CN112582647A - Energy-saving gas supply system of fuel cell test bench - Google Patents
Energy-saving gas supply system of fuel cell test bench Download PDFInfo
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- CN112582647A CN112582647A CN202011566812.4A CN202011566812A CN112582647A CN 112582647 A CN112582647 A CN 112582647A CN 202011566812 A CN202011566812 A CN 202011566812A CN 112582647 A CN112582647 A CN 112582647A
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- 238000012360 testing method Methods 0.000 title claims abstract description 86
- 239000000446 fuel Substances 0.000 title claims abstract description 25
- 230000001105 regulatory effect Effects 0.000 claims abstract description 18
- 230000001276 controlling effect Effects 0.000 claims 1
- 238000000034 method Methods 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 39
- 230000006835 compression Effects 0.000 description 8
- 238000007906 compression Methods 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 230000003213 activating effect Effects 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000001514 detection method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009530 blood pressure measurement Methods 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000036284 oxygen consumption Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04746—Pressure; Flow
- H01M8/04753—Pressure; Flow of fuel cell reactants
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04746—Pressure; Flow
- H01M8/04776—Pressure; Flow at auxiliary devices, e.g. reformer, compressor, burner
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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
- 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
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Abstract
The invention belongs to the field of fuel cell testing, and discloses an energy-saving gas supply system of a fuel cell testing platform, which comprises a main path, wherein the main path comprises an air filter, an air compressor, a cooler, a main path valve, a flowmeter and a humidifier which are sequentially connected; the tail end of the humidifier is connected with a cathode inlet of the galvanic pile, and an outlet of the galvanic pile is connected with a back pressure valve; a branch is further arranged in the test board, the inlet connecting end of the branch is arranged between the cooler and the main path valve, and the outlet connecting end of the branch is arranged between the electric pile and the back pressure valve; and a branch regulating valve is arranged on the branch. The system has simple structure, can obviously reduce energy consumption, saves cost and improves production efficiency.
Description
Technical Field
The invention belongs to the field of fuel cell testing, relates to an energy-saving gas supply system of a fuel cell test bench, and relates to an energy-saving gas supply system built in or arranged adjacent to the test bench. In particular to a cell cathode air supply system of a proton exchange membrane fuel cell testing and activating platform.
Background
Fuel cell research and production requires testing. The equipment used for testing is generally referred to as a test bench. The test station consists of several subsystems including anode fuel hydrogen supply to the stack, cooling of the stack, cathode oxidant air supply to the stack, electronic loads for consumption of the generated electricity, and control systems such as PLC systems. Among them, the cathode air supply is the main energy consuming subsystem, and the emphasis is to reduce its energy consumption.
Fuel cell testing, particularly pressurized hydrogen pem fuel cell testing, requires the use of an air compressor to provide pressurized cathode air to the stack as the reactant oxidant, and the operating pressure generally increases with increasing power. This is because, as the power output increases, the current density increases, the rate of oxygen consumption increases, and the oxygen concentration needs to be increased by increasing the pressure, thereby reducing the adverse effect of so-called concentration diffusion on oxygen transfer.
The air supply air compressor of the fuel cell engine system in application changes the rotating speed along with the output height of the electric pile, the high output corresponds to high rotating speed, high pressure and high air quantity, and the low output corresponds to low rotating speed, low pressure and low air quantity. On the other hand, the resistance of the gas in the flow field increases rapidly with the increase of the gas flow rate, which is another main reason why high pressure is required for high flow rate.
For air supply, especially for high power tests, the air is typically delivered to the test station by a remote air supply system external to the test station, including compression and storage tanks, through pipes and valves, etc., against resistance. The air compressor provides a high-pressure air source, the air pressure of the air compressor is mostly 0.7MPag, the air pressure is reduced in the test bench, the air pressure reaches the fuel cell and is used in 0.02-0.20 MPag, a small amount of air pressure can be used in 0.30MPag, a large proportion of compression work is wasted, and the air supply system occupies a large area and has high equipment cost. Particularly, in a high-power test, a remote conventional compression and storage supply mode is adopted, and the space, the manufacturing cost and the energy consumption far exceed a low-pressure air supply mode built in or arranged nearby a test board body.
The operation of the electric pile has the characteristics of low power, low air pressure and low flow rate, and high power, high air pressure and high flow rate, so that if the integral technology is not researched, the air compressor directly used is easy to generate the surge of a certain flow rate specific to the air compressor in use.
Disclosure of Invention
The invention aims to overcome the defects in the background technology, and provides a cathode air supply subsystem of a fuel cell test board, which is called an energy-saving air supply system of the fuel cell test board for short.
The technical scheme adopted by the invention for solving the technical problems is as follows: an energy-saving gas supply system of a fuel cell test bench comprises a main path, wherein the main path comprises an air filter, an air compressor, a cooler, a main path valve, a flow meter and a humidifier which are sequentially connected; the tail end of the humidifier is connected with a cathode inlet of the galvanic pile, and an outlet of the galvanic pile is connected with a back pressure valve; the system is also provided with a branch, the inlet connecting end of the branch is arranged between the cooler and the main path valve, and the outlet connecting end of the branch is arranged between the electric pile and the back pressure valve; and a branch regulating valve is arranged on the branch.
Further, the air compressor is a low-pressure air compressor; the air compressor is arranged inside the test bench or arranged near the outer part of the test bench.
Further, when the air compressor is arranged inside the test board, the distance between the air compressor and the test board is 1-5 m;
further, when the air compressor is arranged inside the test board, the main path and the branch path are arranged inside the test board; when the air compressor is arranged at the outer part of the test bench, a main path in which the air filter, the air compressor and the cooler are sequentially connected is arranged outside the test bench;
when the air compressor is arranged at the outer part of the test bench, the backpressure valve is connected with an exhaust pipe through a pipeline, and the exhaust pipe and the pipeline thereof are arranged at the outer part of the test bench; the air filter is also connected with a new air pipe, and the cooler is connected with the main path valve through an air supply pipe.
Further, the electric pile is arranged outside the test bench;
further, a gas detector is arranged between the humidifier and the electric pile; the air temperature, pressure and humidity detection device is used for detecting air temperature, pressure and humidity.
Furthermore, the opening degree of the branch regulating valve is adjustable.
And a line section of the outlet of the galvanic pile connected with the backpressure valve is a tail gas discharge line section.
The energy-saving gas supply system of the test bench comprises a PLC system, and the PLC system is respectively connected with an air compressor, a gas source valve, a gas supply valve, a gas detector, a main path valve, a flow meter, a humidifier, a branch regulating valve and a back pressure valve.
The maximum pressure of the rated flow of the low-pressure air compressor is 0.1-0.3 MPa higher than 0.02-0.20 MPag of the operating pressure of the electric pile, 0.4-0.50 MPag is taken as a comparison, the maximum pressure of the rated flow of the air compressor used in the conventional technology is generally 0.60-0.70 MPag, so that the system saves energy compared with the conventional technology, and simultaneously, the pressure change amplitude is reduced, and the gas pressure point generated by the surge flow of the system is also relatively reduced;
according to the surge characteristic of the air compressor and the rotating speed regulation hysteresis characteristic of the air compressor, when low-flow surge occurs, the system keeps the rotating speed of the air compressor, opens the branch regulating valve, and part of gas flow is shunted from the branch to reach the tail gas discharge line section of the electric pile;
the gas detector detects temperature, pressure and humidity and air parameters at the inlet of the galvanic pile, is connected with the PLC system, transmits detected air temperature, humidity, pressure and flow signals to the PLC system, and the PLC system adjusts the temperature, humidity, pressure and flow by taking the signals as regulation and control basis;
for a specific galvanic pile, a flow meter, a branch regulating valve and a back pressure valve are used for regulation and control;
when the specific flow exceeds the flow of a surge area by more than 150%, when the flow of the galvanic pile needs to be adjusted, the rotating speed of the air compressor operates according to a characteristic curve according to the working curve of the air compressor;
when the flow is below 150% in the surge area, the rotating speed of the air compressor is unchanged, the opening degree of the branch adjusting valve is adjusted firstly to enable the flow meter data to be the system operation set data, then the back pressure valve is adjusted to adjust the operation pressure to be the set pressure, then the branch adjusting valve is adjusted, and the two are not adjusted at the same time.
Compared with the prior art, the invention has the beneficial effects that:
1) the system test condition is closer to the real operation condition, the performance of the galvanic pile in actual operation can be reflected better, and the optimization of the using condition of the galvanic pile through the test is facilitated;
2) the energy-saving effect can be generated in the aspect of electric power, and particularly for high-power testing or activating application;
3) the huge gas supply system outside the test board is reduced, the complexity of the equipment system is reduced, and flexible layout is facilitated;
4) the development of an air supply system with high response speed is facilitated, and dynamic testing is realized;
the invention provides an energy-saving air supply system of a fuel cell test bench, which is used for supplying air to the fuel cell test bench and has good flow range adaptability. When the flow of the galvanic pile needs to be adjusted, the rotating speed of the air compressor runs according to the optimal characteristic curve according to the working curve of the air compressor, when the flow is slightly higher than the flow in a surge area and lower, the rotating speed of the air compressor is unchanged, the opening degree of the branch adjusting valve is adjusted firstly to enable the flow meter data to be set for system operation, then the back pressure valve is adjusted to adjust the operating pressure to be set pressure, and then the adjusting valve and the back pressure valve are adjusted in sequence. The system provided by the invention has the advantages that the test condition is closer to the real operation condition, the performance of the galvanic pile in actual operation can be reflected, and the optimization of the using condition of the galvanic pile is facilitated; the energy-saving effect can be generated in the aspect of electric power, and particularly for high-power testing or activating application; the huge gas supply system outside the test board can be reduced, the complexity of the equipment system is reduced, and the equipment layout is convenient; the air supply system with high response speed is developed and dynamic testing is realized.
Drawings
The invention is further illustrated with reference to the following figures and examples:
fig. 1 is a schematic view of a conventional air supply system.
Fig. 2 is a schematic structural view of an energy-saving gas supply system built in a test bench according to embodiment 1 of the present invention.
Fig. 3 is a schematic structural view of a split energy-saving air supply system of a test bench according to embodiment 2 of the present invention.
In the figure, 1, an existing air supply system, 2, a cathode air control system, 3, a galvanic pile, 4, an air supply system, 11, an existing air filter, 12, a high-pressure air compressor, 13, an existing cooler, 14, an air storage tank, 21, an air source valve, 22, a pressure reducing valve, 23, an air supply valve, 24, a flow controller, 25, an existing humidifier, 26, an existing gas detector, 27, an existing back pressure valve and 41, an air filter are arranged; 42. the air compressor, 43, the cooler, 44, the main path valve, 45, the flow meter, 46, the humidifier, 47, the gas detector, 48, the branch adjusting valve, 49, the back pressure valve, 431, the air supply pipe, 432, the indoor and outdoor space, 433, the new air pipe and 434, the exhaust pipe.
Detailed Description
The invention is further described below with reference to the drawings attached to the specification, but the invention is not limited to the following examples.
The air compressor, the air source valve, the air supply valve, the humidifier gas detector, the main path valve, the flow meter, the branch regulating valve and the back pressure valve which are connected with the PLC system are not limited to be in a certain type, and the air source valve, the air supply valve, the main path valve, the branch regulating valve and the back pressure valve can be valves which can receive control signals of the PLC system to realize opening and closing functions; the flowmeter is not limited in model, and can realize flow measurement and feed back signals to a PLC system; the gas detector is not limited in type, and can realize temperature measurement, humidity measurement, pressure measurement and flow measurement and feed back signals to the PLC system. For simplicity and to highlight the technical expression, the hydrogen system, the cooling system and the control system are not shown, but do not affect the essence of the technical content.
Example 1
An energy-saving air supply system of a test bench, as shown in fig. 2, comprises a main path, wherein the main path comprises an air filter 41, an air compressor 42, a cooler 43, a main path valve 44, a flow meter 45 and a humidifier 46 which are sequentially connected; the tail end of the humidifier 46 is connected with the cathode inlet of the galvanic pile 3, and the outlet of the galvanic pile 3 is connected with a back pressure valve 49; the system is also provided with a branch, the inlet connection end of which is arranged between the cooler 43 and the main valve 44, and the outlet connection end of which is arranged between the electric pile 3 and the back pressure valve 49; a branch regulating valve 48 is arranged on the branch.
The air compressor 42 is a low-pressure air compressor;
the electric pile 3 is arranged outside the test bench;
a gas detector 47 is also arranged between the humidifier 46 and the electric pile 3; the air temperature, pressure and humidity detection device is used for detecting air temperature, pressure and humidity.
The opening degree of the branch regulating valve 48 is adjustable.
The energy-saving gas supply system of the test bench comprises a PLC system, and the PLC system is respectively connected with an air compressor 42, a gas source valve, a gas supply valve, a gas detector 47, a main path valve 44, a flow meter 45, a humidifier 46, a branch regulating valve 48 and a backpressure valve 49.
The highest pressure of rated flow of the low-pressure air compressor 42 used in the test bench is 0.10-0.30 MPa higher than the highest pressure of the stack operation, preferably 0.40-0.50 MPag, and the heat generated by compression is less than that generated by the high-pressure air compressor 12 of the comparative example, so that the cooling load required by the cooler 43 is less than that of the existing cooler 13.
In some operating conditions, such as the simultaneous rapid cut-off of the main and branch circuits, the operation of the air compressor 42 is not stopped due to inertia, which can generate vibration and noise with a high price ratio. For this reason, the branch circuit is connected between the cooler 43 and the main circuit valve 44, instead of between the main circuit valve 44 and the flow meter 45.
The maximum pressure of the rated flow of the low pressure air compressor 42 is lower than that of the air compressor used in the conventional art, so that the pressure value at the surge flow generation point is relatively lowered, and the directly controllable stable flow interval is increased.
According to the specific surge characteristic flow value of the low-pressure air compressor 42, when surging occurs, 150% of the flow of a surge point is taken, the rotating speed of the low-pressure air compressor 42 is kept, the branch adjusting valve 48 is opened, part of gas flow is divided from the branch to reach the backpressure valve 48 on the tail gas discharge line section of the electric pile, the flow of the electric pile 3 is detected by the main flow meter 45, and the flow of the electric pile 3 is reduced to a required value according to the opening degree of the branch adjusting valve 48.
For a specific electric pile 3, the optimal operation characteristic curves of different air compressors 42 adopted by the electric pile 3 are different, the test bench system selectively simulates the flow pressure relation of the operation of the electric pile 3 according to the characteristic curves of the different air compressors 42, and the flow meter 45, the branch regulating valve 48 and the back pressure valve 49 are specifically used for regulation and control.
When the specific flow exceeds the flow of a surge area by more than 150%, when the flow of the galvanic pile 3 needs to be adjusted, the rotating speed of the air compressor 42 operates according to the optimal characteristic curve according to the working curve of the air compressor 42;
when the flow is below 150% in the surge area, the rotating speed of the low-pressure air compressor 42 is unchanged, the opening degree of the branch adjusting valve 48 is firstly adjusted to enable the data of the flow meter 45 to be the system operation set data, then the back pressure valve 49 is adjusted to adjust the operation pressure to be the set pressure, and then the branch adjusting valve 48 is adjusted, wherein the two are not adjusted simultaneously.
Example 2
An energy-saving air supply system of a test bench is shown in figure 3. The system comprises a main path, wherein the main path comprises an air filter 41, an air compressor 42, a cooler 43, a main path valve 44, a flow meter 45 and a humidifier 46 which are sequentially connected; the tail end of the humidifier 46 is connected with the cathode inlet of the galvanic pile 3, and the outlet of the galvanic pile 3 is connected with a back pressure valve 49; the system is also provided with a branch, the inlet connection end of which is arranged between the cooler 43 and the main valve 44, and the outlet connection end of which is arranged between the electric pile 3 and the back pressure valve 49; a branch regulating valve 48 is arranged on the branch.
The air compressor 42 is a low-pressure air compressor;
the electric pile 3 is arranged outside the test bench;
a gas detector 47 is also arranged between the humidifier 46 and the electric pile 3; the air temperature, pressure and humidity detection device is used for detecting air temperature, pressure and humidity.
The opening degree of the branch regulating valve 48 is adjustable.
The energy-saving gas supply system of the test bench comprises a PLC system, and the PLC system is respectively connected with an air compressor 42, a gas source valve, a gas supply valve, a gas detector 47, a main path valve 44, a flow meter 45, a humidifier 46, a branch regulating valve 48 and a backpressure valve 49.
The air compressor machine is adjacent external mode at the testboard frame, namely, is in the external connection mode of components of a whole that can function independently with the testboard main part.
The air compressor 42 is arranged outside the frame of the test bench 4, the distance between the air compressor 42 and the test bench is 1-5m, and the air compressor 42 and the main body of the test bench are connected by a pipeline; the air compressor 42 is connected to the cooler by a pressure hose air supply pipe 431, so that the vibration caused by the air flow and the conduction of the vibration are reduced. The air compressor 42 is arranged near the test bench 4 and close to an indoor and outdoor space 432 of a building, fresh air pipes 433 penetrate through the indoor and outdoor space 432 to suck outdoor fresh air, the air compressor 42 compresses the air after passing through the air filter 41, the air is cooled through the cooler 43, and the pressure-resistant hose air supply pipe 431 is connected and conveyed into a test frame of the test bench 4; the air used by the stack passes through the control valve 49 and the exhaust pipe 434 of the test stand 4, passes through the indoor and outdoor space 432, and is discharged to the outside of the building.
Comparative example 1:
the test bench, especially for high-power test, generally uses the remote gas supply system outside the test bench, including compression and storage tanks, through the pipeline and valve, etc., to deliver to the test bench, to provide high-pressure gas source, the gas pressure mostly adopts 0.7MPag, then reduces the pressure in the test bench, reaches the fuel cell to use in 0.02-0.20 MPag, a small amount may use in 0.30MPag, a large proportion of compression work is wasted.
As shown in fig. 1, the air supply system 1 of the cathode air supply system of the conventional test bed mainly comprises a conventional air filter 11, a high-pressure air compressor 12, a conventional cooler 13 and an air storage tank 14, and is sent to the cathode air control system 2 of the test bed from a remote position away from the test bed through a valve control and pipeline system, and then is sent to the cell stack 3 through an air supply valve 21, a pressure reducing valve 22, an air supply valve 23, a flow controller 24, a conventional humidifier 25 and a conventional gas detector 26, and then is returned to the test bed from the cell stack 3, and the pressure of the cell stack 3 is controlled through a conventional back pressure valve 27 and is discharged, thereby completing the management of cathode air. The high pressure air compressor 12 is typically 0.7MPag, which is also due to pressure loss through long lines connected to the test stand, pressure reduction loss through the pressure reduction valve 22, and the storage tank 15.
Therefore, the compression work is wasted due to the high pressure and then the pressure reduction, the air supply system occupies a large area and has more equipment cost, and the layout is also limited by the arrangement of pipelines in the building. In the high-power test, the conventional compression and storage supply mode connected with a remote place is adopted, the space, the manufacturing cost and the energy consumption exceed the system provided by the invention, namely, the low-pressure air supply mode is adopted in the test table body.
Although the invention has been described in detail above with reference to a general description and specific examples, it will be apparent to one skilled in the art that modifications or improvements may be made thereto based on the invention. Accordingly, such modifications and improvements are intended to be within the scope of the invention as claimed.
Claims (6)
1. An energy-saving gas supply system of a fuel cell test bench is characterized by comprising a main path, wherein the main path comprises an air filter (41), an air compressor (42), a cooler (43), a main path valve (44), a flowmeter (45) and a humidifier (46) which are sequentially connected; the tail end of the humidifier (46) is connected with a cathode inlet of the galvanic pile (3), and an outlet of the galvanic pile (3) is connected with a back pressure valve (49); a branch is further arranged in the test bench, the inlet connecting end of the branch is arranged between the cooler (43) and the main path valve (44), and the outlet connecting end of the branch is arranged between the electric pile (3) and the backpressure valve (49); and a branch regulating valve (48) is arranged on the branch.
2. The energy-saving gas supply system of the fuel cell test bench according to claim 1, wherein said air compressor (42) is a low pressure air compressor.
3. An energy saving gas supply system for fuel cell test benches according to claim 2 characterized in that said galvanic pile (3) is arranged outside the test bench.
4. An energy-saving gas supply system for a fuel cell test bench according to claim 3, wherein a gas detector (47) is further provided between the humidifier (46) and the stack (3).
5. An energy-saving gas supply system for a fuel cell test bench according to claim 4, wherein said air compressor is disposed inside the test bench or outside the test bench at a distance of 1-5 m.
6. The working method of the energy-saving gas supply system of the fuel cell test bench according to any one of claims 1 to 5, wherein the maximum pressure of the rated flow of the low-pressure air compressor (42) is 0.1 to 0.3MPa higher than the operating pressure of the pile (3) by 0.02 to 0.20MPag, and 0.4 to 0.50MPag is taken; when low-flow surge is close to occur, the system keeps the rotating speed of an air compressor (42), opens a branch regulating valve (48), and divides part of gas flow to reach a tail gas discharge and pay-off line section of a galvanic pile (3), wherein the flow of the galvanic pile (3) is detected by a main flow meter (45) and is used as a basis for controlling the opening degree of the branch regulating valve (48), so that the flow of the galvanic pile (3) is reduced to a required value;
when the specific flow exceeds the flow of a surge area by more than 150%, when the flow of the galvanic pile (3) needs to be adjusted, the rotating speed of the air compressor (42) operates according to a characteristic curve according to the working curve of the air compressor (42);
when the flow is below 150% in the surge area, the rotating speed of the air compressor (42) is unchanged, the opening degree of the branch adjusting valve (48) is firstly adjusted to enable the data of the flow meter (45) to be set as system operation data, then the back pressure valve (49) is adjusted to adjust the operation pressure to be set pressure, then the branch adjusting valve (48) is adjusted, and the two are not adjusted simultaneously.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113916464A (en) * | 2021-09-30 | 2022-01-11 | 广东利元亨智能装备股份有限公司 | Method for detecting gas leakage of electric pile, method for detecting external leakage and method for detecting gas tightness of electric pile |
| CN114784330A (en) * | 2022-05-19 | 2022-07-22 | 上海捷氢科技股份有限公司 | Activation device for fuel cell system and delivery test method for fuel cell system |
| CN115064727A (en) * | 2022-07-19 | 2022-09-16 | 山东国创燃料电池技术创新中心有限公司 | Air supply system of fuel cell engine, control method and airplane |
| CN115472869A (en) * | 2022-09-21 | 2022-12-13 | 大连锐格新能源科技有限公司 | Ring island type layout of test board and external pipeline of fuel cell test workshop |
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2020
- 2020-12-25 CN CN202011566812.4A patent/CN112582647A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113916464A (en) * | 2021-09-30 | 2022-01-11 | 广东利元亨智能装备股份有限公司 | Method for detecting gas leakage of electric pile, method for detecting external leakage and method for detecting gas tightness of electric pile |
| CN113916464B (en) * | 2021-09-30 | 2023-11-17 | 广东利元亨智能装备股份有限公司 | Pile gas leakage detection method and airtight detection method thereof |
| CN114784330A (en) * | 2022-05-19 | 2022-07-22 | 上海捷氢科技股份有限公司 | Activation device for fuel cell system and delivery test method for fuel cell system |
| CN115064727A (en) * | 2022-07-19 | 2022-09-16 | 山东国创燃料电池技术创新中心有限公司 | Air supply system of fuel cell engine, control method and airplane |
| CN115064727B (en) * | 2022-07-19 | 2023-12-22 | 山东国创燃料电池技术创新中心有限公司 | Air supply system of fuel cell engine, control method and aircraft |
| CN115472869A (en) * | 2022-09-21 | 2022-12-13 | 大连锐格新能源科技有限公司 | Ring island type layout of test board and external pipeline of fuel cell test workshop |
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