit the scope of the present invention. In addition, the three-dimensional dimensions of length, width and depth should be included in the actual fabrication.

For convenience in description, spatial relational terms such as "below," "beneath," "below," "under," "over," "upper," and the like may be used herein to describe one element or feature's relationship to another element or feature as illustrated in the figures. It will be understood that these terms of spatial relationship are intended to encompass other orientations of the device in use or operation in addition to the orientation depicted in the figures. Further, when a layer is referred to as being "between" two layers, it can be the only layer between the two layers, or one or more intervening layers may also be present.

In the context of this application, a structure described as having a first feature "on" a second feature may include embodiments in which the first and second features are formed in direct contact, and may also include embodiments in which additional features are formed in between the first and second features, such that the first and second features may not be in direct contact.

It should be noted that the drawings provided in the present embodiment are only for illustrating the basic idea of the present invention, and the components related to the present invention are only shown in the drawings rather than drawn according to the number, shape and size of the components in actual implementation, and the type, quantity and proportion of the components in actual implementation may be changed freely, and the layout of the components may be more complicated. In order to keep the drawings as concise as possible, not all features of a single figure may be labeled in their entirety.

As shown in fig. 1, the invention provides an automatic pressurizing mixed hydrogen dissolving device, which comprises a pressure-bearing electrolytic tank 1, a three-way valve 8, a water pump 2, a hydrogen dissolver 7, a hydrogen dissolving tank 3, a pressure sensor 12 and an automatic pressure relief valve 11; the pressure-bearing electrolytic cell 1 is an electrolytic cell which can bear a certain pressure and generate hydrogen and oxygen by electrolysis, for example, the pressure-bearing electrolytic cell can bear more than one atmosphere pressure so as to ensure that the content of the hydrogen output from the pressure-bearing electrolytic cell 1 has a certain flow and pressure; the pressure-bearing electrolytic tank 1 is provided with a water inlet, an oxygen-containing water outlet and a hydrogen outlet, and the lower part (preferably the bottom) of the hydrogen dissolving tank 3 is provided with a hydrogen-containing water outlet; the three-way valve 8 is communicated with the hydrogen outlet, the hydrogen dissolver 7 and the water pump 2 through a circulating pipeline 13; the other end of the hydrogen dissolver 7, which is far away from the three-way valve 8, is communicated with the upper part of the hydrogen dissolving tank 3, the other end of the water pump 2, which is far away from the three-way valve 8, is communicated with the lower part (preferably the bottom part, which helps to reduce the power consumption of the water pump) of the hydrogen dissolving tank 3, the pressure sensor 12 and the automatic pressure relief valve 11 are both communicated with the top part of the hydrogen dissolving tank 3 (or are both arranged at the top part of the hydrogen dissolving tank 3), and the pressure sensor 12 can be further connected with the automatic pressure relief valve 11, so that when the pressure sensor 12 detects that the pressure in the hydrogen dissolving tank 3 exceeds a threshold value, the automatic pressure relief valve 11 is opened to release the pressure in the hydrogen dissolving tank 3, and the pressure in the hydrogen dissolving tank 3 can be maintained in a reasonable range in the process of preparing hydrogen water; the hydrogen dissolver 7 includes a plurality of mixers 71 (i.e., single or multiple mixers) and a shrink tube 72 communicated with the mixers 71, and the shrink tube 72 is positioned at one end adjacent to the hydrogen dissolving tank 3, and the size of one end of the shrink tube 72 adjacent to the hydrogen dissolving tank 3 is smaller than that of one end adjacent to the mixers 71. The three-way valve 8 is connected with the pressure-bearing electrolytic tank 1, pressure hydrogen is provided for the whole automatic pressure mixing hydrogen dissolving device, water in the hydrogen dissolving tank 3 and the hydrogen form gas-liquid two-phase flow to enter the hydrogen dissolver 7 under the power action provided by the water pump 2, the water and the gas are fully mixed in the pipeline, the hydrogen is rapidly dissolved in the water, and the hydrogen is sprayed into the hydrogen dissolving tank 3 through the shrinkage pipe 72. According to henry's law: where, X is the mole fraction of the dissolved gas in the solution, Pg is the pressure of the gas on the liquid surface at equilibrium, H is a constant, i.e. the pressure is proportional to the solubility, an increase in pressure will significantly increase the solubility of hydrogen in water, and by increasing the two important indicators of solubility and dissolution rate, hydrogen water of higher concentration can be rapidly produced. Through the improved structural design, the gas-water circulation device is driven by the water pump 2, the gas-water is continuously circulated in the circulation pipeline 13, the concentration of hydrogen in water and the dissolution uniformity of the hydrogen can be obviously improved along with the increase of the circulation times, the dissolved hydrogen is more stable in water and is not easy to separate out again, and high-quality hydrogen-containing water can be continuously and stably prepared. Meanwhile, the invention can realize the recycling of water and reduce the consumption of water resources. The whole device has simple structure and very convenient operation. Taking an electrolytic cell with the hydrogen production of 150mL/min as an example, under the pressure maintaining state of 0.2MPa and the capacity of a hydrogen dissolving tank 3 mL, hydrogen water is directly output through a hydrogen dissolver 7 without circulating through a water pump 2, and the hydrogen concentration is only about 0.6 ppm; the water pump 2 outputs hydrogen water after circulating for 1 minute, and the hydrogen concentration is not lower than 1.0 ppm; the water pump 2 outputs hydrogen water after circulating for 2 minutes, and the hydrogen concentration is not lower than 2.0 ppm. Meanwhile, the pressure sensor 12 detects the pressure in the hydrogen dissolving tank 3 in real time, and when the pressure in the hydrogen dissolving tank 3 is detected to exceed a threshold value, the automatic pressure release valve 11 is automatically opened to release the pressure so as to ensure that the pressure in the pressure release tank 5 is stabilized in a reasonable range, and the whole device is ensured to automatically, safely and efficiently operate.

As an example, the pressure in the hydrogen dissolving tank 3 is usually equal to or less than 0.5MPa (i.e., the threshold pressure in the hydrogen dissolving tank 3 is 0.5MPa) in order to avoid the risk of leakage or explosion.

As an example, the outlet pressure of the pressure-bearing electrolytic tank 1 is not lower than 0.1MPa, and the gas output is not less than 50 mL/min. The three-way valve 8 is used for connecting the water pump 2, the hydrogen outlet and the hydrogen dissolver 7 on the hydrogen outlet of the pressure-bearing electrolytic tank 1, the outlet of the connected hydrogen dissolver 7 is connected with the inlet on the hydrogen dissolving tank 3, the circulation of the mixture of hydrogen and water in the hydrogen dissolving tank 3 and the circulating pipeline is realized under the action of the water pump 2, the pressurized mixing of the hydrogen and the water is realized under the repeated action of the pressure and the hydrogen dissolver 7, and the higher solubility of the hydrogen is further realized.

As an example, the automatic pressurized mixing hydrogen dissolving device further comprises a pressure relief tank 5, wherein the pressure relief tank 5 is communicated with the hydrogen-containing water outlet through a water outlet valve 4 and used for releasing the hydrogen-containing water under pressure into the pressure relief tank 5, and the hydrogen-containing water outlet is arranged below the pressure relief tank 5.

In order to ensure the pressure in the pipeline and increase the friction shearing effect of the hydrogen dissolver 7 on the gas-liquid flow, as an example, the pipe diameter D of the hydrogen dissolver 7 and the circulating pipeline 13 is more than or equal to 0.5cm and less than 1cm, and the outlet diameter D of the end of the contraction pipe 72 adjacent to the hydrogen dissolving tank 3 is more than 0.1cm and less than or equal to 0.5cm, so that the water is sprayed to be better contacted with the hydrogen.

By way of example, the total length L of the hydrogen dissolver 7 is not less than (i.e. not less than) 5cm, wherein the length of the mixer 71 is not less than (i.e. not less than) 4cm, and the length of the shrink tube 72 is not more than (i.e. not more than) 1cm, thereby ensuring sufficient contact and mixing of the hydrogen with the water, and causing the exit of the shrink tube 72 to produce a liquid jet, thereby making the mixing of the water and the hydrogen diffused in the pipe more uniform and sufficient.

The hydrogen dissolving tank 3 is provided with the water outlet valve 4 and the water inlet valve 9, so that water replenishing or hydrogen discharging operation can be carried out, and the hydrogen dissolving tank 3 can be further provided with a water level sensor (not shown) for detecting the internal water level and closing the water inlet valve 9 when the internal water level reaches a preset water level. In addition, in another example, the automatic pressurizing and mixing hydrogen dissolving device further comprises an atmospheric communication valve 10, the atmospheric communication valve 10 is communicated with the hydrogen dissolving tank 3, and the atmospheric communication valve 10 is arranged at a height not lower than the horizontal height of the water inlet valve 9 of the hydrogen dissolving tank 3, preferably at the top of the hydrogen dissolving tank 3. The atmosphere communicating valve 10 can play a role in balancing the hydrogen dissolving tank 3 with the atmospheric pressure when opened, and can accelerate the speed of water replenishing and hydrogen releasing.

The hydrogen dissolver 7 may adopt a static or dynamic mixer, and when a static mixer is adopted, the structure of the hydrogen dissolver may be a forward and reverse spiral structure shown in fig. 2, or a cross insertion plate structure shown in fig. 3, or a combination of the two structures, or may also adopt other structures as long as the hydrogen dissolver can promote the hydrogen and the water to be mixed sufficiently and uniformly, and the structure is not limited strictly here.

The number of the hydrogen dissolvers 7 can be single or multiple, preferably two or more, and the connection mode of the two or more hydrogen dissolvers 7 includes series connection and/or parallel connection, that is, all the hydrogen dissolvers 7 are connected in parallel, as shown in fig. 4 specifically; or all hydrogen dissolvers 7 are connected in series, as shown in fig. 5; or some hydrogen dissolvers 7 are connected in parallel and then connected in series with other hydrogen dissolvers 7, which is not strictly limited in this embodiment. The water pump 2 is communicated with the bottom of the hydrogen dissolving tank 3, and the upper part of the hydrogen dissolving tank 3 is also provided with a water inlet valve 9. Of course, in other examples, a plurality of mixers 71 may be connected in series and/or in parallel to the same shrink tube 72, and the embodiment is not limited thereto.

As an example, valves 6 are arranged on the circulating pipelines 13 between the three-way valve 8 and the hydrogen dissolver 7 and between the hydrogen dissolver 7 and the hydrogen dissolving tank 3, so as to open or close the corresponding section of pipeline as required, thereby improving the control flexibility of the whole device.

By way of example, the volume of the hydrogen dissolving tank 3 is not more than 1L, the internal structure comprises one or more of hollow and filling porous fillers, and a filter can be further arranged in the hydrogen dissolving tank 3.

The automatic pressurizing and mixing hydrogen dissolving device can further comprise a controller such as a PLC (programmable logic controller) and the like, and the PLC can be connected with the electric control structures such as the pressure sensor 12, the water level sensor, the automatic pressure release valve 11, the water inlet valve 9, the water pump 2 and the like, so that the automation level of the whole device is further improved.

The specific installation process of the automatic pressurizing and mixing hydrogen dissolving device provided by the invention is as follows:

as shown in fig. 1, the lower part of a hydrogen dissolving tank 3 is connected with a water pump 2 through a circulation pipeline, an outlet of the water pump 2 is connected to a three-way valve 8, the three-way valve 8 is connected with a hydrogen outlet on a pressure-bearing electrolytic cell 1, so that a gas-liquid two-phase flow is formed and flows into a hydrogen dissolver 7 which is formed by combining a mixer 71 and a contraction pipe 72, and the hydrogen dissolver 7 is directly connected to the hydrogen dissolving tank 3 to form a circulation loop; an automatic pressure relief valve 11 is arranged above the hydrogen dissolving tank 3 to ensure that the pressure in the hydrogen dissolving tank 3 is kept in a reasonable range when hydrogen continuously enters; the water outlet valve 4 below the hydrogen dissolving tank 3 is connected with the pressure relief tank 5 to achieve the effects of pressure relief buffering and hydrogen water release.

An exemplary operation flow for performing pressurized mixed hydrogen dissolving by adopting the automatic pressurized mixed hydrogen dissolving device provided by the invention is as follows:

1. closing the water outlet valve 4, opening the water inlet valve 9 and the atmosphere communicating valve 10, adding water into the hydrogen dissolving tank 3 by a water pump and the like until the water level sensor detects that the water is full, and then closing the water inlet valve 9 and the atmosphere communicating valve 10; starting the pressure-bearing electrolytic tank 1, enabling hydrogen to enter the pipeline and the hydrogen dissolving tank 3 to enable the internal pressure of the hydrogen dissolving tank 3 to be gradually increased, starting the water pump 2 after the automatic pressure release valve 11 starts to release pressure, enabling water and hydrogen in the hydrogen dissolving tank 3 to form a gas-liquid two-phase flow, enabling the water and the hydrogen to enter the hydrogen dissolver 7 to be fully mixed and sprayed by the contraction pipe 72, and enabling the water and the hydrogen to be repeatedly dissolved and circulated in the hydrogen dissolving tank 3 and the circulation pipeline to enable the concentration of the hydrogen dissolved in the water to be rapidly increased; after the design concentration requirement is met, the pressure-bearing electrolytic tank 1 and the water pump 2 are closed, the water outlet valve 4 is opened, the pressure in the hydrogen dissolving tank 3 is released into the pressure relief tank 5, and then the atmosphere communicating valve 10 is opened to communicate the hydrogen dissolving tank 3 with the atmosphere, so that the prepared hydrogen water is released. Of course, in other examples, the water pump does not need to be started until the automatic pressure relief valve 11 is relieved, the water pump can be started simultaneously along with the electrolytic cell, and the dissolving effect can be met at the same time.

2. After the hydrogen dissolved in the water rapidly reaches the designed concentration, the hydrogen water can be stored in the hydrogen dissolving tank 3, after the pressure sensor 12 detects that the gas pressure is reduced or counts for a certain time, the step 1 is started, so that the concentration of the hydrogen water in the hydrogen dissolving tank 3 is always maintained in a reasonable range.

In order to make the technical scheme and the advantages of the invention more prominent, the automatic pressurizing and mixing hydrogen dissolving device of the invention is further experimentally verified through comparative examples and examples. Among them, the hydrogen solubility in water was examined using a dissolved hydrogen concentration measuring reagent in both comparative examples and examples.

Comparative examples 1 to 2

In the comparative example 1, the hydrogen water is directly and rapidly prepared without maintaining the pressure of gas and circulating water, a pressure-bearing electrolytic cell with the hydrogen production amount of 150mL/min is used, the generated hydrogen enters a circulating pipeline and does not pass through circulation, and the hydrogen water is directly released through a valve after passing through a hydrogen dissolver; comparative example 2 in the same manner as in comparative example 1, but using a pressure-bearing electrolytic cell with a hydrogen generation amount of 300mL/min, the hydrogen gas generated was discharged directly through a valve without being circulated after entering a circulation line, and the results are shown in the table.

TABLE 1 hydrogen solubility of comparative examples 1 and 2

Examples 1 to 4

Example 1 on the basis of comparative example 1, a pressure-bearing electrolytic cell with a hydrogen production rate of 150mL/min and 1 hydrogen dissolver were used, and water was circulated for 60 seconds under a hydrogen pressure of 0.2 MPa; the cycle time was further increased to 120 seconds in example 2. Examples 3 and 4 were carried out by replacing the pressure-bearing electrolytic cell having a hydrogen generation amount of 150mL/min in examples 1 and 2 with a pressure-bearing electrolytic cell having a hydrogen generation amount of 300mL/min, and circulating water for 60 seconds and 120 seconds, respectively. The results obtained are shown in the following table.

Table 2 hydrogen solubility of examples 1-4

Comparative examples 3 to 4

In the above examples, a hydrogen dissolver was used, and in this pair of comparative examples, a series of hydrogen dissolvers were added after mixing the hydrogen gas with the gas-liquid two phase formed by the water pump, and the hydrogen water was directly led out through the dissolver for measurement, and in comparative example 3, a pressure-bearing electrolytic cell with a hydrogen production rate of 150mL/min was used to directly mix and lead out the hydrogen water; in the comparative example 4, the pressure-bearing electrolytic cell with the hydrogen production rate of 150mL/min in the comparative example 3 is replaced by the pressure-bearing electrolytic cell with the hydrogen production rate of 300mL/min, and the hydrogen water is directly mixed and led out. The results of comparative examples 3 and 4 are shown in the table below.

TABLE 3 hydrogen solubility of comparative examples 3 and 4

Examples 5 to 8

In the embodiment of the group, on the basis of comparative examples 3 and 4, hydrogen continuously generated by pressure-bearing electrolytic cells with different gas production rates enters the hydrogen dissolving tank, so that the hydrogen pressure in the hydrogen dissolving tank is continuously increased, and the hydrogen water dissolving circulation time is increased to 60s and 120s under the multiple actions of the hydrogen pressure, a hydrogen dissolver, a circulation system and the like. Specifically, example 5 increased the cycle time of comparative example 3 to 60s, and example 6 further increased the cycle time to 120 s; example 7 further increased the cycle time of comparative example 4 to 60s and example 8 further increased the cycle time to 120s, with the results shown in the table below.

Table 4 hydrogen solubility of examples 5-8

Examples 9 to 12

Examples 9 to 12 the following table shows the results of tests in which two phases of gas and liquid mixed by hydrogen gas and a water pump were mixed and the 2 serial hydrogen dissolvers were replaced with 2 parallel hydrogen dissolvers in accordance with examples 5 to 8.

TABLE 5 hydrogen solubility of examples 9-12

Examples 13 to 14

Examples 13 and 14 on the basis of examples 9 and 10, the hydrogen pressure was increased from 0.2MPa to 0.25MPa, and further experiments were carried out using a pressure-bearing electrolytic cell having a gas production rate of 150mL/min, in which example 13 was circulated for 60 seconds under the multiple actions of the hydrogen pressure of 0.25MPa and a dissolver and circulation system, and example 14 was carried out with a cycle time further increased to 120 seconds, and the results are shown in table 6.

TABLE 6 hydrogen solubility of examples 13-14

Examples 15 to 16

Examples 15 and 16 increased the hydrogen pressure from 0.25MPa to 0.3MPa on the basis of examples 13 and 14. Specifically, in example 15, a pressure-bearing electrolytic cell with a gas production rate of 150mL/min and 2 hydrogen dissolvers connected in parallel are used, and circulation is performed for 30s under the action of 0.3MPa of hydrogen pressure; example 16 the cycle time was further increased to 60s and the results obtained are shown in table 7.

TABLE 7 hydrogen solubility of examples 13-14

It can be seen from the above comparative examples and examples that the use of the automatic pressurized mixed hydrogen dissolving device provided by the present invention can effectively increase the hydrogen content in water under the same conditions, and can achieve the purpose of flexibly adjusting the solubility of hydrogen in water by adjusting one or more of the parameters of hydrogen pressure, the gas production rate of the pressure-bearing electrolytic cell, the number and/or connection mode of the hydrogen dissolvers, the cycle time, etc., and can meet different requirements.

In summary, the present invention provides an automatic pressurizing and mixing hydrogen dissolving device. The automatic pressurizing and mixing hydrogen dissolving device comprises a pressure-bearing electrolytic tank, a three-way valve, a water pump, a hydrogen dissolver, a hydrogen dissolving tank, a pressure sensor and an automatic pressure relief valve; the pressure-bearing electrolytic tank is provided with a water inlet, an oxygen-containing water outlet and a hydrogen outlet, and the lower part of the hydrogen dissolving tank is provided with a hydrogen-containing water outlet; the three-way valve is communicated with the hydrogen outlet, the hydrogen dissolver and the water pump through a circulating pipeline; the other end of the hydrogen dissolver, which is far away from the three-way valve, is communicated with the upper part of the hydrogen dissolving tank, the other end of the water pump, which is far away from the three-way valve, is communicated with the lower part of the hydrogen dissolving tank, and the pressure sensor and the automatic pressure release valve are communicated with the top of the hydrogen dissolving tank; the hydrogen dissolver comprises a plurality of mixers and a contraction pipe communicated with the mixers, the contraction pipe is positioned at one end adjacent to the hydrogen dissolving tank, and the size of the contraction pipe at one end adjacent to the hydrogen dissolving tank is smaller than that of the end adjacent to the mixers. Through the improved structural design, the gas-water is continuously circulated in the circulating pipeline through the driving of the water pump, the concentration of hydrogen in water and the dissolving uniformity of the hydrogen can be obviously improved along with the increase of the circulating times, the dissolved hydrogen is more stable in water and is not easy to separate out again, and the hydrogen water with high hydrogen content can be continuously and stably prepared. Meanwhile, the invention can realize the recycling of water and reduce the consumption of water resources. The whole device has simple structure and very convenient operation. Therefore, the invention effectively overcomes various defects in the prior art and has high industrial utilization value.

The foregoing embodiments are merely illustrative of the principles and utilities of the present invention and are not intended to limit the invention. Any person skilled in the art can modify or change the above-mentioned embodiments without departing from the spirit and scope of the present invention. Accordingly, it is intended that all equivalent modifications or changes which can be made by those skilled in the art without departing from the spirit and technical spirit of the present invention be covered by the claims of the present invention.