CN219550251U - Movable hydrogenation machine - Google Patents
Movable hydrogenation machine Download PDFInfo
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- CN219550251U CN219550251U CN202320107622.9U CN202320107622U CN219550251U CN 219550251 U CN219550251 U CN 219550251U CN 202320107622 U CN202320107622 U CN 202320107622U CN 219550251 U CN219550251 U CN 219550251U
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- hydrogen
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- 238000005984 hydrogenation reaction Methods 0.000 title claims abstract description 74
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 194
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 97
- 239000001257 hydrogen Substances 0.000 claims abstract description 95
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 95
- 238000000746 purification Methods 0.000 claims abstract description 52
- 239000007788 liquid Substances 0.000 claims description 46
- 239000000463 material Substances 0.000 claims description 12
- 239000012535 impurity Substances 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 5
- 238000002347 injection Methods 0.000 claims description 5
- 239000007924 injection Substances 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 5
- 238000004891 communication Methods 0.000 claims description 3
- 239000007787 solid Substances 0.000 abstract description 13
- 239000007789 gas Substances 0.000 description 10
- 239000008213 purified water Substances 0.000 description 10
- 238000005868 electrolysis reaction Methods 0.000 description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000013461 design Methods 0.000 description 4
- 238000004880 explosion Methods 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 230000009172 bursting Effects 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Separation By Low-Temperature Treatments (AREA)
Abstract
The utility model provides a movable hydrogenation machine, which comprises a shell, a water tank, a purification cavity, a PEM (PEM) electrolytic tank, a gas-water separator, a power supply and a controller module, wherein the water tank, the purification cavity, the PEM electrolytic tank, the gas-water separator, the power supply and the controller module are arranged in the shell, compressed hydrogen is conveniently injected into an external device by communicating a hydrogenation gun with a hydrogenation port of the gas-water separator, the working state of the hydrogenation machine is monitored in real time by arranging a plurality of types of sensors, the reliable running time of the hydrogenation machine and the purity of generated hydrogen are improved, the portable movement of the hydrogenation machine is realized by a movable hub arranged at the bottom of the shell, and compared with a fixed hydrogenation station, the hydrogenation efficiency of the solid hydrogen storage is improved, the hydrogenation of the solid hydrogen storage can be realized anytime and anywhere.
Description
Technical Field
The utility model relates to the field of hydrogen energy, in particular to a movable hydrogenation machine.
Background
The economic development has increasingly increased demands for new energy, and in order to solve the problems of insufficient energy supply and environmental pollution, the use of fossil fuels must be reduced, and the input of renewable energy sources is increased. Among them, renewable energy sources such as hydrogen energy, solar energy, biomass energy and the like are popular choices, and particularly, hydrogen energy is recognized as the most promising energy carrier at present due to the characteristics of no pollution, storability, transportable, wide source, cleanliness, high heat value, rich application scene, low ignition point and the like.
Hydrogen energy sources are in gaseous form under normal conditions and are flammable and explosive, which presents great difficulties in their storage and transportation. At present, a relatively mature hydrogen storage mode is a high-pressure gas hydrogen mode, and the principle is that hydrogen is compressed and stored in a pressure-resistant tank, however, the hydrogen storage mode has extremely high requirements on a container, and the bottlenecks such as low hydrogen storage capacity, short transportation distance and the like and the risks of gas leakage and explosion exist. Compared with the hydrogen storage mode of high-pressure gas hydrogen, the solid hydrogen storage mode has high hydrogen storage capacity, does not need high pressure or a heat insulation container, has no explosion hazard, and becomes a very ideal hydrogen storage mode. However, at present, the devices and apparatuses for hydrogenation and hydrogen charging of the solid-state hydrogen storage device are fewer, and most hydrogenation devices are fixed hydrogenation stations and the like, so that hydrogenation of the solid-state hydrogen storage device at any time and any place cannot be realized.
Disclosure of Invention
In view of the above-mentioned drawbacks of the prior art, an object of the present utility model is to provide a mobile hydrogenation machine, which is used for solving the problem that most hydrogenation devices in the prior art are fixed hydrogenation stations, so that hydrogenation for a solid hydrogen storage device can not be performed anytime and anywhere.
To achieve the above and other related objects, the present utility model provides a mobile hydrogenation machine comprising:
a housing;
the movable hub is positioned at the bottom of the shell;
the water tank is arranged in the shell, comprises a water tank inlet and a water tank outlet, and is further provided with a tank cover at the water tank inlet, and is provided with a water quality sensor, a pressure sensor, a water temperature sensor, a first liquid level sensor and a second liquid level sensor;
the purification cavity is arranged in the shell, positioned below the water tank and communicated with the water tank outlet, comprises a purification cavity outlet, and is filled with a purification medium;
the PEM electrolyzer is arranged in the shell and is positioned below the purification cavity, the PEM electrolyzer comprises a water injection port and a hydrogen outlet, and the water injection port is communicated with the purification cavity outlet;
the gas-water separator is arranged in the shell and comprises a hydrogen inlet, a pressure relief opening and a hydrogenation opening, wherein the hydrogen inlet is communicated with the hydrogen outlet through a pipeline, a first control valve is arranged on the pipeline, the hydrogenation opening is communicated with a hydrogenation gun positioned outside the shell through a pipeline, a second control valve is arranged on the pipeline, the pressure relief opening is positioned at the bottom of the water-gas separation mechanism and extends to the outside of the shell, a third control valve is arranged at the pressure relief opening, and a third liquid level sensor and a hydrogen purity sensor are arranged on the gas-water separator;
the direct current power supply is arranged in the shell, and the positive electrode and the negative electrode of the output end of the direct current power supply are respectively and electrically connected with the positive electrode and the negative electrode of the PEM electrolytic tank;
the controller module is respectively in communication connection with the water quality sensor, the pressure sensor, the water temperature sensor, the first liquid level sensor, the second liquid level sensor, the third liquid level sensor and the hydrogen purity sensor.
Optionally, the mobile hydrogenation machine further comprises an alarm, and the controller module is electrically connected with a plurality of the alarms.
Optionally, the first liquid level sensor and the second liquid level sensor are located outside the water tank, the first liquid level sensor is a high liquid level sensor, the second liquid level sensor is a low liquid level sensor, the third liquid level sensor is located outside the gas-water separator, and the third liquid level sensor is a high liquid level sensor.
Optionally, the first control valve, the second control valve and the third control valve are all automatic valves.
Optionally, the volume of the water tank is not less than 1L and the compressive strength is not less than 2MPa.
Optionally, the gas-water separator is filled with a gas-water separation material, a hydrogen drying material and a hydrogen impurity removal material in sequence from bottom to top.
Optionally, the volume capacity of the gas-water separator is not less than 500mL and the compressive strength is not less than 2MPa.
Optionally, the water tank, the purification cavity and the PEM electrolyzer are detachably connected, wherein the fixing mode comprises one or a combination of screw connection, buckle connection and bolt connection.
Optionally, the purification medium and the purification chamber are detachably connected so as to facilitate the replacement of the purification medium.
Optionally, the gas-water separator is detachably connected with the hydrogen inlet, the pressure relief port and the hydrogenation port, wherein the fixing mode comprises one or a combination of threaded connection and buckle connection.
As described above, the mobile hydrogenation machine comprises a shell, and a water tank, a purification cavity, a PEM (PEM) electrolytic tank, a gas-water separator, a power supply and a controller module which are arranged in the shell, wherein the hydrogenation gun is communicated with a hydrogenation gas port of the gas-water separator, so that compressed hydrogen is conveniently injected into an external device, the working state of the hydrogenation machine is monitored in real time by arranging a plurality of types of sensors, the reliable running time of the hydrogenation machine and the purity of generated hydrogen are improved, the portable movement of the hydrogenation machine is realized by arranging a movable hub at the bottom of the shell, and compared with a fixed hydrogenation station, the hydrogenation efficiency of the solid hydrogen storage is improved, the hydrogenation of the solid hydrogen storage can be realized anytime and anywhere.
Drawings
FIG. 1 is a schematic diagram showing the structure of a mobile hydrogenation apparatus according to the present utility model.
FIG. 2 shows a schematic diagram of the structure of the water tank, purification chamber and PEM electrolyzer of the mobile hydrogenator of the present utility model.
Fig. 3 is a schematic structural view of a gas-water separator of the mobile hydrogenation machine according to the present utility model.
Fig. 4 is a schematic diagram of the working principle of the controller module of the mobile hydrogenation machine according to the present utility model.
Description of element reference numerals
101. Shell body
102. Water tank
1021. Water tank inlet
1022. Water tank outlet
1023. Water quality sensor
1024. Second liquid level sensor
1025. First liquid level sensor
1026. Water temperature sensor
1027. Pressure sensor
103. Purification chamber
1031. Purification chamber outlet
1032. Purification medium
104 PEM electrolytic cell
1041. Hydrogen outlet
105. DC power supply
106. Gas-water separator
1061. Pressure relief port
1062. Hydrogen inlet
1063. Hydrogenation port
1064. Third liquid level sensor
1065. Hydrogen purity sensor
1066. Gas-water separation material
1067. Hydrogen drying material
1068. Hydrogen impurity removing material
107. Movable hub
108. Controller module
109. First control valve
110. Second control valve
111. Third control valve
112. Hydrogenation gun
113. Alarm device
Detailed Description
In order to describe the possible application scenarios, technical principles, practical embodiments, and the like of the present utility model in detail, the following description is made with reference to the specific embodiments and the accompanying drawings. The embodiments described herein are only for more clearly illustrating the technical aspects of the present utility model, and thus are only exemplary and not intended to limit the scope of the present utility model.
Unless defined otherwise, technical terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which the present utility model pertains; the use of related terms herein is for the purpose of describing particular embodiments only and is not intended to limit the utility model.
In the present utility model, terms such as "first" and "second" are used merely to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply any actual number, order, or sequence of such entities or operations.
Spatially relative terms, such as "above … …," "above … …," "upper surface at … …," "above," and the like, may be used herein for ease of description to describe one device or feature's spatial location relative to another device or feature as illustrated in the figures. It will be understood that the spatially relative terms are intended to encompass different orientations in use or operation in addition to the orientation depicted in the figures. For example, if the device in the figures is turned over, elements described as "above" or "over" other devices or structures would then be oriented "below" or "beneath" the other devices or structures. Thus, the exemplary term "above … …" may include both orientations of "above … …" and "below … …". The device may also be positioned in other different ways (rotated 90 degrees or at other orientations) and the spatially relative descriptors used herein interpreted accordingly.
Unless specifically stated or limited otherwise, the terms "mounted," "connected," "affixed," "disposed," and the like as used in the description of embodiments of the utility model should be construed broadly. For example, the "connection" may be a fixed connection, a detachable connection, or an integral arrangement; the device can be mechanically connected, electrically connected and communicated; it can be directly connected or indirectly connected through an intermediate medium; which may be a communication between two elements or an interaction between two elements. The specific meaning of the above terms in the embodiments of the present utility model can be understood by those skilled in the art to which the present utility model pertains according to circumstances.
According to some embodiments of the utility model, please refer to fig. 1-4. As shown in fig. 1 to 3, the present embodiment relates to a mobile hydrogenation machine, comprising a housing 101, a water tank 102, a purification chamber 103, a PEM electrolyzer 104 and a gas-water separator 106, wherein the water tank 102 is arranged in the housing 101, the water tank 102 comprises a water tank inlet 1021 and a water tank outlet 1022, and a tank cover (not shown) is arranged at the water tank inlet, wherein the water tank inlet 1021 is connected with the housing 101 to form an injection port of purified water; the purification chamber 103 is arranged in the shell 101 and is positioned right below the water tank 102, the purification chamber 103 and the water tank outlet 1022 are communicated with each other, and the purification chamber 103 is also provided with a purification chamber outlet 1031 so that purified water in the water tank can enter the PEM electrolytic cell 104 through the purification chamber 103; the PEM electrolyzer 104 is arranged in the shell 101 and is positioned below the purification cavity 103, the PEM electrolyzer 104 comprises a water filling port and a hydrogen outlet 1041, wherein the water filling port is communicated with the purification cavity outlet 1031, oxygen generated by electrolysis water can escape into the purification cavity 103 through the water filling port and finally escape to the outside of the shell through the water tank inlet 1021, a purification medium 1032 is also arranged in the purification cavity 103, and is generally purification resin, so that purified water in the water tank can be further purified to ensure that the water quality entering the PEM electrolyzer 104 is qualified, and in addition, the purification medium 1032 has a certain service life, so that the purification medium 1032 and the purification cavity 103 are detachably connected, thereby facilitating the replacement of the purification medium 1032; the gas-water separator 106 is disposed in the housing 101, the gas-water separator 106 includes a hydrogen inlet 1062, a pressure relief port 1061, and a hydrogenation port 1063, the hydrogen inlet 1062 is communicated with the hydrogen outlet 1041 through a pipe so that hydrogen generated by the PEM electrolyzer 104 can enter the gas-water separator 106, the hydrogenation port 1063 is communicated to the hydrogenation gun 112 outside the housing through a gas pipe, and the pressure relief port 1061 is disposed at the bottom of the gas-water separator 106 and extends to the outside of the housing 101, thereby implementing pressure relief and water drainage for the inside of the gas-water separator 106.
In this embodiment, as shown in fig. 1, a dc power supply 105 is further disposed in the housing 101, the positive and negative electrodes of the dc power supply 105 are electrically connected with the positive and negative electrodes of the PEM electrolyzer 104, the dc power supply 105 adopts a power supply in the prior art, which is not described in detail here, and the dc power supply 105 can stably supply power to the PEM electrolyzer 104, so as to continuously electrolyze water to produce hydrogen.
In this embodiment, as shown in fig. 2 and 4, in order to make the volume of purified water added into the water tank 102 not overflow due to too much or not too little for subsequent electrolysis, a first liquid level sensor 1025 and a second liquid level sensor 1024 connected to the controller module 108 are disposed outside the water tank 102, where the first liquid level sensor 1025 is a high liquid level sensor and the second liquid level sensor 1024 is a low liquid level sensor, so that when purified water is added into the water tank 102, the water level is enough when the first liquid level sensor 1025 is reached, at this time, the controller module 108 controls the corresponding alarm 113 to alarm, thereby reminding the operator to stop adding water, and when the water level is reached to the second liquid level sensor 1024, the corresponding alarm 113 is controlled to alarm, thereby reminding the operator to add water into the water tank.
In this embodiment, as shown in fig. 2 and 4, in order to prevent the purification resin 1032 in the purification chamber 103 from being damaged due to the excessive water temperature, on the one hand, the water temperature has an important effect on the operation efficiency, operation performance, etc. of the PEM electrolyzer 104, and in order to maintain the temperature of the PEM electrolyzer 104 in an optimal temperature range, the temperature of purified water entering the PEM electrolyzer 104 needs to be controlled. Therefore, a water temperature sensor 1026 is provided in the water tank 102, and the water temperature sensor 1026 is electrically connected to the controller module 108, so that the water temperature in the water tank 102 can be monitored in real time; if the water temperature in the water tank 102 is detected to be too high (e.g., above 60 ℃), the controller module 108 will stop the electrolysis operation of the PEM electrolyzer 104 and send a corresponding high temperature warning signal to prompt the operator to replace purified water in the water tank 102 or to cool the water tank 102 until the water temperature is below 60 ℃, thereby ensuring that the water temperature entering the PEM electrolyzer 104 is always no higher than 60 ℃.
In this embodiment, as shown in fig. 2 and 4, in the process of generating hydrogen and oxygen by using the PEM electrolyzer 104, the purification chamber 103 and the water tank 102, since the PEM electrolyzer 104, the purification chamber 103 and the water tank 102 are communicated with each other, the oxygen is released to the outside of the housing 101 through the purification chamber 103 and the water tank inlet 1021 for exhausting, and in order to maintain the gas pressures of the PEM electrolyzer 104, the purification chamber 103 and the water tank 102 at a constant value (for example, not more than 2 MPa), the gas pressures in the PEM electrolyzer 104, the purification chamber 103 and the water tank 102 need to be controlled. Therefore, the pressure sensor 1027 is disposed in the water tank 102, the pressure sensor 1027 is electrically connected with the controller module 108, so that the pressure in the water tank 102 can be monitored in real time, and the cover can be automatically opened and closed by the controller module 108, if the pressure in the water tank 102 is detected to be too high (for example, more than 2 MPa), the controller module 108 can control the cover to be automatically opened to release the pressure in the water tank, so that the pressure in the water tank 102 is prevented from being too high, the phenomenon of bursting of the water tank 102 occurs, and after the pressure of the water tank 102 is released, the controller module 108 can also control the cover to be automatically closed.
In this embodiment, as shown in fig. 1 and 3, before the hydrogen generated by the water electrolysis in the PEM electrolyzer 104 enters the gas-water separator 106, the pressure of the hydrogen entering the gas-water separator 106 needs to be ensured, therefore, a first control valve 109, which is an automatic valve, is disposed on the pipeline where the hydrogen outlet 1041 communicates with the hydrogen inlet 1062, when the pressure of the hydrogen generated in the PEM electrolyzer 104 is not less than 2Mpa, the first control valve 109 will be automatically opened to enable the hydrogen to enter the gas-water separator 106, and when the pressure of the hydrogen is less than 2Mpa, the first control valve 109 will be closed, and of course, the first control valve 109 may also be manually opened.
In addition, as shown in fig. 3, a small amount of moisture and oxygen are added to the hydrogen generated by the water electrolysis in the PEM electrolyzer 104 during the process of entering the gas-water separator 106, so that the gas-water separator 106 is sequentially filled with a gas-water separation material 1066, a hydrogen drying material 1067 and a hydrogen impurity removal material 1068 from bottom to top, thereby ensuring that the hydrogen added through the hydrogenation gun 112 can reach the required purity. In addition, when the hydrotreater is continuously operated for a long time (more than or equal to 24 h), waste water exists in the gas-water separator 106, so that a third liquid level sensor 1064 is arranged outside the gas-water separator 106, and the third liquid level sensor 1064 is a high liquid level sensor, when the third liquid level sensor 1064 detects the water level in the gas-water separator 106, the waste water content in the gas-water separator 106 is too high, a third control valve 111 which is an automatic valve and is arranged at the pressure relief port 1061 is automatically started to release pressure and discharge water, so that redundant waste water is discharged to the outside of the shell 101 through the pressure relief port 1061, the pressure relief port is closed again after 30s, the service life of the gas-water separator 106 and the purity of hydrogen are improved, and the third control valve 111 can be opened manually.
In this embodiment, as shown in fig. 3, in order to ensure the purity and pressure of the hydrogen gas added to the solid hydrogen storage device, a hydrogen purity sensor 1065 is further disposed on the pipe of the gas-water separator 106 leading to the hydrogenation gun 112, and optionally, the hydrogen purity sensor 1065 also has a function of detecting the pressure. Specifically, a second control valve 110 with an automatic valve is disposed on a gas pipeline communicating the hydrogenation port 1063 with the hydrogenation gun 112, when the hydrogen purity sensor 1065 detects that the hydrogen pressure in the gas-water separator 106 reaches 2MPa and the hydrogen purity reaches 99.99%, the hydrogenation gun 112 is started, at this time, the second control valve 110 is automatically opened to hydrogenate the solid hydrogen storage device, when the hydrogen pressure in the gas-water separator 106 is less than 2MPa or the hydrogen purity is less than 99.99%, at this time, the hydrogenation gun 112 cannot be started, and the second control valve 110 is in a closed state, i.e. the hydrogenation machine is in a standby state. In addition, the hydrogenation guns used in the present embodiment can monitor the pressure of hydrogen gas injected into the solid-state hydrogen storage in real time to prevent the risk of explosion caused by excessive pressure of hydrogen gas injected into the solid-state hydrogen storage.
In addition, as shown in fig. 2, the water quality condition in the water tank 102 also affects the electrolysis efficiency, so that the water quality sensor 1023 is arranged in the water tank 102, and the water quality sensor 1023 is electrically connected with the controller module 108, so that the water quality condition in the water tank 102 can be monitored in real time; if it is detected that the total dissolved solids in the water is too high (e.g., TDS. Gtoreq.1), the controller module 108 will stop the electrolysis of the PEM electrolyzer 104 and issue a corresponding warning signal to prompt the operator to replace the water in the water tank, at which point the pressure sensor 1027, third control valve 111 and first control valve 109 are activated to release all pressure in the hydrogenation machine until the water in the water tank 102 is replaced, thereby ensuring good water quality entering the PEM electrolyzer 104.
As an example, the volume of the water tank 102 is not less than 1L and the compressive strength is not less than 2Mpa.
Specifically, in this embodiment, as shown in fig. 2, in order to ensure that hydrogen gas can be continuously generated and that the operator does not continuously add water, the volume of the water tank 102 is set to be not less than 1L, and in addition, the compressive strength of the water tank 102 is also not less than 2Mpa, so as to prevent the explosion of the water tank 102. The design of the water tank 102 is not limited thereto and may be adapted as desired.
As an example, the volume capacity of the gas-water separator 106 is not less than 500mL and the compressive strength is not less than 2Mpa.
Specifically, in this embodiment, as shown in fig. 3, in order to ensure that hydrogen generated by electrolysis can be stored in a certain amount in the gas-water separator and in order to arrange a drying and impurity removing component for hydrogen, the volume capacity of the gas-water separator 106 is set to be not less than 500mL, and in addition, the compressive strength of the gas-water separator 106 is also not less than 2Mpa, so that the gas-water separator 106 is prevented from cracking. However, the design of the gas-water separator 106 is not limited thereto, and may be changed adaptively as needed.
As an example, the water tank 102, the purification chamber 103 and the PEM electrolyzer 104 are detachably connected, wherein the fixing means comprises one or a combination of screw connection, snap connection and latch connection.
Specifically, in this embodiment, as shown in fig. 2, the water tank 102 is detachably connected to the purification chamber 103, and the purification chamber 103 is detachably connected to the PEM electrolyzer 104, preferably specifically, by a snap-fit connection, so that the maintenance is facilitated, but the design of the connection mode is not limited thereto, and can be changed adaptively as required.
As an example, the gas-water separator 106 is detachably connected to the hydrogen inlet 1062, the pressure relief port 1061, and the hydrogenation port 1063, where the fixing manner includes one or a combination of a threaded connection and a snap connection.
In particular, in the present embodiment, as shown in fig. 3, the hydrogen inlet 1062, the pressure relief port 1061, and the hydrogenation port 1063 provided on the gas-water separator 106 are detachably connected to the gas-water separator 106, and are preferably specifically threaded, so as to facilitate detachment and replacement, but the design of the connection mode is not limited thereto, and may be adaptively changed as required.
In this embodiment, as shown in fig. 1, a moving hub 107 is further rotatably installed at the bottom of the housing 101 through a frame, and the number of the moving hubs is at least four, so that the portable movement of the hydrogenation machine is realized, and the effect of performing real-time hydrogenation on the solid hydrogen storage device is achieved.
In this embodiment, the working principle of the hydrogenation machine is as follows:
firstly, adding a certain amount of purified water into the water tank 102 through the water tank inlet 1021, at this time, starting the hydrogenation machine and continuing to add the purified water until a high liquid level sensor 1025 of the water tank 102 sends out an early warning signal, then waiting for a water quality sensor 1023 and a water temperature sensor 1026 to detect the purified water, after the detection is qualified, controlling the PEM electrolytic tank 104 to electrolyze the water to produce hydrogen through the direct current power supply 105, when the hydrogen pressure in the PEM electrolytic tank 104 at least reaches 2Mpa, automatically opening the first control valve 109 to enable the hydrogen to enter the gas-water separator 106 and dry and remove impurities in the gas-water separator 106, and when the hydrogen pressure in the gas-water separator 106 reaches 2Mpa and the hydrogen purity reaches 99.99%, starting the hydrogenation gun 112 to hydrogenate the solid hydrogen storage, and in the use process, when the water quantity in the gas-water separator 106 is overlarge, automatically opening the third control valve 111 to discharge the water, thereby guaranteeing the pressure relief and the dryness of the hydrogen in the gas-water separator 106.
In summary, the mobile hydrogenation machine provided by the utility model comprises a shell, and a water tank, a purification cavity, a PEM (PEM) electrolytic tank, a gas-water separator, a power supply and a controller module which are arranged in the shell, wherein a hydrogenation gun is communicated with a hydrogenation gas port of the gas-water separator, so that compressed hydrogen is conveniently injected into an external device, the working state of the hydrogenation machine is monitored in real time by arranging various types of sensors, the reliable running time of the hydrogenation machine and the purity of generated hydrogen are improved, the portable movement of the hydrogenation machine is realized by arranging a movable hub at the bottom of the shell, the hydrogenation efficiency of the solid hydrogen storage is improved compared with that of a fixed hydrogenation station, the hydrogenation of the solid hydrogen storage can be realized at any time and any place, in addition, the device is simple in structure, the components are detachably connected, and the replacement and assembly efficiency is improved. Therefore, the utility model effectively overcomes various defects in the prior art and has high industrial utilization value.
The above embodiments are merely illustrative of the principles of the present utility model and its effectiveness, and are not intended to limit the utility model. Modifications and variations may be made to the above-described embodiments by those skilled in the art without departing from the spirit and scope of the utility model. Accordingly, it is intended that all equivalent modifications and variations of the utility model be covered by the claims, which are within the ordinary skill of the art, be within the spirit and scope of the present disclosure.
Claims (10)
1. A mobile hydrogenator, the mobile hydrogenator comprising at least:
a housing;
the movable hub is positioned at the bottom of the shell;
the water tank is arranged in the shell, comprises a water tank inlet and a water tank outlet, and is further provided with a tank cover at the water tank inlet, and is provided with a water quality sensor, a pressure sensor, a water temperature sensor, a first liquid level sensor and a second liquid level sensor;
the purification cavity is arranged in the shell, positioned below the water tank and communicated with the water tank outlet, comprises a purification cavity outlet, and is filled with a purification medium;
the PEM electrolyzer is arranged in the shell and is positioned below the purification cavity, the PEM electrolyzer comprises a water injection port and a hydrogen outlet, and the water injection port is communicated with the purification cavity outlet;
the gas-water separator is arranged in the shell and comprises a hydrogen inlet, a pressure relief opening and a hydrogenation opening, wherein the hydrogen inlet is communicated with the hydrogen outlet through a pipeline, a first control valve is arranged on the pipeline, the hydrogenation opening is communicated with a hydrogenation gun positioned outside the shell through a pipeline, a second control valve is arranged on the pipeline, the pressure relief opening is positioned at the bottom of the gas-water separator and extends to the outside of the shell, a third control valve is arranged at the pressure relief opening, and a third liquid level sensor and a hydrogen purity sensor are arranged on the gas-water separator;
the direct current power supply is arranged in the shell, and the positive electrode and the negative electrode of the output end of the direct current power supply are respectively and electrically connected with the positive electrode and the negative electrode of the PEM electrolytic tank;
the controller module is respectively in communication connection with the water quality sensor, the pressure sensor, the water temperature sensor, the first liquid level sensor, the second liquid level sensor, the third liquid level sensor and the hydrogen purity sensor.
2. The mobile hydrogenator of claim 1, wherein: the mobile hydrogenation machine further comprises an alarm, and the controller module is electrically connected with a plurality of the alarms.
3. The mobile hydrogenator of claim 1, wherein: the first liquid level sensor and the second liquid level sensor are positioned outside the water tank, the first liquid level sensor is a high liquid level sensor, the second liquid level sensor is a low liquid level sensor, and the third liquid level sensor is positioned outside the gas-water separator, and the third liquid level sensor is a high liquid level sensor.
4. The mobile hydrogenator of claim 1, wherein: the first control valve, the second control valve and the third control valve are all automatic valves.
5. The mobile hydrogenator of claim 1, wherein: the volume of the water tank is not less than 1L and the compressive strength is not less than 2MPa.
6. The mobile hydrogenator of claim 1, wherein: the gas-water separator is internally and sequentially filled with a gas-water separation material, a hydrogen drying material and a hydrogen impurity removal material from bottom to top.
7. The mobile hydrogenator of claim 1, wherein: the volume capacity of the gas-water separator is not less than 500mL, and the compressive strength is not less than 2MPa.
8. The mobile hydrogenator of claim 1, wherein: the water tank, the purification cavity and the PEM electrolytic tank are detachably connected, wherein the fixing mode comprises one or a combination of screw connection, buckle connection and bolt connection.
9. The mobile hydrogenator of claim 1, wherein: the purification medium is detachably connected with the purification cavity so as to facilitate the replacement of the purification medium.
10. The mobile hydrogenator of claim 1, wherein: the gas-water separator is detachably connected with the hydrogen inlet, the pressure relief opening and the hydrogenation opening, wherein the fixing mode comprises one or a combination of threaded connection and buckle connection.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320107622.9U CN219550251U (en) | 2023-02-03 | 2023-02-03 | Movable hydrogenation machine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320107622.9U CN219550251U (en) | 2023-02-03 | 2023-02-03 | Movable hydrogenation machine |
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| CN219550251U true CN219550251U (en) | 2023-08-18 |
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| CN202320107622.9U Active CN219550251U (en) | 2023-02-03 | 2023-02-03 | Movable hydrogenation machine |
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| CN (1) | CN219550251U (en) |
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