CN206467720U - One proton exchanging film fuel battery air water fetching device - Google Patents
One proton exchanging film fuel battery air water fetching device Download PDFInfo
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- CN206467720U CN206467720U CN201720100758.1U CN201720100758U CN206467720U CN 206467720 U CN206467720 U CN 206467720U CN 201720100758 U CN201720100758 U CN 201720100758U CN 206467720 U CN206467720 U CN 206467720U
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- water
- air
- proton exchange
- evaporator
- gas
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- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
-
- 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
- Y02E60/50—Fuel cells
Abstract
The utility model discloses a proton exchanging film fuel battery air water fetching device, including proton exchange film fuel battery system, vapor compression type refrigerating system, water vapor condenser, steam-water separator and water treatment system.The proton exchange film fuel battery system generates direct current, and driving vapor compression type refrigerating system work obtains low temperature, so as to condense the vapor in air in the cold drawing evaporator surface of refrigeration system；Meanwhile, the weary gas of air of the pile discharge of the proton exchange film fuel battery system is condensed into steam water interface when by water vapor condenser, and is separated into water and gas by steam-water separator, so as to reach the purpose for reclaiming fuel cell reaction water.Water vapor condensation in vapor in air and the weary gas of the air of fuel cell exhaust is aqueous water by the utility model synthesis, and the yield of water is greatly improved, and the supply in emergency circumstances drinking water provides effective guarantee.
Description
Technical field
The utility model is related to field of fuel cell technology, more particularly to a proton exchanging film fuel battery air water-intaking
Device.
Background technology
On desert, island and other places, how to obtain fresh water is an important topic.In some occasions, the deposit of fuel is sufficient,
But the supply shortage of fresh water, accordingly, it is considered to significant come preparing fresh using a part of fuel.
The content of the invention
In view of this, embodiment of the present utility model provides one kind and supplies fuel cell power generation with fuel, and then obtains
The Proton Exchange Membrane Fuel Cells air water fetching device of fresh water.
Embodiment of the present utility model provides a proton exchanging film fuel battery air water fetching device, including proton exchange
Film fuel battery system, vapor compression type refrigerating system, water vapor condenser and steam-water separator, the pem fuel
Battery system generates direct current, and the direct current is converted into stable DC electricity, the stable DC electric drive steam compression type
Refrigeration system works, and the weary gas of air after the proton exchange film fuel battery system generation direct current is discharged to water vapor condenser
In, the weary gas of air is condensed into steam water interface, and the steam water interface is separated into water and gas by steam-water separator, institute
State water to flow out from the bottom of steam-water separator, the gas flows out from the top of steam-water separator, and is discharged into air.
Further, the proton exchange film fuel battery system includes hydrogen supply loop, air supply loop, proton friendship
Film fuel cell electric piling and DC-DC converter are changed, the hydrogen supply loop and air supply loop are all connected with proton friendship
Film fuel cell electric piling is changed, the hydrogen supply loop supplies hydrogen, and air, hydrogen and air are supplied in the air supply loop
In oxygen reacted in proton exchange film fuel cell electric piling generation direct current, the DC-DC converter will be straight
Stream electricity is converted into stable DC electricity, and remaining trace hydrogen is discharged in air through the first magnetic valve after reaction.
Further, the hydrogen supply loop includes high-pressure hydrogen storage, pressure-reducing valve, check valve, hand stop valve and prevented
Quick-fried magnetic valve, the high-pressure hydrogen storage, pressure-reducing valve, check valve, hand stop valve and explosion-proof solenoid valve are sequentially connected, hydrogen from
High-pressure hydrogen storage comes out, and sequentially passes through pressure-reducing valve, check valve, hand stop valve and explosion-proof solenoid valve and is fired into PEM
Expect battery pile；The air supply loop includes air cleaner and Air pressurizer, the air cleaner and air
Supercharging device is sequentially connected, and air enters Air pressurizer after air cleaner is handled, and the Air pressurizer will
Air boosts, and sends into proton exchange film fuel cell electric piling.
Further, the steam-water separator is whirlwind separator, and the steam water interface is from the top of whirlwind separator
The tangential inflow of portion's circumference, the steam water interface rotates at a high speed in the presence of cyclone separator air-flow, and the big water of density exists
Barrel is thrown toward under centrifugal action, and the bottom for falling to flowing to cyclone separator along barrel under gravity is flowed out, density
Small gas cyclone separator internal contraction and to center flow, secondary vortex flow is upwardly formed, from the top of cyclone separator
Flow out in portion.
Further, the vapor compression type refrigerating system includes direct current refrigeration compressor, evaporator, restricting element and condensation
Device, the direct current refrigeration compressor, evaporator, restricting element and condenser are sequentially connected under composition loop, the evaporator
Side is provided with water treatment system, stable DC electric drive direct current refrigeration compressor operating, and direct current refrigeration compressor is by refrigerant
Gas compression is high temperature and high pressure gas, and the HTHP gas enters condenser, and the HTHP gas is condensed within the condenser
Into high temperature high pressure liquid, the high temperature high pressure liquid flows through the gas-liquid mixture that restricting element is changed into low-temp low-pressure, the gas-liquid
Mixture flows into evaporator, and the gas-liquid mixture absorbs the heat of evaporator outside air in evaporator, and evaporates again
For refrigerant gas, the air entry of the direct current refrigeration compressor sucks refrigerant gas in direct current refrigeration compressor, refrigeration
Agent gas is compressed again in direct current refrigeration compressor, and the air setting on the outside of the evaporator is into the globule, and the globule exists
Dripped in the presence of gravity in the water treatment system below evaporator.
Further, the side of evaporator is provided with fan, the outside of the fans drive air flow evaporator, the steam
Compression-type refrigerating system also includes device for drying and filtering, and the device for drying and filtering is located between condenser and restricting element, described dry
Impurity and moisture in dry filter filtering high temperature highly pressurised liquid.
Further, the condenser is refrigerant-water- to-water heat exchanger, and the restricting element is capillary, heating power expansion valve or electricity
Sub- expansion valve, the evaporator is cold drawing evaporator, and the cold drawing evaporator includes flat board and refrigerant flow path, the refrigerant
Runner is located at the inside of flat board, and the two ends of the refrigerant flow path are respectively communicated with direct current refrigeration compressor and restricting element, described
The outer surface of cold drawing evaporator is directly contacted with air, and the cold drawing evaporator is placed or slant setting using upright.
Further, the water treatment system includes water-collecting tray, ultraviolet ray generating apparatus, water filter and water intake valve, described
Ultraviolet ray generating apparatus is located at the top side of water-collecting tray, and the bottom of the water-collecting tray is provided with water pipe, and the water pipe is provided with water
Filter and water intake valve, the water-collecting tray connect the globule dripped from evaporator, meanwhile, the steam water interface passes through steam-water separation
The isolated water of device is also flowed into water-collecting tray, and the water in the water-collecting tray is by ultraviolet ray generating apparatus sterilization processing, then flows
Filtration treatment is carried out to water filter, that is, obtains pure water, the water intake valve controls the outflow of pure water.
Further, the Proton Exchange Membrane Fuel Cells air water fetching device also includes auxiliary heat dissipating system, the auxiliary
Cooling system connects proton exchange film fuel battery system, the Proton Exchange Membrane Fuel Cells system by water vapor condenser
System, condenser and auxiliary heat dissipating system are sequentially communicated, and the auxiliary heat dissipating system is supplied to proton exchange film fuel battery system
Water first flow into water vapor condenser, then flow into proton exchange film fuel battery system and allow water to absorb pem fuel electricity
The reaction heat of cell system, absorbs the water of proton exchange film fuel battery system reaction heat from proton exchange film fuel battery system
Middle outflow, and flow into condenser zone and walk condensation heat, then flow back in auxiliary heat dissipating system and be cooled, the auxiliary heat dissipating system will be cold
But the water circulation after is supplied to proton exchange film fuel battery system.
Further, the auxiliary heat dissipating system includes radiator, cooling fan and water pump, and the cooling fan accelerates radiating
The convection current of device extraneous air, the water pump connects water vapor condenser, and the water pump draws water from the bottom of radiator, and is pumped into water
In vapour condenser, proton exchange film fuel battery system is entered back into；The auxiliary heat dissipating system also includes expansion tank, described
Expansion tank connect radiator, the expansion tank be radiator supplies water and provide water temperature change when needed for volumetric expansion sky
Between.
Compared with prior art, the utility model has the advantages that：The utility model synthesis is by the water in air
Water vapor condensation in the weary gas of air of steam and fuel cell exhaust is aqueous water, and then obtains fresh water, is lacking drinking water
In the case of, clean drinking water can be provided, the area that desert, island etc. lack fresh water is can be widely applied to, it is especially right
There is certain application value for desert, the military installations of Island；Meanwhile, the utility model can be serious at water source
The area of pollution is used as urgent fresh water sources；On ocean LNG (liquefied natural gas) cargo ship, skill described in the utility model
Art scheme can also be as a kind of water supply measure in emergency circumstances.
Brief description of the drawings
Fig. 1 is the composition schematic diagram of the embodiment of the utility model one.
Fig. 2 is the schematic appearance of steam-water separator in Fig. 1.
Embodiment
It is new to this practicality below in conjunction with accompanying drawing to make the purpose of this utility model, technical scheme and advantage clearer
Type embodiment is further described.
Fig. 1 is refer to, embodiment one kind of the present utility model provides Proton Exchange Membrane Fuel Cells air water fetching device,
Including proton exchange film fuel battery system 1, vapor compression type refrigerating system 2, water vapor condenser 3, steam-water separator 4 and water
Processing system 5.
Proton exchange film fuel battery system 1 includes hydrogen supply loop 11, air supply loop 12, PEM combustion
Expect battery pile 13 and DC-DC converter 14, hydrogen supply loop 11 and air supply loop 12 are all connected with proton exchange
Film fuel cell electric piling 13.
Hydrogen supply loop 11 supplies hydrogen, and hydrogen supply loop 11 includes high-pressure hydrogen storage 111, pressure-reducing valve 112, list
To valve 113, hand stop valve 114 and explosion-proof solenoid valve 115, high-pressure hydrogen storage 111, pressure-reducing valve 112, check valve 113, manually
Stop valve 114 and explosion-proof solenoid valve 115 are sequentially connected, and hydrogen comes out from high-pressure hydrogen storage 111, sequentially pass through pressure-reducing valve 112,
Check valve 113, hand stop valve 114 and explosion-proof solenoid valve 115 enter proton exchange film fuel cell electric piling 13.
Air is supplied in air supply loop 12, and air supply loop 12 includes air cleaner 121 and Air pressurizer
122, air cleaner 121 and Air pressurizer 122 are sequentially connected, and air enters sky after the processing of air cleaner 121
Gas pressure charging device 122, Air pressurizer 122 boosts air, and sends into proton exchange film fuel cell electric piling 13.
Oxygen in hydrogen and air reacts generation direct current, proton in proton exchange film fuel cell electric piling 13
The weary gas of air after the generation direct current of exchange film fuel battery system 13 is discharged in water vapor condenser 3, and the weary gas of air is condensed into
Steam water interface, steam water interface is separated into water and gas by steam-water separator 4, and water flows out from the bottom of steam-water separator 4,
Gas flows out from the top of steam-water separator 4, and is discharged into air, and remaining trace hydrogen is through the first magnetic valve 116 after reaction
It is discharged in air.
Fig. 2 is refer to, in one embodiment, steam-water separator 4 is whirlwind separator, and steam water interface divides from cyclone type
From the tangential inflow of the top circumference of device, steam water interface rotates at a high speed in the presence of cyclone separator air-flow, and density is big
Water is thrown toward barrel under the action of the centrifugal force, and the bottom for falling to flowing to cyclone separator along barrel under gravity is flowed out,
The small gas of density cyclone separator internal contraction and to center flow, secondary vortex flow is upwardly formed, from cyclone separator
Top outflow.
Direct current is converted into stable DC electricity, stable DC electric drive steam compression type system by DC-DC converter 14
Cooling system 2 works, and vapor compression type refrigerating system 2 includes direct current refrigeration compressor 21, condenser 22, restricting element 23 and evaporation
Device 24, direct current refrigeration compressor 21, condenser 22, restricting element 23 and evaporator 24 are sequentially connected composition loop, evaporator 24
Lower section be provided with water treatment system 5, in one embodiment, condenser 22 be refrigerant-water- to-water heat exchanger, restricting element 23 be capillary
Pipe, heating power expansion valve or electric expansion valve, evaporator 24 are cold drawing evaporator, and cold drawing evaporator includes flat board 241 and refrigerant
Runner 242, refrigerant flow path 242 is located at the inside of flat board 241, and the two ends of refrigerant flow path 242 are respectively communicated with DC system cold pressing
Contracting machine 21 and restricting element 23, the outer surface of cold drawing evaporator are directly contacted with air, cold drawing evaporator placed using upright or
Slant setting, preferential using upright placement, the side of evaporator 24 is provided with fan (not shown), fans drive air flow
The outside of evaporator 24, effectively strengthens convection current, to make the yield of condensed water enough, and the evaporating temperature of evaporator 24 is optimized to
It is sufficiently low, but higher than 0 degree Celsius, to avoid condensed water from being frozen on the surface of evaporator 24.In one embodiment, steam compression type
Refrigeration system 2 also includes device for drying and filtering 25, and device for drying and filtering 25 is located between condenser 22 and restricting element 23, dry filter
Impurity and moisture in the filtering high temperature highly pressurised liquid of device 25.
Stable DC electric drive direct current refrigeration compressor 21 is operated, and direct current refrigeration compressor 21 is by refrigerant gas boil down to
High temperature and high pressure gas, HTHP gas enters condenser 22, and HTHP gas is condensed into high temperature high pressure liquid in condenser 22,
High temperature high pressure liquid flows through the gas-liquid mixture that restricting element 23 is changed into low-temp low-pressure, and gas-liquid mixture flows into evaporator 24, gas
Liquid mixture absorbs the heat of the outside air of evaporator 24 in evaporator 24, and is evaporated to refrigerant gas, DC system again
The air entry of cold compressor 21 sucks refrigerant gas in direct current refrigeration compressor 21, and refrigerant gas is in direct current refrigerant compression
Compressed again in machine 21, the air setting in the outside of evaporator 24 is into the globule, and the globule drips to evaporator 24 under gravity
In the water treatment system 5 of lower section.
Water treatment system 5 includes water-collecting tray 51, ultraviolet ray generating apparatus 52, water filter 53 and water intake valve 54, ultraviolet
Generating means 52 is located at the top side of water-collecting tray 51, and the bottom of water-collecting tray 51 is provided with water pipe 55, and water pipe 55 is provided with water filtration
Device 53 and water intake valve 54, water-collecting tray 51 connect the globule dripped from evaporator 24, meanwhile, steam water interface passes through steam-water separator 3
Isolated water is also flowed into water-collecting tray 51, and the water in water-collecting tray 51 is by the sterilization processing of ultraviolet ray generating apparatus 52, then flows
Filtration treatment is carried out to water filter 53, that is, obtains pure water, water intake valve 54 controls the outflow of pure water.
Proton Exchange Membrane Fuel Cells air water fetching device also includes auxiliary heat dissipating system 6, and auxiliary heat dissipating system 6 passes through water
Vapour condenser 3 connects proton exchange film fuel battery system 1, proton exchange film fuel battery system 1, condenser 22 and auxiliary
Cooling system 6 is sequentially communicated, and auxiliary heat dissipating system 6 is supplied to the water of proton exchange film fuel battery system 1 to first flow into vapor
Condenser 3, then flow into proton exchange film fuel battery system 1 and allow water absorb proton exchange film fuel battery system 1 reaction
Heat, the water for absorbing the reaction heat of proton exchange film fuel battery system 1 flows out from proton exchange film fuel battery system 1, and
Flow into condenser 22 and take away condensation heat, then flow back in auxiliary heat dissipating system 6 and be cooled, auxiliary heat dissipating system 6 is by the water after cooling
Circulation-supplied is to proton exchange film fuel battery system 1.
Auxiliary heat dissipating system 6 includes radiator 61, cooling fan 62 and water pump 63, and cooling fan 62 accelerates outside radiator 61
The convection current of portion's air, the connection water vapor condenser 3 of water pump 63, the bottom of water pump 63 from radiator 61 is drawn water, and is pumped into vapor
In condenser 3, proton exchange film fuel battery system 1 is entered back into；In one embodiment, auxiliary heat dissipating system 6 also includes expansion
Water tank 64, expansion tank 64 connection radiator 61, expansion tank 64 be radiator 61 supply water and provide water temperature change when needed for
Volumetric expansion space.
The course of work：Oxygen in hydrogen and air reacts generation direct current in proton exchange film fuel cell electric piling 13
Electricity, the reacted weary gas of air is discharged in water vapor condenser 3, and the weary gas of air is condensed into steam water interface, and steam water interface leads to
Cross steam-water separator 4 and be separated into water and gas, water flows out from the bottom of steam-water separator 4, and flows into water-collecting tray 51, gas from
The top outflow of steam-water separator 4, and be discharged into air, remaining trace hydrogen is discharged to through the first magnetic valve 116 after reaction
In air；The direct current for reacting generation is converted to stable DC electricity, stable DC electric drive direct current through DC-DC converter 14
Refrigeration compressor 21 is operated, and direct current refrigeration compressor 21 enters refrigerant gas boil down to high temperature and high pressure gas, HTHP gas
Enter condenser 22, HTHP gas is condensed into high temperature high pressure liquid in condenser 22, and high temperature high pressure liquid flows through restricting element
23 are changed into the gas-liquid mixture of low-temp low-pressure, and gas-liquid mixture flows into evaporator 24, and gas-liquid mixture absorbs in evaporator 24
The heat of the outside air of evaporator 24, and refrigerant gas is evaporated to again, the air entry of direct current refrigeration compressor 21 will freeze
In agent gas suction direct current refrigeration compressor 21, refrigerant gas is compressed again in direct current refrigeration compressor 21, evaporator
The air setting in 24 outsides is into the globule, and the globule is dripped on the water-collecting tray 51 of the lower section of evaporator 24 under gravity；Water-collecting tray
51 pass through ultraviolet ray generating apparatus 52 by the globule dripped from evaporator 24 of reception and from the isolated water of steam-water separator 3
Sterilization processing, then flow to the progress filtration treatment of water filter 53, that is, pure water is obtained, water intake valve 54 controls the outflow of pure water.
Meanwhile, in course of reaction, the bottom of water pump 63 from radiator 61 is drawn water, and is pumped into water vapor condenser 3, then is entered
Enter proton exchange film fuel cell electric piling 13, the water into proton exchange film fuel cell electric piling 13 absorbs pem fuel
Reaction heat in battery pile 13, absorbs the reaction heat outflow in proton exchange film fuel cell electric piling 13, and enter condensation
Device 22 takes away condensation heat, then flows back in auxiliary heat dissipating system 6 and be cooled, and auxiliary heat dissipating system 6 supplies the water circulation after cooling
To proton exchange film fuel battery system 1.
The utility model synthesis is by the water vapor condensation in the vapor in air and the weary gas of the air of fuel cell exhaust
For aqueous water, and then fresh water is obtained, in the case where lacking drinking water, clean drinking water can be provided, be can be widely applied to
Desert, island etc. lack fresh water area, especially for for desert, the military installations of Island have certain application
Value；Meanwhile, the area that the utility model can be heavily polluted at water source is used as urgent fresh water sources；In ocean LNG (liquid
Change natural gas) on cargo ship, technical scheme described in the utility model can also be as a kind of water supply in emergency circumstances
Measure.
Herein, the involved noun of locality such as forward and backward, upper and lower is to be located at parts in accompanying drawing in figure and zero
The position of part each other is intended merely to the clear of expression technology scheme and conveniently come what is defined.It should be appreciated that the noun of locality
Use should not limit the claimed scope of the application.
In the case where not conflicting, the feature in embodiment and embodiment herein-above set forth can be combined with each other.
Preferred embodiment of the present utility model is the foregoing is only, it is all in this practicality not to limit the utility model
Within new spirit and principle, any modification, equivalent substitution and improvements made etc. should be included in guarantor of the present utility model
Within the scope of shield.
Claims (10)
1. a proton exchanging film fuel battery air water fetching device, it is characterised in that including Proton Exchange Membrane Fuel Cells system
System, vapor compression type refrigerating system, water vapor condenser and steam-water separator, the proton exchange film fuel battery system generation
Direct current, the direct current is converted into stable DC electricity, and the stable DC electric drive vapor compression type refrigerating system works,
The weary gas of air after the proton exchange film fuel battery system generation direct current is discharged in water vapor condenser, and the air is weary
Gas is condensed into steam water interface, and the steam water interface is separated into water and gas by steam-water separator, and the water divides from carbonated drink
Bottom from device is flowed out, and the gas flows out from the top of steam-water separator, and is discharged into air.
2. Proton Exchange Membrane Fuel Cells air water fetching device according to claim 1, it is characterised in that the proton is handed over
Changing film fuel battery system includes hydrogen supply loop, air supply loop, proton exchange film fuel cell electric piling and direct current-straight
Current converter, the hydrogen supply loop and air supply loop are all connected with proton exchange film fuel cell electric piling, the hydrogen
Supply loop supplies hydrogen, and the oxygen that the air supply loop is supplied in air, hydrogen and air is in pem fuel
Reacted generation direct current in battery pile, and direct current is converted into stable DC electricity, reaction by the DC-DC converter
Remaining trace hydrogen is discharged in air through the first magnetic valve afterwards.
3. Proton Exchange Membrane Fuel Cells air water fetching device according to claim 2, it is characterised in that the hydrogen is supplied
Answer loop include high-pressure hydrogen storage, pressure-reducing valve, check valve, hand stop valve and explosion-proof solenoid valve, the high-pressure hydrogen storage,
Pressure-reducing valve, check valve, hand stop valve and explosion-proof solenoid valve are sequentially connected, and hydrogen comes out from high-pressure hydrogen storage, are sequentially passed through
Pressure-reducing valve, check valve, hand stop valve and explosion-proof solenoid valve enter proton exchange film fuel cell electric piling；The air supply is returned
Road includes air cleaner and Air pressurizer, and the air cleaner and Air pressurizer are sequentially connected, and air passes through
Enter Air pressurizer after air cleaner processing, the Air pressurizer boosts air, and sends into PEM
Fuel cell pile.
4. Proton Exchange Membrane Fuel Cells air water fetching device according to claim 2, it is characterised in that the carbonated drink point
It is whirlwind separator from device, the steam water interface is from the tangential inflow of the top circumference of whirlwind separator, the carbonated drink
Mixture rotates at a high speed in the presence of cyclone separator air-flow, and the big water of density is thrown toward barrel under the action of the centrifugal force, and
The bottom for falling to flowing to cyclone separator along barrel under gravity is flowed out, and the small gas of density is in the inside of cyclone separator
Shrink and to center flow, be upwardly formed secondary vortex flow, flowed out from the top of cyclone separator.
5. Proton Exchange Membrane Fuel Cells air water fetching device according to claim 1, it is characterised in that the vapour pressure
Compression type refrigerating system includes direct current refrigeration compressor, evaporator, restricting element and condenser, the direct current refrigeration compressor, steaming
Hair device, restricting element and condenser are sequentially connected composition loop, and the lower section of the evaporator is provided with water treatment system, the stabilization
DC powered direct current refrigeration compressor is operated, and direct current refrigeration compressor is by refrigerant gas boil down to high temperature and high pressure gas, institute
State HTHP gas and enter condenser, the HTHP gas is condensed into high temperature high pressure liquid within the condenser, and the high temperature is high
Press liquid flows through the gas-liquid mixture that restricting element is changed into low-temp low-pressure, and the gas-liquid mixture flows into evaporator, the gas-liquid
Mixture absorbs the heat of evaporator outside air in evaporator, and is evaporated to refrigerant gas, the direct current refrigeration again
The air entry of compressor by refrigerant gas suck direct current refrigeration compressor in, refrigerant gas in direct current refrigeration compressor again
Secondary to be compressed, the air setting on the outside of the evaporator is into the globule, and the globule is dripped to below evaporator under gravity
Water treatment system on.
6. Proton Exchange Membrane Fuel Cells air water fetching device according to claim 5, it is characterised in that the one of evaporator
Side is provided with fan, and the outside of the fans drive air flow evaporator, the vapor compression type refrigerating system also includes drying
Filter, the device for drying and filtering is located between condenser and restricting element, the device for drying and filtering filtering high temperature highly pressurised liquid
In impurity and moisture.
7. Proton Exchange Membrane Fuel Cells air water fetching device according to claim 5, it is characterised in that the condenser
For refrigerant-water- to-water heat exchanger, the restricting element is capillary, heating power expansion valve or electric expansion valve, and the evaporator is cold drawing
Evaporator, the cold drawing evaporator includes flat board and refrigerant flow path, and the refrigerant flow path is located at the inside of flat board, the system
The two ends of refrigerant flow conduit are respectively communicated with direct current refrigeration compressor and restricting element, and the outer surface of the cold drawing evaporator and air are straight
Contact, the cold drawing evaporator is placed or slant setting using upright.
8. fuel battery air water fetching device according to claim 5, it is characterised in that the water treatment system includes collection
Water pond, ultraviolet ray generating apparatus, water filter and water intake valve, the ultraviolet ray generating apparatus are located at the top side of water-collecting tray,
The bottom of the water-collecting tray is provided with water pipe, and the water pipe is provided with water filter and water intake valve, and the water-collecting tray is connect from evaporator
The globule dripped, meanwhile, the steam water interface is also flowed into water-collecting tray by the isolated water of steam-water separator, the collection
Water in water pond is by ultraviolet ray generating apparatus sterilization processing, then flow to water filter progress filtration treatment, that is, obtains pure water,
The water intake valve controls the outflow of pure water.
9. Proton Exchange Membrane Fuel Cells air water fetching device according to claim 5, it is characterised in that the proton is handed over
Changing membrane cell air water fetching device also includes auxiliary heat dissipating system, and the auxiliary heat dissipating system is connected by water vapor condenser
Logical proton exchange film fuel battery system, the proton exchange film fuel battery system, condenser and auxiliary heat dissipating system are successively
Connection, the auxiliary heat dissipating system is supplied to the water of proton exchange film fuel battery system to first flow into water vapor condenser, then flows
Enter proton exchange film fuel battery system and allow water to absorb the reaction heat of proton exchange film fuel battery system, absorb proton friendship
The water for changing film fuel battery system reaction heat flows out from proton exchange film fuel battery system, and flow into condenser zone walk condensation
Heat, then flow back in auxiliary heat dissipating system be cooled, the water circulation after cooling is supplied to proton exchange by the auxiliary heat dissipating system
Film fuel battery system.
10. Proton Exchange Membrane Fuel Cells air water fetching device according to claim 9, it is characterised in that the auxiliary
Cooling system includes radiator, cooling fan and water pump, and the cooling fan accelerates the convection current of radiator extraneous air, the water
Pump connects water vapor condenser, and the water pump draws water from the bottom of radiator, and is pumped into water vapor condenser, enters back into proton
Exchange film fuel battery system；The auxiliary heat dissipating system also includes expansion tank, and the expansion tank connects radiator, described
Expansion tank for radiator supply water and provide water temperature change when needed for volumetric expansion space.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720100758.1U CN206467720U (en) | 2017-01-24 | 2017-01-24 | One proton exchanging film fuel battery air water fetching device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720100758.1U CN206467720U (en) | 2017-01-24 | 2017-01-24 | One proton exchanging film fuel battery air water fetching device |
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| Publication Number | Publication Date |
|---|---|
| CN206467720U true CN206467720U (en) | 2017-09-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201720100758.1U Active CN206467720U (en) | 2017-01-24 | 2017-01-24 | One proton exchanging film fuel battery air water fetching device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106677260A (en) * | 2017-01-24 | 2017-05-17 | 武汉地质资源环境工业技术研究院有限公司 | Proton exchange membrane fuel cell air water intake device |
-
2017
- 2017-01-24 CN CN201720100758.1U patent/CN206467720U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106677260A (en) * | 2017-01-24 | 2017-05-17 | 武汉地质资源环境工业技术研究院有限公司 | Proton exchange membrane fuel cell air water intake device |
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