CN212209663U - Fuel cell air management device and system - Google Patents
Fuel cell air management device and system Download PDFInfo
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- CN212209663U CN212209663U CN201921792420.2U CN201921792420U CN212209663U CN 212209663 U CN212209663 U CN 212209663U CN 201921792420 U CN201921792420 U CN 201921792420U CN 212209663 U CN212209663 U CN 212209663U
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Abstract
The utility model discloses a fuel cell air management device and system, the device include the device body and set up this internal heat-retaining granule of device, the device body still includes device body input port and device body delivery outlet, absorbs moisture and produces heat through fuel cell air management device, preheats the fuel cell galvanic pile to the start-up of fuel cell galvanic pile under the lower temperature, through the flow direction of the temperature of detecting the fuel cell galvanic pile and control air current, accomplish the state control of fuel cell galvanic pile cold start, normal start and fuel cell air management device heat transfer.
Description
Technical Field
The utility model belongs to the technical field of the new forms of energy, concretely relates to fuel cell air management device and system.
Background
Currently, large-scale commercialization of fuel cell vehicles, which is one of solutions for motorization of vehicles, has problems of high cost, short life, weak hydrogen infrastructure, and the like. Among them, the cold start problem of fuel cell is one of the key technical bottlenecks that hinder the commercialization of fuel cell, and is the biggest challenge in the winter operation of fuel cell vehicles.
When the fuel cell is cold started in a low-temperature environment lower than 0 ℃ without taking any protective measures, water generated by the reaction can be frozen in the catalytic layer firstly, so that the reactive active sites of the catalytic layer are covered, the oxygen transmission is blocked, and the voltage drops suddenly; when the catalytic layer is completely covered with ice and the temperature of the stack has not risen above 0 ℃, ice may form in the diffusion layer and the flow channels, resulting in a failed cold start. On the other hand, the icing process of the catalyst layer can cause gaps between the catalyst layer and the proton exchange membrane, and meanwhile, the icing/melting cycle can cause the collapse and densification of the microporous structure of the catalyst layer and the coarsening of platinum particles in the catalyst layer, so that the electrochemical active surface area is reduced and difficult to recover, thereby causing permanent damage to the power generation performance of the fuel cell, and the damage to the cell is larger when the cold start temperature is lower as the cycle times are larger.
The current solutions for low temperature fuel cell start-up fall into two categories: one is that gas purging is used to reduce the water content of the membrane electrode of the fuel cell when the electric pile is shut down, so as to reduce the formation of solid ice, but when the temperature of the electric pile is not raised to be above 0 ℃, the electric pile is only started to generate water and the water freezes, and firstly, ice is generated on the contact part of the platinum particle surface and the Nafion resin, once the temperature is raised to room temperature, the ice on the platinum and Nafion interface is melted, so that the interface is separated, and irreversible electrochemical active area loss is caused; the other type is that the electric pile and the internal polar plate and the membrane electrode thereof are preheated by the modes of electric heating of the vehicle-mounted power battery or catalytic combustion heat release of the vehicle-mounted hydrogen, and the like, wherein the electric pile can consume a part of electric quantity of the vehicle-mounted power battery, the power battery is difficult to cold start and greatly reduced in discharge capacity in a low-temperature environment, and the power battery can consume a part of the vehicle-mounted hydrogen, so that the electric pile and the internal polar plate and the membrane electrode thereof can shorten the endurance mileage of the fuel cell automobile.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a fuel cell air management device and system has solved the inconvenient problem of current fuel cell cold start.
The utility model provides a fuel cell air management device, include: the device body and setting are in this internal heat-retaining granule of device, the device body still includes device body input port and device body delivery outlet.
Optionally, the heat storage particles comprise silica gel, activated carbon, activated alumina, metal organic framework, or zeolite.
Optionally, the device body comprises a storage cavity for loading heat storage particles and a shell for heat preservation.
Optionally, filter screens are respectively arranged at positions where the input port of the device body is matched with the output port of the device body.
A fuel cell air management system comprising: an air supply unit including a humidifier for humidifying air and a fuel cell air management device for preheating air, the humidified air being capable of being preheated after passing through the fuel cell air management device; a fuel cell stack in communication with the air supply unit; and the fuel cell controller is used for controlling the air input and output of the air supply unit and the fuel cell stack, and is respectively in signal connection with the air supply unit and the fuel cell stack.
Optionally, the air supply unit further comprises an air compressor for compressing and heating air, the air compressor being in communication with the humidifier.
Optionally, an output port of the compressor is respectively communicated with an input port of a humidifier and an input port of the fuel cell stack through a first valve, an output port of the compressor is further respectively communicated with an input port of an air management device of the fuel cell and an input port of the humidifier through a second valve, an output port of the humidifier is respectively communicated with an input port of the fuel cell stack and an input port of the air management device of the fuel cell through a third valve, an output port of the fuel cell stack is respectively communicated with a discharge port of the fuel cell stack and an input port of the humidifier through a fourth valve, and an output port of the air management device of the fuel cell is respectively communicated with an input port of the air compressor and an input port of the humidifier through a fifth valve.
Optionally, the first valve, the second valve, the third valve, the fourth valve and the fifth valve all include three-way solenoid valves.
Optionally, the fuel cell air management system further comprises an air filter for filtering and a sixth valve for controlling air flow, the air filter being in communication with the sixth valve.
Optionally, the fuel cell air management system further includes a first temperature sensor, a second temperature sensor and a third temperature sensor, the first temperature sensor is configured to detect a temperature of an output port of the fuel cell air management device, the second temperature sensor is configured to detect an internal temperature of the fuel cell air management device, and the third temperature sensor is configured to detect an internal temperature of the fuel cell stack.
Compared with the prior art, the utility model discloses during the use, absorb moisture through fuel cell air management device and accomplish preheating to the fuel cell galvanic pile is in the start-up of lower temperature, through the flow direction that detects the temperature of fuel cell galvanic pile and control air current, accomplishes the state control of fuel cell galvanic pile cold start, normal start and fuel cell air management device heat transfer.
Drawings
Fig. 1 is a schematic structural diagram of a fuel cell air management device provided in embodiment 1 of the present invention.
Fig. 2 is a structural diagram of a fuel cell air management device according to embodiment 1 of the present invention.
Fig. 3 is a schematic structural diagram of a fuel cell air management system according to embodiment 2 of the present invention.
Fig. 4 is a schematic diagram of an operating state of the fuel cell air management method according to embodiment 3 of the present invention.
Fig. 5 is a schematic flow chart of a fuel cell air management method according to embodiment 3 of the present invention.
Fig. 6 is a schematic diagram of the state of heat exchange of the fuel cell air management device in embodiment 4 of the present invention.
Fig. 7 is a schematic diagram of a state in which the fuel cell air management device of embodiment 4 of the present invention is operating normally.
Fig. 8 is a schematic flow chart of a fuel cell air management method according to embodiment 4 of the present invention.
Fig. 9 is a schematic flow chart of a fuel cell air management method according to embodiment 5 of the present invention.
Fig. 10 is a schematic flow chart of a fuel cell air management method according to embodiment 6 of the present invention.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
Referring to fig. 2, in an implementation process, the air management device of the fuel cell may adopt a sleeve-type structural design, and includes a solid adsorption-type heat reservoir shell 1091, a heat insulating layer 1092 and a solid adsorption-type heat reservoir tube 1093, where the solid adsorption-type heat reservoir shell 1091, the heat insulating layer 1092 and the solid adsorption-type heat reservoir tube 1093 can form a shell of a device body, and an internal cavity of the solid adsorption-type heat reservoir tube 1093 is a storage cavity; wherein, the space between the solid adsorption type heat reservoir shell 1091 and the solid adsorption type heat reservoir tube 1093 shell is filled with heat insulating material, thereby forming the heat preservation layer 1092, a filter screen 1095 is respectively arranged at the position where the input port 1096 of the device body and the output port 1097 of the device body are matched, specifically, a round filter screen 1095 with a sieve mesh is respectively welded at a certain distance from the air inlet and the air outlet in the solid adsorption type heat reservoir tube 1093, solid adsorption type heat reservoir particles 1094 are filled in the cavity enclosed between the two round filter screens 1095 and the inner wall of the solid adsorption type heat reservoir tube 1093, the pores inside the solid adsorption type heat reservoir particles 1094 and the gaps between the particles are flow channels of air, when the air passes through the flow channels, the moisture in the air and the heat reservoir particles 1094 are physically adsorbed and generate heat, and the heat is transferred to the fuel cell stack by the air flow, the fuel cell stack can be conveniently started at a lower temperature.
The solid adsorption heat storage particles 1094 filled in the solid adsorption heat storage tube 1093 include but are not limited to one or more of silica gel, activated carbon, activated alumina, Metal Organic Frameworks (MOFs), natural zeolite, artificial zeolite molecular sieves and other materials, and the heat storage particles 1094 are particles formed by porous adsorption solid materials with abundant micropores, mesopores and macropores, can absorb moisture to generate heat, and can discharge the absorbed moisture in a heating state. For example, the heat storage particles 1094 may be artificial zeolite molecular sieves, including but not limited to artificial zeolite molecular sieves such as 3A, 4A, 5A, 13X spheres, 13X bars, etc., and zeolite molecular sieves/CaCl 2, zeolite molecular sieves/MgCl 2, zeolite molecular sieves/MgSO 4, etc., and hydrated salt composite adsorption materials. The first temperature sensor 111 and the second temperature sensor 112 may be further provided, the first temperature sensor 111 measures the temperature of the device body output port 1097, the second temperature sensor 112 measures the internal temperature of the device body, when the heat storage particles 1094 need to be heated and moisture is discharged, so that the heat storage particles 1094 can be reused, the temperature difference between the temperature of the device body output port 1097 and the internal temperature of the device body can be detected, the temperature difference is monitored, when the temperature difference is smaller than a certain threshold value, that is, when the pore space of the heat storage particles 1094 does not have too much adsorbed moisture and needs heat energy to complete desorption, the temperature change can be regarded as heat conduction loss, and therefore, it can be determined that the heat storage particles 1094 basically completely desorb the adsorbed moisture.
Referring to fig. 3, in embodiment 2, a fuel cell air management system is provided, which includes an air supply unit 1, a fuel cell stack 2 and a fuel cell controller 3, wherein the air supply unit 1 is connected to the fuel cell stack 2, and the fuel cell controller 3 is in signal connection with the air supply unit 1 and the fuel cell stack 2, respectively. In practice, the air supply unit 1 comprises a humidifier 106 for humidifying air and a fuel cell air management device 109 for preheating air, and the humidified air can be preheated after passing through the fuel cell air management device 109; the fuel cell stack 2 communicates with the air supply unit 1; the fuel cell controller 3 is configured to control air input and output of the air supply unit 1 and the fuel cell stack 2, and the fuel cell controller 3 is in signal connection with the air supply unit 1 and the fuel cell stack 2, respectively. The air supply unit 1 further includes an air compressor 103, the air compressor 103 is configured to compress and heat air, and the air compressor 103 is in communication with the humidifier 106. The fuel cell air management system has three operating states: cold start, normal start and heat exchange with the fuel cell air management device. When the cold starting state is achieved, the air input and output of each unit and device are controlled, and the air flow direction is as follows: the air compressor 103 → the fuel cell stack 2 → the humidifier 106 → the fuel cell air management device 109 → the air compressor 103, heat generated when the air compressor 103 compresses air is absorbed by the fuel cell stack 2, the fuel cell air management device 109 absorbs moisture to complete pre-heating of air, and the pre-heated air is transmitted to the fuel cell stack 2 through the air compressor 103, and the fuel cell stack 2 is heated to a normal working temperature to complete cold start. When the air conditioner is in a normal starting state, the air flow direction is as follows by controlling the air input and output of each unit and device: the air compressor 103 → the humidifier 106 → the fuel cell stack 2, and the start-up temperature of the fuel cell stack 2 is at the temperature of normal operation and is normally started up. When the fuel cell stack is started normally from a cold start and is in a steady operation state, in order to discharge moisture absorbed by the fuel cell air management device 109 and facilitate reuse of the fuel cell air management device 109, the air flows in the following directions by controlling the air input and output of each unit and device: the air compressor 103 → the fuel cell air management device 109 → the humidifier 106 → the fuel cell stack 109, the air compressor 103 continuously compresses and heats the air, and the air is input into the fuel cell air management device 109, the heat storage particles are heated to discharge the moisture, and the heat exchange of the fuel cell air management device is further completed.
To facilitate the input and output of air for the control unit and device, the output port of the compressor 103 is respectively communicated with the input port of the humidifier 106 and the input port of the fuel cell stack 2 through the first valve 104, the output of the compressor 103 is also in communication with an input of a fuel cell air management device 109 and an input of the humidifier 106 via a second valve 105, the output port of the humidifier 106 is respectively communicated with the input port of the fuel cell stack 2 and the input port of the fuel cell air management device 109 through a third valve 107, the output port of the fuel cell stack 2 is respectively communicated with the exhaust port of the fuel cell stack 2 and the input port of the humidifier 106 through a fourth valve 108, an output port of the fuel cell air management device 109 communicates with an input port of the air compressor 103 and an input port of the humidifier 106, respectively, through a fifth valve 110. In the implementation process, the first valve 104, the second valve 105, the third valve 107, the fourth valve 108, and the fifth valve 110 all include three-way electromagnetic valves, interface switches of each passage in the three-way electromagnetic valves are controlled by the fuel cell controller 3, so as to realize the switching of the operating states of the fuel cell stack 2, the control signals may adopt signals or coding modes in various forms, and the control signals may adopt digital signals, and accordingly, the fuel cell controller 3 may adopt various units capable of realizing adjustable digital signals, such as various single-chip microcomputers, microcontrollers, DSPs (digital signal processors), FPGAs (Field-Programmable Gate arrays), upper computers, or Central Processing Units (CPUs), in this embodiment, the controller may adopt a single-chip microcomputer, and various control functions may be realized by programming the single-chip microcomputer, for example, in this embodiment, realize temperature signal's collection, processing and regulatory function to and can realize the switch of each three-way solenoid valve, the singlechip has the advantage that makes things convenient for the interface to call, be convenient for control.
The fuel cell air management system further comprises an air filter 101 for filtering and a sixth valve 102 for controlling the air flow, the air filter 101 is communicated with the sixth valve 102, the air filter 101 is arranged at the input port of the air supply unit 1 and is used for filtering floating objects, dust and impurity gases which are easy to poison a fuel cell catalyst in the air, and the sixth valve 102 can adopt a proportional valve, so that the opening degree of the proportional valve can be conveniently controlled, and the air flow of the air supply unit 1 can be further controlled. The fuel cell air management system also includes a first temperature sensor 111, a second temperature sensor 112 and a third temperature sensor 21, the first temperature sensor 111 is used to detect the temperature of the output port of the fuel cell air management device 109, the second temperature sensor 112 is used to detect the internal temperature of the fuel cell air management device 109, by collecting the temperature difference between the two parts, whether the air management device of the fuel cell needs energy to discharge water is judged, and thus whether heat exchange is required by the fuel cell air management device, the third temperature sensor 21 is used to detect the internal temperature of the fuel cell stack 2, the internal temperature of the fuel cell stack 2 is detected by the third temperature sensor 21, and a signal is transmitted to the fuel cell controller 3, so that the fuel cell controller 3 can conveniently switch the working states of cold start, normal start and heat exchange of the fuel cell air management device.
Referring to fig. 4 and 5, in embodiment 3, there is provided a fuel cell air management method, including:
s10, detecting the current temperature inside the fuel cell stack 2, and when the current temperature is lower than the normal working temperature threshold value, starting the air supply unit 1 and inputting air into the fuel cell stack 2;
s20, inputting air into a humidifier 106 through an output port of the fuel cell stack 2, and humidifying the air in the humidifier 106;
s30, inputting air into the fuel cell air management device 109 through the output port of the humidifier 106, and performing air pre-heating on the fuel cell air management device 109;
and S40, re-heating the air subjected to pre-heating by the air compressor 103, inputting the air into the fuel cell stack 2, preheating the fuel cell stack 2, and performing cold start on the fuel cell stack 2.
After the step of turning on the air supply unit and before the step of inputting air to the fuel cell stack 2, the fuel cell air management method further includes the steps of: an air compressor 103 for compressing and heating air is provided, and the air compressed and heated by the air compressor 103 is input to the fuel cell stack 2.
When T is reached after the step of cold starting the fuel cell stack 2C≤TF≤TSWhen the fuel cell stack 2 is operated at low power and generates heat, when T isS＜TFThen, the fuel cell stack 2 is normally operated, wherein TFIs the current temperature, T, of the fuel cell stackCFor cold start temperature threshold, TSIs a normal operating temperature threshold, TCAnd TSThe mathematical relationship of (a) is expressed as: t is more than or equal to minus 5 DEG CC≤0℃＜TS。
In the specific implementation process, the fuel cell controller 3 controls the opening of the first valve 104, the third valve 107, the fourth valve 108 and the fifth valve 110, and closes the second valve 105, then starts the air compressor 103 and appropriately adjusts the opening of the air proportional valve 102, the air in the environment purified by the air filter 101 is adiabatically compressed by the air compressor 103 to achieve the first temperature rise of the air, then the air carrying heat is sent to the fuel cell stack 2 and directly transfers the heat to the membrane electrode and the bipolar plate of the fuel cell stack 2, the air flowing out of the fuel cell stack 2 is humidified by the humidifier 106 and then enters the fuel cell air management device 109 with a large amount of water vapor, the heat storage particles 1094 begin to physically adsorb the water vapor, thereby reducing the freedom of water molecules and releasing a large amount of adsorption heat, supplementing heat to the air flow to realize secondary heating, returning the air flow subjected to heat supplementation to the air compressor 103 to heat again, and transferring more heat to the fuel cell stack 2 to accelerate preheating of the fuel cell stack 2 so as to meet the temperature requirement of normal operation of the fuel cell stack 2; meanwhile, the fuel cell controller 3 may completely close the air proportional valve 102 such that the air circulates in a path of the air compressor 103 → the first valve 104 → the fuel cell stack 2 → the fourth valve 108 → the humidifier 106 → the third valve 107 → the fuel cell air management device 109 → the first temperature sensor 111 → the fifth valve 110 → the air compressor 103, thereby continuously and progressively preheating the membrane electrodes and the bipolar plates of the fuel cell stack 2; when the fuel cell controller 3 detects that the temperature of the fuel cell stack 2 meets TC≤TF≤TSWhen the fuel cell stack 2 is started up with a small power and a large current (namely, the fuel cell stack 2 works with low power) and works for self-heating, the fuel cell stack 2 enables the generated electric energy to heat the temperature of the fuel cell stack in the form of ohmic polarization heat until TF＞TSCompleting the cold start operation of the fuel cell stack; for better heating, the opening degree of the air proportional valve 102 can be properly adjusted during the process, and the fourth valve 1 is opened intermittently08 is connected to the air exhaust line so that a portion of the air flows in to supply the fuel cell stack 2 with oxygen consumed by the autothermal process.
Referring to fig. 6, 7 and 8, in embodiment 4, there is provided a fuel cell air management method, including:
s11: detecting T of fuel cell stackF，
S21: judgment of TFWhether or not greater than TSWhen T isF＜TSWhen the fuel cell stack is in a cold start state, and when T is in a cold start stateF≥TSWhen the fuel cell stack is in a normal operating state, wherein TFIs the current temperature, T, of the fuel cell stackSA normal operating temperature threshold;
s31: judging T againFWhether or not greater than TSWhen T isF＜TSWhen the fuel cell stack is in a cold start state, and when T is in a cold start stateF≥TSWhen the fuel cell stack is in a normal working state;
s41: and heating air and inputting the heated air to a fuel cell air management device, wherein the fuel cell air management device exchanges heat, and then the air is input to a fuel cell stack after being humidified.
In the specific implementation process, the implementation process in the normal working state is as follows: the fuel cell controller 3 controls the opening of the first to fourth valves, and controls the opening of the air proportional valve 102, and closes the fifth valve 110, and then starts the air compressor 103 to make the air delivery path: air cleaner 101 → air proportional valve 102 → air compressor 103 → first valve 104 → second valve 105 → humidifier 106 → third valve 107 → fuel cell stack 2 → fourth valve 108 → discharge port of fuel cell stack 2; in the process, the high-pressure air generated by the air compressor 103 is humidified by the humidifier 106 and then directly enters the fuel cell stack 2 for subsequent electrochemical catalytic reaction or other operations, so that the fuel cell stack 2 is in a normal working state.
The specific implementation process of S41 is as follows: the fuel cell controller 3 controls the first to fifth valves and the air proportional valve 102 respectively, then starts the air compressor 103, so that the air in the environment is adiabatically compressed under the action of the air compressor 103 to generate a high-temperature air flow, the high-temperature air flow is input to the fuel cell air management device 109, moisture adsorbed by the heat storage particles 1094 in the fuel cell air management device 109 is desorbed from the adsorbent when heated, then is taken out by the high-speed air flow to complete pre-humidification of the air, the air flow after pre-humidification enters the humidifier 106 for humidification, and then enters the fuel cell stack 2 for electrocatalytic reduction reaction to output electric energy, and the delivery path of the air is: the air compressor 103 → the first valve 104 → the second valve 105 → the fuel cell air management device 109 → the humidifier 106 → the fuel cell stack 2.
In this process, the temperatures T displayed by the first temperature sensor 111 and the second temperature sensor 112 are monitored in real time by the fuel cell controller 3oAnd TiThe size change of (2), the temperature of first temperature sensor 111 measurement device body delivery outlet, the inside temperature of second temperature sensor 112 measurement device body, when needs heat the heat-retaining granule and discharge moisture to when heat-retaining granule used repeatedly, can be through the inside temperature of the temperature of detection device body delivery outlet and device body, and monitor the temperature difference between them, when the temperature difference is less than certain threshold value, do not have too much adsorbed moisture in the hole of heat-retaining granule 1094 promptly and need heat energy to accomplish the desorption, temperature variation can be regarded as the heat conduction loss, consequently can judge that the moisture that the heat-retaining granule adsorbs desorbs basically finishes desorbing. For example, when Ti-ToWhen the air flow rate is less than or equal to delta T, air is input into the fuel cell stack, and an input port and an output port of the fuel cell air management device are closed, wherein T isoFor the temperature, T, of the outlet of the fuel cell air management deviceiThe temperature delta T is the temperature inside the air management device of the fuel cell, and delta T is the temperature difference threshold value of the air management device of the fuel cell, wherein delta T is more than or equal to 0 ℃ and less than or equal to 10 ℃.
Referring to fig. 3 and 9, embodiment 5 provides a fuel cell air management method, including:
s12: detection ofMeasure TF；
S22: when T isF＜TCWhen the fuel cell stack is in a cold start state, the fuel cell stack is in a cold start state;
s23: when T isC≤TF≤TSWhen the fuel cell stack is in a low power state;
s24: when T isS＜TFThen, the fuel cell stack is normally operated, wherein TFIs the current temperature, T, of the fuel cell stackCFor cold start temperature threshold, TSIs a normal operating temperature threshold.
In the implementation process, the air flow direction in the cold start state refers to fig. 4, which specifically includes: air compressor 103 → fuel cell stack 2 → humidifier 106 → fuel cell air management device 109 → air compressor 103 → fuel cell stack 2;
referring to fig. 7, the air flow direction during normal start-up includes: air compressor 103 → humidifier 106 → fuel cell stack 2 → discharge port of fuel cell stack 2.
After cold start, the method further includes heat exchange by the fuel cell air management device, and the air flow direction of the heat exchange by the fuel cell air management device refers to fig. 6, which specifically includes: air compressor 103 → fuel cell air management device 109 → humidifier 106 → fuel cell stack 2 → discharge port of fuel cell stack 2.
Referring to fig. 3 and 10, embodiment 6 provides a fuel cell air management method, including:
s600: the fuel cell controller 3 reads the current temperature T of the fuel cell stack 2FThen comparing TFAnd TCAnd TSAnd go to S601, TFIs the current temperature, T, of the fuel cell stackCFor cold start temperature threshold, TSA normal operating temperature threshold;
s601: if the fuel cell controller 3 detects TF＜TCStep 602 is entered if T is detectedC≤TF≤TSStep 603 is entered if T is detectedF＞TSThen enter intoStep 604;
s602: entering a cold start, the fuel cell controller 3 controls the first valve 104, the third valve 107, the fourth valve 108 and the fifth valve 110 to be opened and the second valve 105 to be closed respectively, and then starts the air compressor 103 and appropriately adjusts the opening degree of the air proportional valve 102; after a certain time interval, the fuel cell controller 3 closes the air proportional valve 102 to enable the air to form a closed circulation loop among the air compressor 103, the fuel cell stack 2, the humidifier 106 and the fuel cell air management device 109 so as to continuously and progressively preheat the membrane electrode and the bipolar plate of the fuel cell stack; then returning to S601 to monitor and compare T in real timeFAnd TC、TSThe size change in between;
s603: the fuel cell controller 3 controls the opening of the first valve 104, the third valve 107, the fourth valve 108 and the fifth valve 110, closes the second valve 105, then starts the air compressor 103 and properly adjusts the opening degree of the air proportional valve 102, and then starts (operates at low power) the fuel cell stack 2 at low power and high current to accelerate the warming-up of the electric energy generated by the fuel cell stack 2 in the form of ohmic polarization heat; during the process, the opening degree of the air proportional valve 102 is properly adjusted, the passage connected with the air tail exhaust pipeline of the fourth valve 108 is intermittently opened to replenish the oxygen consumed in the thermal process, and then the process returns to S601 to monitor and compare T in real timeFAnd TC、TSThe size change in between;
s604: entering normal operation, the fuel cell controller 3 controls the first to fourth valves and the air proportional valve 102 to open respectively, closes the fifth valve 110, and then starts the air compressor 103 to complete low-temperature start of the fuel cell and subsequent power output or other operations of the fuel cell; then receiving the real-time driving state of the fuel cell vehicle transmitted by the vehicle controller in real time and entering S610;
s610: judging whether heat exchange is needed or not, and starting to detect whether the fuel cell automobile is in a stable running state or not and whether the fuel cell air management device 109 needs desorption regeneration or not by the fuel cell controller 3; if yes, entering S611, otherwise, returning to S604;
s611: performing heat exchange of a fuel cell air management device, wherein the fuel cell controller 3 controls the first valve to the fifth valve and controls the air proportional valve 102 to be opened, then starting the air compressor 103 to enable air in the environment to be subjected to adiabatic compression under the action of the air compressor 103 to generate high-temperature air flow, the high-temperature air flow flows through the fuel cell air management device 109, moisture adsorbed by heat storage particles is desorbed from an adsorbent in response to heat and is taken out by the high-speed air flow, at the moment, the fuel cell air management device 109 completes pre-humidification of the air, the air flow subjected to the pre-humidification enters the humidifier 106 for humidification, and then the air flow is input to the fuel cell stack 2 to perform an electrocatalytic reduction reaction to output electric energy; during the process, the fuel cell controller 3 monitors the temperatures T displayed by the first temperature sensor 111 and the second temperature sensor 112 in real timeoAnd TiThen proceeds to S612.
In S612, the fuel cell controller 3 detects the presence or absence of Ti-ToIn the case of ≦ Δ T, ToFor the temperature, T, of the outlet of the fuel cell air management deviceiThe temperature of the inside of the air management device of the fuel cell is regarded as delta T, the delta T is the temperature difference threshold value of the air management device of the fuel cell, and the delta T is more than or equal to 0 ℃ and less than or equal to 10 ℃: if yes, go to S613; otherwise, returning to S611.
In S613, the fuel cell controller 3 controls the second valve 105 to open the passage connected to the humidifier 106 and close the fifth valve 110, thereby completing the desorption/regeneration of the stored heat particles and preparing for the next low-temperature start of the fuel cell.
In summary, the present application has the following features:
(1) the heat storage density is large and far higher than that of a sensible heat and latent heat energy storage mode, so that the using amount and the volume of materials can be reduced, and particularly, the zeolite/water working medium pair has the advantages of relatively high energy storage density and energy density, strong absorption capacity, large adsorption heat value, high adsorption speed and the like;
(2) the temperature rising speed is high, and the adsorption heat is utilized to perform heat supplementing and temperature rising on the air at the inlet of the air compressor;
(3) the environment adaptability is strong, when the air management device of the fuel cell is closed, namely no air flow passes through, the heat storage particles are always in an energy storage state and are not limited by time and environment temperature, and long-time heat insulation is not needed, so that the cost of the device is reduced;
(4) the energy utilization rate is high, and the preheating process does not need external power supply heating or hydrogen combustion heating; the regeneration process fully utilizes the heat energy generated by the air compressor doing work on the air to realize the heat exchange process of the heat storage particles, so that the heat energy generated by the air compressor during working is stored in the heat storage particles, the temperature of the air flowing out of the air compressor is reduced, the extra energy consumption is greatly reduced, the pre-humidification of the air is realized, the energy consumption of the humidifier is reduced, and the endurance mileage of the fuel cell automobile is further prolonged.
The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any changes or substitutions that can be easily conceived by those skilled in the art within the technical scope of the present invention should be covered by the present invention. Therefore, the protection scope of the present invention shall be subject to the protection scope of the claims.
Claims (10)
1. A fuel cell air management device, comprising: the device body and setting are in this internal heat-retaining granule of device, the device body still includes device body input port and device body delivery outlet.
2. The fuel cell air management device according to claim 1 wherein said heat storage particles comprise silica gel, activated carbon, activated alumina, metal organic frameworks, or zeolites.
3. The fuel cell air management device according to claim 1 or 2 wherein said device body comprises a storage chamber for loading heat storage particles and a housing for thermal insulation.
4. The fuel cell air management device according to claim 1 wherein a screen is provided at each of matching positions of said device body inlet and said device body outlet.
5. A fuel cell air management system, comprising:
an air supply unit comprising a humidifier for humidifying air and the fuel cell air management device of any one of claims 1 to 4, the humidified air being able to be preheated as it passes through the fuel cell air management device;
a fuel cell stack in communication with the air supply unit;
and the fuel cell controller is used for controlling the air input and output of the air supply unit and the fuel cell stack, and is respectively in signal connection with the air supply unit and the fuel cell stack.
6. The fuel cell air management system according to claim 5 wherein said air supply unit further comprises an air compressor for compressing and heating air, said air compressor communicating with said humidifier.
7. The fuel cell air management system according to claim 6 wherein an output of said compressor is in communication with an input of a humidifier and an input of a fuel cell stack, respectively, via a first valve, the output port of the compressor is also respectively communicated with the input port of the fuel cell air management device and the input port of the humidifier through a second valve, the output port of the humidifier is respectively communicated with the input port of the fuel cell stack and the input port of the fuel cell air management device through a third valve, the output port of the fuel cell stack is respectively communicated with the exhaust port of the fuel cell stack and the input port of the humidifier through a fourth valve, and an output port of the air management device of the fuel cell is respectively communicated with an input port of the air compressor and an input port of the humidifier through a fifth valve.
8. The fuel cell air management system according to claim 7 wherein said first valve, said second valve, said third valve, said fourth valve and said fifth valve each comprise a three-way solenoid valve.
9. The fuel cell air management system according to claim 5 or 6 further comprising an air filter for filtering and a sixth valve for controlling air flow, said air filter communicating with said sixth valve.
10. The fuel cell air management system according to claim 5 further comprising a first temperature sensor for sensing the temperature of an output port of said fuel cell air management device, a second temperature sensor for sensing the internal temperature of said fuel cell air management device, and a third temperature sensor for sensing the internal temperature of said fuel cell stack.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921792420.2U CN212209663U (en) | 2019-10-23 | 2019-10-23 | Fuel cell air management device and system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921792420.2U CN212209663U (en) | 2019-10-23 | 2019-10-23 | Fuel cell air management device and system |
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| CN212209663U true CN212209663U (en) | 2020-12-22 |
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