CN107575734A - A kind of simple hydrogen gas single stage supercharging purification bulking system and its application method - Google Patents

A kind of simple hydrogen gas single stage supercharging purification bulking system and its application method Download PDF

Info

Publication number
CN107575734A
CN107575734A CN201710855103.XA CN201710855103A CN107575734A CN 107575734 A CN107575734 A CN 107575734A CN 201710855103 A CN201710855103 A CN 201710855103A CN 107575734 A CN107575734 A CN 107575734A
Authority
CN
China
Prior art keywords
hydrogen
pressure
valve
pressure bottle
hydrogen gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201710855103.XA
Other languages
Chinese (zh)
Other versions
CN107575734B (en
Inventor
程宏辉
徐林华
王葵葵
刘晶晶
颜庆云
吴瑛
严凯
陈东雷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yangzhou University
Original Assignee
Yangzhou University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yangzhou University filed Critical Yangzhou University
Priority to CN201710855103.XA priority Critical patent/CN107575734B/en
Publication of CN107575734A publication Critical patent/CN107575734A/en
Application granted granted Critical
Publication of CN107575734B publication Critical patent/CN107575734B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen storage
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P90/00Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
    • Y02P90/45Hydrogen technologies in production processes

Landscapes

  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

The present invention relates to hydrogen to reclaim filling field, particularly a kind of simple hydrogen gas single stage supercharging purification bulking system and its application method.The system includes the parts such as commercially available pressure hydrogen gas cylinder, the first ball valve, first pressure sensor, first check-valve, high-pressure bottle, safety valve, the first temperature transducer, the second temperature transducer, spherical composite hydrogen storage material, electrically heated rod, filter, second pressure sensor, second check-valve, the second ball valve, commercially available pressure hydrogen gas cylinder, circulating water system, magnetic valve, spray equipment, pallet, control system, water tap, and its workflow is broadly divided into cooling suction hydrogen and two processes of hydrogen are put in heating.The present invention have it is versatile, it is safe and efficient, operate simple and convenient, take up an area it is few, it is easy to adjust, while supercharging can purified hydrogen, no running gear, no abrasion, low noise advantages.

Description

A kind of simple hydrogen gas single stage supercharging purification bulking system and its application method
Technical field
The present invention relates to hydrogen to reclaim filling field, particularly a kind of simple hydrogen gas single stage supercharging purification bulking system and its Application method.
Background technology
Hydrogen is widely used in industrial and agricultural production process, the pure hydrogen (volumetric concentration largely used in the market 99.99%), High Purity Hydrogen (volumetric concentration 99.999%) is all full bottle pressure 13MPa or so, and the steel cylinder that volume is 40L is supplied. During using these steel cylinder hydrogen, to ensure the security filled again, national standard (GB 4962-2008, hydrogen Technical regulation safe to use) regulation, the gas in hydrogen cylinder must not be used up, at least retained in bottle more than 0.15MPa (absolute pressure) Pressure, to prevent air from entering gas cylinder.But in practice often due to pressure does not reach numerical value as defined in downstream equipment equipment, Many hydrogen gas cylinder pressure for retracting gas station reach more than 0.5MPa, and even more high, this is a kind of waste for user, is not had There is the economic benefit for having given play to maximum.
The residual hydrogen that the present invention proposes to realize low pressure hydrogen steel cylinder by way of to hydrogen pressurization is to high-pressure hydrogen cylinder Recovery it is filling.But what be can be provided in the market is all mechanical hydrogen gas compressor.These mechanical hydrogen gas compressors Have the disadvantage that:(1) moving component be present, it is necessary to periodic maintenance;(2) there is noise;(3) disposal of pollutants be present;(4) steamed in oil Hydrogen purity can be reduced in the presence of gas;(5) high energy consumption, operating cost are high.Therefore, it is necessary to develop more efficient and using pin To the hydrogen compressibility of property.
The content of the invention
In order to overcome needed existing for mechanical hydrogen gas compressor periodic maintenance, have noise, exist disposal of pollutants, reduce hydrogen The shortcomings of gas purity, it is an object of the invention to provide a kind of safe efficient, compact-sized, output based on metal hydride The high simple hydrogen gas single stage supercharging purification bulking system of hydrogen purity and its application method.
To achieve these goals, the technical scheme is that:
A kind of simple hydrogen gas single stage supercharging purifies bulking system, it is characterised in that the pressure hydrogen gas cylinder of the system passes through spiral shell Line and bulb valve are joined directly together with the first ball valve entrance, the first ball valve outlet by threeway respectively with first pressure sensor and First check-valve entrance is connected, and first check-valve outlet is connected by stainless steel tube with the entrance of high-pressure bottle;On high-pressure bottle Equipped with safety valve, outdoor is led in the outlet of safety valve by plastic flexible pipe;Spherical composite hydrogen storage material is housed inside high-pressure bottle, Electrically heated rod is placed on the horizontal axis position of high-pressure bottle;The first thermometric is placed in the centre and lower surface of high-pressure bottle respectively Sensor and the second temperature transducer;The outlet of high-pressure bottle is connected by stainless steel tube with filter inlet, and filter goes out Mouth is connected by entrance of the threeway respectively with second pressure sensor and second check-valve;The outlet of second check-valve and the second ball The entrance of valve is connected, and the outlet of the second ball valve is directly connected by screw thread and bulb valve with the valve of High Pressure Hydrogen gas cylinder;
The circulating water system of the system is connected by plastic flexible pipe with electromagnetic valve entrance, and electromagnetic valve outlet is soft by plastics Pipe is connected with spray equipment, and the lower section of spray equipment is corresponding with high-pressure bottle, and the lower section of high-pressure bottle is corresponding with pallet, support Disk is connected by plastic flexible pipe with circulating water system.
Described simple hydrogen gas single stage supercharging purification bulking system, the first temperature transducer, the second temperature transducer, electricity add Hot pin, first pressure sensor, second pressure sensor, circulating water system and magnetic valve, pass through cable and control respectively System is connected.
Described simple hydrogen gas single stage supercharging purification bulking system, hydrogen in pressure hydrogen gas cylinder for bulk purity >= 99.99%th, 0.15MPa<Pressure<2MPa, remaining hydrogen through can not be again continuing with after by instrument and equipment;High pressure Hydrogen in hydrogen cylinder is bulk purity >=99.99%, 2MPa<Pressure<13MPa, the hydrogen being still continuing with by instrument and equipment.
Described simple hydrogen gas single stage supercharging purification bulking system, spherical composite hydrogen storage material store up comprising La-Ce-Ni-Al Hydrogen alloy, gas phase SiO2, graphite powder;Wherein, suction hydrogen platform pressure of the La-Ce-Ni-Al hydrogen bearing alloys used at 5 DEG C is 0.12MPa, and the hydrogen platform pressure of putting at 150 DEG C is 14.5MPa, and there is extremely low lag coefficient;The La-Ce-Ni- Al hydrogen bearing alloys can produce fresh surface during hydrogen is put in suction, the foreign gas in fresh adsorption hydrogen, make hydrogen Purity can be lifted further.
Described simple hydrogen gas single stage supercharging purification bulking system, the filtering accuracy of filter is 0.5um.
Described simple hydrogen gas single stage supercharging purification bulking system, circulating water internal system include matching used water Case, evaporator, condenser, compressor, are equipped with liquid level sensor wherein on water tank, water tank passes through internal magnetic valve and the originally fire hose Head is connected, and when high water tank is relatively low, opens internal magnetic valve, running water is supplemented into water tank;Temperature biography is also equipped with water tank Sensor, test the temperature of cooling water;Circulating water system carries out temperature adjustment in 5~20 DEG C of scopes, obtains the cold of different temperatures But water.
Described simple hydrogen gas single stage supercharging purification bulking system, control system carry touch-screen, shown in high-pressure bottle The temperature of heart position and the temperature of high-pressure bottle lower surface, show circulating water system in water tank temperature, and show this three The historical variations curve of individual position temperature;The temperature of recirculated cooling water is set by the touch-screen of control system, control system is led to Cross control of the pid control algorithm realization to circulating water cooling system power;Electrical heating is set by the touch-screen of control system The heating-up temperature of rod, control system realize the control of the heating power of electrically heated rod, heated for controlling temperature when institute by pid control algorithm The temperature of foundation is to be positioned over the temperature that the second temperature transducer of high-pressure bottle lower surface is surveyed;Control system is realized to high pressure The cooling of container and ramp cycle alternately control, so as to realize that supercharging of the pressure hydrogen gas cylinder to High Pressure Hydrogen gas cylinder is filling;Pass through The duration that the touch-screen of control system puts hydrogen to the duration of cooling suction hydrogen and heating sets, to ensure hydrogen storage material Material has sufficiently long time suction hydrogen saturation and dehydrogenation abundant.
Described simple hydrogen gas single stage supercharging purification bulking system, when high-pressure bottle internal pressure>During 15MPa, safety valve Automatically open up, complete pressure release;When the pressure value of first pressure sensor<0.16MPa, the whole canning process that is pressurized terminate, and this is System is stopped, i.e., electrically heated rod stops heating, magnetic valve returns to the closed mode of acquiescence.
Described simple hydrogen gas single stage supercharging purification bulking system, when being heated by electrically heated rod, control system Magnetic valve is closed, so as to which cooling water path is truncated, avoids causing the surface cooling of high-pressure bottle;Sprayed when passing through When shower device cools down to high-pressure bottle, control system stops powering to electrically heated rod to stop heating.
The application method of described simple hydrogen gas single stage supercharging purification bulking system, the purification of simple hydrogen gas single stage supercharging are filling The workflow of system is divided into cooling suction hydrogen and two processes of hydrogen are put in heating;Wherein,
(1) hydrogen is inhaled in cooling includes below scheme:
Control system sends instruction unpack magnetic valve, and the cooling water in circulating water machine enters in spray equipment, cooling water Sprayed from the nozzle in spray equipment, and be injected in the surface of high-pressure bottle, it is cooled down, makes the temperature of high-pressure bottle It is rapid to reduce;With the reduction of high-pressure bottle internal temperature, spherical composite hydrogen storage material starts to inhale hydrogen, causes inside high-pressure bottle Hydrogen Vapor Pressure decrease;When the Hydrogen Vapor Pressure in high-pressure bottle is less than the pressure of pressure hydrogen gas cylinder, first check-valve is certainly Dynamic to open, for hydrogen by being flowed into pressure hydrogen gas cylinder in high-pressure bottle, the spherical composite hydrogen storage material in high-pressure bottle persistently inhales hydrogen, When change of the pressure value in 1 minute of first pressure sensor<During 0.05MPa, that is, think that high-pressure bottle has inhaled hydrogen saturation;Control Thus system processed sends instruction and closes magnetic valve, spray equipment stops spray cooling water, and high-pressure bottle is inhaled hydrogen and terminated;
(2) hydrogen is put in heating includes below scheme:
Control system sends instruction and starts electrically heated rod, realizes the heating to high-pressure bottle, and control system is surveyed according to second The heating power of the real-time adjust automatically electrically heated rod of temperature value and pid algorithm of temperature sensor, with the progress of heating, high pressure-volume The internal temperature of device constantly raises, and the spherical composite hydrogen storage material inside high-pressure bottle starts to be pressurized dehydrogenation, the hydrogen of high-pressure bottle Atmospheric pressure also constantly rise therewith;When the Hydrogen Vapor Pressure of high-pressure bottle is more than the pressure of pressure hydrogen gas cylinder, first check-valve is certainly It is dynamic to close, prevent the hydrogen of high-pressure bottle to be back in pressure hydrogen gas cylinder, when the Hydrogen Vapor Pressure of high-pressure bottle is more than high pressure hydrogen During the pressure of bottle, second check-valve is automatically opened up, and hydrogen is entered in High Pressure Hydrogen gas cylinder by high-pressure bottle;With holding for high-pressure bottle It is continuous to put hydrogen, when the pressure value of second pressure sensor changed in 1 minute<During 0.05MPa, that is, think high-pressure bottle dehydrogenation Fully;Thus control system sends instruction stopping electrically heated rod and continues to heat, the internal temperature of high-pressure bottle is gradual, therewith hydrogen Pressure also gradually reduces;When the Hydrogen Vapor Pressure of high-pressure bottle is less than the Hydrogen Vapor Pressure of High Pressure Hydrogen gas cylinder, second check-valve is automatic Close, to avoid hydrogen in High Pressure Hydrogen gas cylinder from being back in high-pressure bottle;Now, the heating of high-pressure bottle is put hydrogen process and terminated.
The present invention design philosophy be:
Van ' t Hoff relations be present between the hydrogen pressure and temperature of metal hydride:Δ in formula H0、ΔS0The standard enthalpy change and Entropy Changes respectively reacted, within the scope of larger temperature, ln PH2Linearly closed substantially with 1/T System.At different temperatures, the difference of test puts hydrogen pressure, and the enthalpy of formation Δ H of hydrogen bearing alloy can be calculated according to slope0, as The important indicator of hydrogen compression material selection, the enthalpy of formation of hydride determine the Important Parameters of compression efficiency and compression ratio.Using gold It is exactly material is inhaled hydrogen at a lower temperature that category hydride, which carries out hydrogen compression, releases heat when inhaling hydrogen, then passes through heating Temperature is improved, is raised so as to the pressure platform of hydrogen storage material, hydrogen storage material absorbs heat, releases High Pressure Hydrogen.Whole process only needs Want heat energy to input, put one circulation of hydrogen by inhaling, it is possible to which hydrogen is compressed to elevated pressures from lower pressure.In addition, metal Hydride puts hydrogen process in suction can occur efflorescence, produce substantial amounts of fresh surface, these fresh activity surfaces can be with adsorbed hydrogen Middle impurity, enables hydrogen purity effectively to be lifted.The present invention is based on above-mentioned metal hydride supercharging and cleaning principle exploitation Simple hydrogen gas single stage supercharging purification bulking system.
The invention has the advantages that and beneficial effect:
(1) present invention is versatile, safe and efficient, operates simple and convenient;
(2) topology layout of the present invention is rationally compact, takes up an area few;
(3) pressure ratio of the present invention and the adjustable range of displacement are big, easy to adjust;
(4) present invention is in supercharging Simultaneous purification hydrogen;
(5) present system annex is few, simple in construction, reliability is high, is easy to safeguard;
(6) present invention without running gear, without abrasion, the low of noise.
Brief description of the drawings
Simple hydrogen gas supercharging purification bulking system structural representation in Fig. 1 embodiment of the present invention.In figure, 1 low pressure hydrogen Bottle;2 first ball valves;3 first pressure sensors;4 first check-valves;5 high-pressure bottles;6 safety valves;7 first temperature transducers;8 Second temperature transducer;9 composite hydrogen storage materials;10 electrically heated rods;11 filters;12 second pressure sensors;13 second non-returns Valve;14 second ball valves;15 High Pressure Hydrogen gas cylinders;16 circulating water systems;17 magnetic valves;18 spray equipments;19 pallets;20 running water Tap;21 control systems.
Hydrogen flow chart is inhaled in cooling in Fig. 2 embodiment of the present invention.
Hydrogen flow chart is put in heating in Fig. 3 embodiment of the present invention.
Embodiment
The present invention is further described below in conjunction with the accompanying drawings.
As shown in figure 1, pressure hydrogen gas cylinder 1 is direct by W21.8-14LHF screw threads and bulb valve and the entrance of the first ball valve 2 It is connected.The outlet of first ball valve 2 is connected with first pressure sensor 3 and the entrance of first check-valve 4 respectively by threeway, the first non-return The outlet of valve 4 is connected by stainless steel tube with the entrance of high-pressure bottle 5.Safety valve 6, the outlet of safety valve 6 are housed on high-pressure bottle 5 Outdoor is led to by plastic flexible pipe.When the internal pressure of high-pressure bottle 5>During 15MPa, safety valve 6 automatically opens up, and completes pressure release to keep away Exempt from that security incident occurs because maloperation or equipment fault cause container serious overcompression.The inside of high-pressure bottle 5 is equipped with spherical Composite hydrogen storage material 9, the spherical composite hydrogen storage material 9 include La-Ce-Ni-Al hydrogen bearing alloys, gas phase SiO2, graphite powder, can be with Ensure good heat and mass effect, there is good suction hydrogen desorption kineticses performance and antifading, minimum gas can be achieved Flow resistance and maximum loadings, and the phenomenon of efflorescence and string powder will not be caused due to long-term use of, it is to realize that hydrogen increases The core material of pressure.Wherein, suction hydrogen platform pressure of the La-Ce-Ni-Al hydrogen bearing alloys used at 5 DEG C is 0.12MPa (absolute pressure), And the hydrogen platform pressure of putting at 150 DEG C is 14.5MPa (absolute pressure), and there is extremely low lag coefficient.The La-Ce-Ni-Al Hydrogen bearing alloy can produce many fresh surfaces during hydrogen is put in suction, and these fresh surfaces can be with the impurity gas in adsorbed hydrogen Body, the purity of hydrogen is set further to be lifted.
Electrically heated rod 10 is placed on the horizontal axis position of high-pressure bottle 5, for heating spherical composite hydrogen storage material 9. The first temperature transducer 7 and the second temperature transducer 8 are placed in the centre and lower surface of high-pressure bottle 5 respectively, are respectively used to test The temperature of among high-pressure bottle 5 and lower surface.The outlet of high-pressure bottle 5 is connected by stainless steel tube with the entrance of filter 11, should The filtering accuracy of filter 11 is 0.5 μm, to avoid powder that may be present from causing downstream gas circuit breakdown pressure to pass into pipeline The fluidic component such as sensor and valve.The outlet of filter 11 by threeway respectively with second pressure sensor 12 and second check-valve 13 entrance is connected, and the outlet of second check-valve 13 is connected with the entrance of the second ball valve 14, and the outlet of the second ball valve 14 is directly logical Cross W21.8-14LHF screw threads and bulb valve is connected with the valve of High Pressure Hydrogen gas cylinder 15, second check-valve 13 mainly avoids can Can occur High Pressure Hydrogen gas cylinder 15 in backflow phenomenon from hydrogen to high-pressure bottle 5.First ball valve 2 and the second ball valve 14 are mainly Realize that internal system is completely isolated in air, avoids oxygen and vapor when hydrogen single stage supercharging purification bulking system is vacant Entrance and cause La-Ce-Ni-Al hydrogen bearing alloys oxidation cause performance degradation.
Wherein, the hydrogen in commercially available pressure hydrogen gas cylinder 1 is bulk purity >=99.99%, 0.15MPa<Pressure<2MPa is (absolutely Pressure), the remaining hydrogen through can not be again continuing with after by instrument and equipment;Hydrogen in commercially available High Pressure Hydrogen gas cylinder 15 is Bulk purity >=99.99%, 2MPa<Pressure<13MPa's (absolute pressure), the hydrogen that can be still continuing with by instrument and equipment.First The range of pressure sensor 3 is the Hydrogen Vapor Pressure that 0~3MPa (absolute pressure) is used in indication low-voltage hydrogen cylinder 1, and second pressure senses The range of device is that 0~16MPa (absolute pressure) is used to indicate the Hydrogen Vapor Pressure in high-pressure bottle 5.
Circulating water system 16 is connected by plastic flexible pipe with the entrance of magnetic valve 17, and the outlet of magnetic valve 17 passes through plastic flexible pipe It is connected with spray equipment 18, the lower section of spray equipment 18 is corresponding with high-pressure bottle 5, lower section and the phase of pallet 19 of high-pressure bottle 5 Corresponding, pallet 19 is used for the cold water for catching the drippage of spray equipment 18.Hole is arranged at the bottom of pallet 19, cold with circulating by plastic flexible pipe Water system 16 is connected, and makes cooling water backflow cooling to reuse.Include inside circulating water system 16 matching used Water tank, evaporator, condenser, compressor, are equipped with liquid level sensor wherein on water tank, water tank passes through internal magnetic valve and running water Tap 20 is connected, and when high water tank is relatively low, opens internal magnetic valve, running water is supplemented into water tank.Temperature is also equipped with water tank Sensor is spent, the temperature of cooling water can be tested.Circulating water system 16 can carry out temperature adjustment in 5~20 DEG C of scopes, obtain The cooling water of different temperatures is obtained, general default setting is 5 DEG C.Equally distributed (operating) water nozzle is housed on spray equipment 18, can be made Cooling water is uniformly sprayed at the surface of high-pressure bottle 5, it is cooled rapidly, completes to inhale hydrogen process.
First temperature transducer 7, the second temperature transducer 8, electrically heated rod 10, first pressure sensor 3, second pressure pass Sensor 12, circulating water system 16 and magnetic valve 17, it is connected respectively by cable with control system 21.The band of control system 21 There is touch-screen, the temperature of the center of high-pressure bottle 5 and the temperature of the lower surface of high-pressure bottle 5 can be shown, circulation can be shown The temperature of water tank in chilled water system 16, and the historical variations curve of these three position temperature can be shown.Pass through control system 21 touch-screen can set the temperature of recirculated cooling water, and control system 21 is realized to circulating water system by pid control algorithm The control of system refrigeration work consumption.The heating-up temperature of electrically heated rod 10 can be set by the touch-screen of control system 21, general acquiescence Heating-up temperature be set as 150 DEG C.Control system 21 realizes the control to the heating power of electrically heated rod 10 by pid control algorithm System, the temperature of heated for controlling temperature when institute foundation is to be positioned over the temperature that second temperature transducer 8 on the surface of high-pressure bottle 5 is surveyed, with Ensure that the temperature of all spherical composite hydrogen storage materials 9 in high-pressure bottle 5 is on the hydrogen discharging temperature of setting, make high-pressure bottle 5 entirety can fully put hydrogen.When being heated by electrically heated rod 10, control system 21 makes magnetic valve 17 be in closing shape State, so as to which cooling water path is truncated, avoid causing the surface cooling of high-pressure bottle 5.When by spray equipment 18 to high pressure-volume When device 5 is cooled down, control system 21 stops powering to electrically heated rod 10 to stop heating.When being cooled down to high-pressure bottle 5, The test temperature for cooling down temperature control institute foundation is to be positioned over the temperature that first temperature transducer 7 at the center of high-pressure bottle 5 is surveyed, to protect The temperature of all spherical composite hydrogen storage materials 9 is under the suction hydrogen temperature of setting in card high-pressure bottle 5, makes high-pressure bottle 5 Entirety can fully inhale hydrogen.The touch-screen of control system 21 can show first pressure sensor 3 and second pressure sensor 12 Pressure value, and the historical variations curve of the two position pressure can be shown.Control system 21 is realized to high-pressure bottle 5 Cooling and ramp cycle alternately control, so as to realize that repeatedly supercharging of the pressure hydrogen gas cylinder 1 to High Pressure Hydrogen gas cylinder 15 is filling.Pass through The duration that the touch-screen of control system 21 can put hydrogen to the duration of cooling suction hydrogen and heating sets, to ensure Spherical composite hydrogen storage material 9 has sufficiently long time suction hydrogen saturation and dehydrogenation abundant, typically gives tacit consent to cool time for 5 minutes, writes from memory The time for recognizing heating is 5 minutes.When the pressure value of first pressure sensor 3<0.16MPa, the whole canning process that is pressurized terminate, should System stalls, i.e. electrically heated rod 10 stopping heating, magnetic valve 17 return to the closed mode of acquiescence.
In the present invention, the workflow of simple hydrogen gas single stage supercharging purification bulking system is broadly divided into cooling and inhales hydrogen and heating Put two processes of hydrogen.Be pressurized it is filling before, first ensure that the air inlet of hydrogen single stage supercharging purification bulking system with The valve of pressure hydrogen gas cylinder is connected, and air tight, the gas outlet of hydrogen single stage supercharging purification bulking system and High Pressure Hydrogen The valve of gas cylinder is connected, and air tight.Pressure hydrogen gas cylinder and the High Pressure Hydrogen gas cylinder bottle valve of itself are opened, slowly opens the One ball valve, quick flow that may be present is avoided to be impacted to caused by high-pressure bottle.The second ball valve is slowly opened, avoids depositing Quick flow impacted to caused by High Pressure Hydrogen gas cylinder.
As shown in Fig. 2 simple hydrogen gas single stage supercharging purification bulking system is at work, the drop of high-pressure bottle 5 is carried out first Temperature inhales hydrogen, ensures that its internal La-Ce-Ni-Al hydrogen bearing alloy can fully inhale hydrogen, its main working process is:
Control system 21 sends instruction unpack magnetic valve 17, and the cooling water in circulating water machine 16 enters spray equipment 18 In, cooling water is sprayed from the nozzle in spray equipment 18, and is injected in the surface of high-pressure bottle 5, and it is cooled down, makes height The temperature of pressure vessel 5 reduces rapidly.With the reduction of the internal temperature of high-pressure bottle 5, spherical composite hydrogen storage material 9 starts to inhale hydrogen, Cause the Hydrogen Vapor Pressure inside high-pressure bottle 5 also to follow van ' t Hoff relations to decrease.Hydrogen in high-pressure bottle 5 When pressure is less than the pressure of pressure hydrogen gas cylinder 1, first check-valve 4 automatically opens up, and hydrogen in pressure hydrogen gas cylinder 1 by flowing into high pressure-volume In device 5, the spherical composite hydrogen storage material 9 in high-pressure bottle 5 persistently inhales hydrogen, when the pressure value of first pressure sensor 3 was at 1 minute Interior change<During 0.05MPa (absolute pressure), that is, think that high-pressure bottle 5 has inhaled hydrogen saturation.Thus control system 21 sends instruction and closed Magnetic valve 17, spray equipment 18 stop spray cooling water, and high-pressure bottle 5 is inhaled hydrogen and terminated.
As shown in figure 3, it is exactly that hydrogen is put in supercharging that simple hydrogen gas single stage supercharging, which purifies bulking system after hydrogen is fully inhaled, it is led The workflow is wanted to be:
Control system 21 sends instruction startup electrically heated rod 10 first, realizes the heating to high-pressure bottle 5, control system 21 According to the temperature value of the second temperature transducer 8 and the heating power of the real-time adjust automatically electrically heated rod 10 of pid algorithm;With heating Progress, the internal temperature of high-pressure bottle 5 constantly raises, and it is de- that the spherical composite hydrogen storage material 9 inside high-pressure bottle 5 starts supercharging Hydrogen, van ' t Hoff relations can be also followed between the Hydrogen Vapor Pressure and temperature of high-pressure bottle 5 and are constantly raised therewith.Work as high-pressure bottle When 5 Hydrogen Vapor Pressure is more than the pressure of pressure hydrogen gas cylinder 1, first check-valve 4 is closed automatically, can prevent the hydrogen of high-pressure bottle 5 Gas is back in pressure hydrogen gas cylinder 1;When the Hydrogen Vapor Pressure of high-pressure bottle 5 is more than the pressure of High Pressure Hydrogen gas cylinder 15, the second non-return Valve 13 is automatically opened up, and hydrogen is entered in High Pressure Hydrogen gas cylinder 15 by high-pressure bottle 5.With the type discharge hydrogen of high-pressure bottle 5, when second The pressure value of pressure sensor 12 changed in 1 minute<During 0.05MPa, that is, thinking high-pressure bottle 5, dehydrogenation is abundant.Control Thus system 21 sends instruction stopping electrically heated rod 10 and continues to heat, the internal temperature of high-pressure bottle 5 is gradual, therewith Hydrogen Vapor Pressure Also gradually reduce.When the Hydrogen Vapor Pressure of high-pressure bottle 5 is less than the Hydrogen Vapor Pressure of High Pressure Hydrogen gas cylinder, second check-valve 13 is closed automatically Close, to avoid hydrogen in High Pressure Hydrogen gas cylinder 15 from being back in high-pressure bottle 5.Now, hydrogen process knot is put in the heating of high-pressure bottle 5 Beam.

Claims (10)

1. a kind of simple hydrogen gas single stage supercharging purifies bulking system, it is characterised in that the pressure hydrogen gas cylinder of the system passes through screw thread Be joined directly together with bulb valve and the first ball valve entrance, the outlet of the first ball valve by threeway respectively with first pressure sensor and the One non-return valve inlet is connected, and first check-valve outlet is connected by stainless steel tube with the entrance of high-pressure bottle;Filled on high-pressure bottle There is safety valve, outdoor is led in the outlet of safety valve by plastic flexible pipe;Spherical composite hydrogen storage material is housed inside high-pressure bottle, electricity Heating rod is placed on the horizontal axis position of high-pressure bottle;The first thermometric biography is placed in the centre and lower surface of high-pressure bottle respectively Sensor and the second temperature transducer;The outlet of high-pressure bottle is connected by stainless steel tube with filter inlet, the outlet of filter It is connected by entrance of the threeway respectively with second pressure sensor and second check-valve;The outlet of second check-valve and the second ball valve Entrance be connected, the outlet of the second ball valve is directly connected by screw thread and bulb valve with the valve of High Pressure Hydrogen gas cylinder;
The circulating water system of the system is connected by plastic flexible pipe with electromagnetic valve entrance, electromagnetic valve outlet by plastic flexible pipe with Spray equipment is connected, and the lower section of spray equipment is corresponding with high-pressure bottle, and the lower section of high-pressure bottle is corresponding with pallet, and pallet leads to Plastic flexible pipe is crossed with circulating water system to be connected.
2. simple hydrogen gas single stage supercharging according to claim 1 purifies bulking system, it is characterised in that the first temperature transducers Device, the second temperature transducer, electrically heated rod, first pressure sensor, second pressure sensor, circulating water system and electromagnetism Valve, it is connected respectively by cable with control system.
3. simple hydrogen gas single stage supercharging according to claim 1 purifies bulking system, it is characterised in that in pressure hydrogen gas cylinder Hydrogen for bulk purity >=99.99%, 0.15MPa<Pressure<2MPa, can not again be continued after use by instrument and equipment The remaining hydrogen used;Hydrogen in High Pressure Hydrogen gas cylinder is bulk purity >=99.99%, 2MPa<Pressure<13MPa, still by instrument The hydrogen that equipment is continuing with.
4. simple hydrogen gas single stage supercharging according to claim 1 purifies bulking system, it is characterised in that spherical composite hydrogen occluding Material includes La-Ce-Ni-Al hydrogen bearing alloys, gas phase SiO2, graphite powder;Wherein, La-Ce-Ni-Al hydrogen bearing alloys used are at 5 DEG C When suction hydrogen platform pressure be 0.12MPa, and press putting at 150 DEG C be 14.5MPa by hydrogen platform, and has extremely low hysteresis Coefficient;The La-Ce-Ni-Al hydrogen bearing alloys can produce fresh surface during hydrogen is put in suction, miscellaneous in fresh adsorption hydrogen Matter gas, the purity of hydrogen is set further to be lifted.
5. simple hydrogen gas single stage supercharging according to claim 1 purifies bulking system, it is characterised in that the filtering of filter Precision is 0.5um.
6. simple hydrogen gas single stage supercharging according to claim 1 purifies bulking system, it is characterised in that circulating water system Inside includes matching used water tank, evaporator, condenser, compressor, and liquid level sensor is housed wherein on water tank, and water tank leads to Cross internal magnetic valve with water tap to be connected, when high water tank is relatively low, opens internal magnetic valve, supplemented originally into water tank Water;Temperature sensor is also equipped with water tank, tests the temperature of cooling water;Circulating water system enters trip temperature in 5~20 DEG C of scopes Regulation, obtain the cooling water of different temperatures.
7. simple hydrogen gas single stage supercharging according to claim 2 purifies bulking system, it is characterised in that control system carries Touch-screen, the temperature of display high-pressure bottle center and the temperature of high-pressure bottle lower surface, show circulating water system reclaimed water The temperature of case, and show the historical variations curve of these three position temperature;It is cold by the touch-screen setting circulation of control system But the temperature of water, control system realize the control to circulating water cooling system power by pid control algorithm;It is by controlling The heating-up temperature of the touch-screen setting electrically heated rod of system, control system realize the heating work(of electrically heated rod by pid control algorithm The control of rate, the temperature of heated for controlling temperature when institute foundation are to be positioned over the temperature that the second temperature transducer of high-pressure bottle lower surface is surveyed Degree;Cooling and ramp cycle of the control system realization to high-pressure bottle alternately control, so as to realize pressure hydrogen gas cylinder to high pressure The supercharging of hydrogen cylinder is filling;The duration of hydrogen is inhaled to cooling by the touch-screen of control system and the duration of hydrogen is put in heating Set, to ensure that hydrogen storage material has sufficiently long time suction hydrogen saturation and dehydrogenation abundant.
8. simple hydrogen gas single stage supercharging according to claim 1 purifies bulking system, it is characterised in that when in high-pressure bottle Portion's pressure>During 15MPa, safety valve automatically opens up, and completes pressure release;When the pressure value of first pressure sensor<0.16MPa, entirely Supercharging canning process terminates, and the system stalls, i.e. electrically heated rod stopping heating, magnetic valve return to the closing shape of acquiescence State.
9. simple hydrogen gas single stage supercharging according to claim 2 purifies bulking system, it is characterised in that when passing through electrical heating When rod is heated, control system is closed magnetic valve, so as to which cooling water path is truncated, avoids causing high pressure-volume The surface cooling of device;When being cooled down by spray equipment to high-pressure bottle, control system stop to electrically heated rod power with Stop heating.
10. the application method of the simple hydrogen gas single stage supercharging purification bulking system described in a kind of one of claim 1 to 9, it is special Sign is that the workflow of simple hydrogen gas single stage supercharging purification bulking system is divided into cooling suction hydrogen and two processes of hydrogen are put in heating; Wherein,
(1) hydrogen is inhaled in cooling includes below scheme:
Control system sends instruction unpack magnetic valve, and the cooling water in circulating water machine enters in spray equipment, and cooling water is from spray Nozzle in shower device is sprayed, and is injected in the surface of high-pressure bottle, and it is cooled down, makes the temperature of high-pressure bottle rapid Reduce;With the reduction of high-pressure bottle internal temperature, spherical composite hydrogen storage material starts to inhale hydrogen, causes the hydrogen inside high-pressure bottle Atmospheric pressure decreases;When the Hydrogen Vapor Pressure in high-pressure bottle is less than the pressure of pressure hydrogen gas cylinder, first check-valve is beaten automatically Open, for hydrogen by being flowed into pressure hydrogen gas cylinder in high-pressure bottle, the spherical composite hydrogen storage material in high-pressure bottle persistently inhales hydrogen, when the Change of the pressure value of one pressure sensor in 1 minute<During 0.05MPa, that is, think that high-pressure bottle has inhaled hydrogen saturation;Control system Thus system sends instruction and closes magnetic valve, spray equipment stops spray cooling water, and high-pressure bottle is inhaled hydrogen and terminated;
(2) hydrogen is put in heating includes below scheme:
Control system sends instruction and starts electrically heated rod, realizes the heating to high-pressure bottle, control system passes according to the second thermometric The heating power of the real-time adjust automatically electrically heated rod of temperature value and pid algorithm of sensor, with the progress of heating, high-pressure bottle Internal temperature constantly raises, and the spherical composite hydrogen storage material inside high-pressure bottle starts to be pressurized dehydrogenation, the hydrogen pressure of high-pressure bottle Power also constantly rise therewith;When the Hydrogen Vapor Pressure of high-pressure bottle is more than the pressure of pressure hydrogen gas cylinder, first check-valve is closed automatically Close, prevent the hydrogen of high-pressure bottle to be back in pressure hydrogen gas cylinder, when the Hydrogen Vapor Pressure of high-pressure bottle is more than High Pressure Hydrogen gas cylinder During pressure, second check-valve is automatically opened up, and hydrogen is entered in High Pressure Hydrogen gas cylinder by high-pressure bottle;With the type discharge of high-pressure bottle Hydrogen, when the pressure value of second pressure sensor changed in 1 minute<During 0.05MPa, that is, think that high-pressure bottle fill by dehydrogenation Point;Thus control system sends instruction stopping electrically heated rod and continues to heat, the internal temperature of high-pressure bottle is gradual, therewith hydrogen pressure Power also gradually reduces;When the Hydrogen Vapor Pressure of high-pressure bottle is less than the Hydrogen Vapor Pressure of High Pressure Hydrogen gas cylinder, second check-valve is closed automatically Close, to avoid hydrogen in High Pressure Hydrogen gas cylinder from being back in high-pressure bottle;Now, the heating of high-pressure bottle is put hydrogen process and terminated.
CN201710855103.XA 2017-09-20 2017-09-20 Simple hydrogen single-stage pressurizing, purifying and filling system and using method thereof Active CN107575734B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710855103.XA CN107575734B (en) 2017-09-20 2017-09-20 Simple hydrogen single-stage pressurizing, purifying and filling system and using method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710855103.XA CN107575734B (en) 2017-09-20 2017-09-20 Simple hydrogen single-stage pressurizing, purifying and filling system and using method thereof

Publications (2)

Publication Number Publication Date
CN107575734A true CN107575734A (en) 2018-01-12
CN107575734B CN107575734B (en) 2022-10-18

Family

ID=61032982

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710855103.XA Active CN107575734B (en) 2017-09-20 2017-09-20 Simple hydrogen single-stage pressurizing, purifying and filling system and using method thereof

Country Status (1)

Country Link
CN (1) CN107575734B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112158804A (en) * 2020-09-29 2021-01-01 扬州大学 Method for manufacturing hydrogen supply device
CN113915525A (en) * 2021-10-29 2022-01-11 江苏氢枫能源装备有限公司 Solid hydrogen-storing hydrogen adsorbing and releasing device
CN114017669A (en) * 2021-11-23 2022-02-08 安徽安凯汽车股份有限公司 Hydrogen fuel cell passenger car hydrogenation supercharging device

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001173899A (en) * 1999-12-22 2001-06-29 Denso Corp Hydrogen supplying device
US20150047503A1 (en) * 2013-08-19 2015-02-19 Uop Llc Enhanced hydrogen recovery
CN105202365A (en) * 2015-09-17 2015-12-30 北京有色金属研究总院 Metal hydride hydrogen storage tank circulation hydrogen inflation and deflation device and method
CN106567814A (en) * 2015-10-13 2017-04-19 北京浩运金能科技有限公司 Heat self-balancing metal hydride hydrogen supercharging device
CN106770397A (en) * 2016-11-30 2017-05-31 扬州大学 A kind of hydrogen storage material original position high pressure inhales the portable test arrangement for putting hydrogen synchrotron radiation X-ray powder diffraction
CN206447564U (en) * 2017-01-10 2017-08-29 中国工程物理研究院材料研究所 A kind of high pressure hydrogen feedway

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001173899A (en) * 1999-12-22 2001-06-29 Denso Corp Hydrogen supplying device
US20150047503A1 (en) * 2013-08-19 2015-02-19 Uop Llc Enhanced hydrogen recovery
CN105202365A (en) * 2015-09-17 2015-12-30 北京有色金属研究总院 Metal hydride hydrogen storage tank circulation hydrogen inflation and deflation device and method
CN106567814A (en) * 2015-10-13 2017-04-19 北京浩运金能科技有限公司 Heat self-balancing metal hydride hydrogen supercharging device
CN106770397A (en) * 2016-11-30 2017-05-31 扬州大学 A kind of hydrogen storage material original position high pressure inhales the portable test arrangement for putting hydrogen synchrotron radiation X-ray powder diffraction
CN206447564U (en) * 2017-01-10 2017-08-29 中国工程物理研究院材料研究所 A kind of high pressure hydrogen feedway

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112158804A (en) * 2020-09-29 2021-01-01 扬州大学 Method for manufacturing hydrogen supply device
CN112158804B (en) * 2020-09-29 2023-08-22 扬州大学 Method for manufacturing hydrogen supply device
CN113915525A (en) * 2021-10-29 2022-01-11 江苏氢枫能源装备有限公司 Solid hydrogen-storing hydrogen adsorbing and releasing device
CN113915525B (en) * 2021-10-29 2022-08-23 江苏氢枫能源装备有限公司 Solid hydrogen-storing hydrogen adsorbing and releasing device
CN114017669A (en) * 2021-11-23 2022-02-08 安徽安凯汽车股份有限公司 Hydrogen fuel cell passenger car hydrogenation supercharging device

Also Published As

Publication number Publication date
CN107575734B (en) 2022-10-18

Similar Documents

Publication Publication Date Title
CN107575734A (en) A kind of simple hydrogen gas single stage supercharging purification bulking system and its application method
CN209745517U (en) Low-temperature liquid drop impact rigid wall surface experimental device
CN107726040A (en) A kind of cryogenic propellant storage tank with pressure control device
CN110442160A (en) A kind of air stable-pressure device for closed circulating cooling system
CN207196073U (en) A kind of simple hydrogen gas single stage supercharging purifies bulking system
CN107726656A (en) The refrigerant heat pump system of single twin-stage conversion can be carried out
CN106196793A (en) A kind of removable ice machine
CN207585127U (en) It can carry out the transcritical refrigerant heat pump assembly of single twin-stage conversion
CN203248988U (en) Vapor zero discharge treatment system of LNG receiving station
CN104406324B (en) Improved two-stage ejection type refrigerating system
CN106744957B (en) A kind of pump pressure type dry-ice machine
CN104132239B (en) A kind of cryogenic gas condensation cycle system and method
CN109984836A (en) Cryoablation system
CN204787520U (en) Energy -efficient refrigerator of rivers
CN204345957U (en) BOG cold energy utilization device
CN203717342U (en) High-pressure jet enthalpy-increase scroll compressor
CN209196539U (en) A kind of receiving station&#39;s LNG storage facilities
CN210718189U (en) High-efficient refrigeration plant of carbon dioxide
CN209672900U (en) A kind of more tube sheet leakage-proof petrochemical industry condensers
CN207493619U (en) A kind of mixed organization for mixing liquid carbon dioxide and combined polyether
CN106288655A (en) Liquid nitrogen tank emptying low temperature nitrogen is utilized to make the air precooler of low-temperature receiver
CN203672047U (en) Recovery device for heptafluoropropane
CN110530044A (en) A kind of high-efficiency carbon dioxide refrigeration equipment
CN112129040A (en) Liquid xenon cooling and xenon reliquefaction skid-mounted device and method thereof
CN209512379U (en) A kind of device with ammonia heat pump refrigerating recycling dry ice gas phase

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant