CN207896211U - A kind of air gas supply humidification ICS intercooler system for Proton Exchange Membrane Fuel Cells - Google Patents
A kind of air gas supply humidification ICS intercooler system for Proton Exchange Membrane Fuel Cells Download PDFInfo
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Abstract
本实用新型公开了一种用于质子交换膜燃料电池的空气供气增湿中冷系统。所述系统连接在燃料电池堆处,燃料电池堆具有用于循环冷却水的冷却回路。增湿中冷系统包括:增湿中冷器、增湿支路和气水分离器。增湿中冷器连接在包括空气滤清器和空压机的供气支路上,用于冷却并加湿进入燃料电池堆之前的空气。增湿支路连通冷却回路中冷却水泵的出口及增湿中冷器冷却水入口,用于为增湿中冷器输送冷却水。气水分离器连通增湿中冷器的空气出口及电堆空气入口。本实用新型兼备中冷和增湿功能,无需专门设置增湿水路,降温增湿环节无需电动控制,适用于大功率燃料电池系统且有助于大幅缩减系统成本。
The utility model discloses an air supply, humidification and intercooling system for a proton exchange membrane fuel cell. The system is connected to a fuel cell stack which has a cooling circuit for circulating cooling water. The humidification and intercooling system includes: a humidification intercooler, a humidification branch and a gas-water separator. The humidifying intercooler is connected to the air supply branch including the air filter and the air compressor, and is used for cooling and humidifying the air before entering the fuel cell stack. The humidification branch is connected with the outlet of the cooling water pump in the cooling circuit and the cooling water inlet of the humidification intercooler, and is used for delivering cooling water to the humidification intercooler. The air-water separator communicates with the air outlet of the humidifying intercooler and the air inlet of the stack. The utility model has the functions of intercooling and humidification, does not need to specially set up a humidification waterway, and does not need electric control in the cooling and humidification link, is suitable for high-power fuel cell systems and helps to greatly reduce system costs.
Description
技术领域technical field
本实用新型涉及质子交换膜燃料电池,尤其涉及一种用于质子交换膜燃料电池的空气供气增湿中冷系统。The utility model relates to a proton exchange membrane fuel cell, in particular to an air supply humidification intercooling system for the proton exchange membrane fuel cell.
背景技术Background technique
质子交换膜燃料电池(以下简称燃料电池)功率密度高、效率高、工作温度低、产物无污染等优势使其非常适合于车载使用;而且相对于锂离子电池作主动力的纯电动汽车而言,燃料电池汽车可以有效解决里程焦虑问题,极具发展前景。Proton exchange membrane fuel cells (hereinafter referred to as fuel cells) have the advantages of high power density, high efficiency, low operating temperature, and non-polluting products, making them very suitable for vehicle use; and compared to pure electric vehicles with lithium-ion batteries as the main power , Fuel cell vehicles can effectively solve the problem of mileage anxiety and have great development prospects.
燃料电池作为一种电化学动力源,其工作需要在空气供给系统、氢气供给系统、冷却系统等子系统的配合下完成。燃料电池对内部水状态非常敏感。内部缺水会导致:(1)质子交换膜脱水,质子传导能力下降,电堆欧姆阻抗升高;(2)催化层催化活性降低,燃料电池活化损失增大。而内部液态水的集聚会阻碍反应气体扩散到催化层参与反应,可能会导致燃料电池水淹。缺水和水的过量都会造成燃料电池性能下降,由此说明为燃料电池反应气体提供增湿是必要的,而且增湿必须恰当。As an electrochemical power source, the fuel cell needs to be completed with the cooperation of air supply system, hydrogen supply system, cooling system and other subsystems. Fuel cells are very sensitive to internal water conditions. The lack of internal water will lead to: (1) dehydration of the proton exchange membrane, the decrease of proton conductivity, and the increase of the ohmic impedance of the stack; (2) the decrease of the catalytic activity of the catalytic layer, and the increase of the activation loss of the fuel cell. The accumulation of internal liquid water will hinder the reaction gas from diffusing to the catalytic layer to participate in the reaction, which may cause the fuel cell to flood. Both lack of water and excess of water will cause the performance of the fuel cell to decline, which shows that it is necessary to provide humidification for the reaction gas of the fuel cell, and the humidification must be appropriate.
目前,有通过合理设计燃料电池堆和流场的结构的方式实现电堆内部自增湿的方案,丰田Mirai燃料电池堆的三维流场设计就属于内部增湿。但是结构设计难度较大,工艺要求复杂,控制变量多,而且增湿效果有限。At present, there is a scheme to achieve self-humidification inside the stack by rationally designing the structure of the fuel cell stack and the flow field. The three-dimensional flow field design of the Toyota Mirai fuel cell stack belongs to internal humidification. However, the structural design is difficult, the process requirements are complex, the control variables are many, and the humidification effect is limited.
目前,还有液态水喷雾增湿法,该方法在大功率燃料电池系统中应用比较广泛,可以同时起到空气的增湿中冷作用。但是,目前的喷雾增湿系统存在明显的技术弱点,主要包括:At present, there is also a liquid water spray humidification method, which is widely used in high-power fuel cell systems, and can also play the role of air humidification and cooling. However, the current spray humidification system has obvious technical weaknesses, mainly including:
(1)为液态水喷雾需要另外构建水路。若新构建水路无加热,则增湿效果差;若新构建水路有加热,则系统结构进一步复杂化。(1) It is necessary to separately construct a water channel for liquid water spray. If the newly constructed waterway is not heated, the humidification effect will be poor; if the newly constructed waterway is heated, the system structure will be further complicated.
(2)喷雾容腔内部结构设计考虑不足,降温增湿效果不理想,需要依靠喷水量控制;容腔结构优化空间较大。(2) The internal structure design of the spray chamber is insufficiently considered, and the effect of cooling and humidifying is not ideal, and it is necessary to rely on the control of the amount of water sprayed; there is a large space for optimizing the structure of the chamber.
(3)控制增湿器内部水位。通过控制规避增湿器内部液态水过多造成故障,使得系统控制复杂化,降低系统可靠性。(3) Control the water level inside the humidifier. By controlling and avoiding excessive liquid water inside the humidifier and causing failures, the system control is complicated and the system reliability is reduced.
实用新型内容Utility model content
本实用新型旨在至少解决现有技术中存在的技术问题之一。为此,本实用新型提出一种用于质子交换膜燃料电池的空气供气增湿中冷系统。The utility model aims at at least solving one of the technical problems existing in the prior art. For this reason, the utility model proposes an air supply air humidification intercooler system for proton exchange membrane fuel cells.
本实用新型提供的一种用于质子交换膜燃料电池的空气供气增湿中冷系统,连接在燃料电池堆处,所述燃料电池堆具有电堆冷却水入口、电堆冷却水出口及电堆空气入口,所述燃料电池堆具有冷却回路以循环冷却水,其中,冷却水经过冷却水泵,从所述电堆冷却水入口进入所述燃料电池堆,经所述电堆冷却水出口进入散热器,散热后经所述冷却水泵进入所述电堆冷却水入口实现循环,所述空气供气增湿中冷系统包括:The utility model provides an air supply humidification intercooling system for proton exchange membrane fuel cells, which is connected to the fuel cell stack. The fuel cell stack has a stack cooling water inlet, a stack cooling water outlet and a The stack air inlet, the fuel cell stack has a cooling circuit to circulate cooling water, wherein the cooling water passes through the cooling water pump, enters the fuel cell stack from the stack cooling water inlet, and enters the heat dissipation through the stack cooling water outlet After dissipating heat, it enters the stack cooling water inlet through the cooling water pump to realize circulation. The air supply humidification and intercooling system includes:
增湿中冷器,连接在包括空气滤清器和空压机的供气支路上,用于冷却并加湿进入所述燃料电池堆之前的空气,所述增湿中冷器具有增湿中冷器冷却水入口、增湿中冷器空气入口及增湿中冷器空气出口;A humidifying intercooler, connected to the air supply branch including an air filter and an air compressor, for cooling and humidifying the air before entering the fuel cell stack, the humidifying intercooler has a humidifying intercooler Cooling water inlet of humidifier, air inlet of humidifying intercooler and air outlet of humidifying intercooler;
增湿支路,连通所述冷却水泵的出口及所述增湿中冷器冷却水入口,用于为所述增湿中冷器输送冷却水;和a humidification branch, connected to the outlet of the cooling water pump and the cooling water inlet of the humidification intercooler, for delivering cooling water to the humidification intercooler; and
气水分离器,连通所述增湿中冷器空气出口及所述电堆空气入口,用于分离增湿空气中的液态水,具有气水分离器入口、气水分离器出口及气水分离器排水口;The air-water separator is connected to the air outlet of the humidification intercooler and the air inlet of the electric stack, and is used to separate the liquid water in the humidified air, and has an inlet of the air-water separator, an outlet of the air-water separator and an air-water separation drain outlet;
其中,空气依次经所述空气滤清器、所述空压机、所述增湿中冷器和所述气水分离器,从所述电堆空气入口进入所述燃料电池堆参与阴极反应。Wherein, the air passes through the air filter, the air compressor, the humidifying intercooler and the gas-water separator in sequence, and enters the fuel cell stack from the stack air inlet to participate in the cathode reaction.
进一步地,所述冷却水泵流量固定,通过控制所述散热器中的冷却风扇起停和转速来控制冷却水温度,以此保证所述冷却水泵的出口的水压恒定。Further, the flow rate of the cooling water pump is fixed, and the temperature of the cooling water is controlled by controlling the start, stop and rotation speed of the cooling fan in the radiator, so as to ensure a constant water pressure at the outlet of the cooling water pump.
进一步地,所述的空气供气增湿中冷系统中,Further, in the air supply humidification intercooling system,
ΔP=Ppump-Phumidifier ΔP=P pump -P humidifier
ΔP是所述冷却水泵出口压力与所述的空气供气增湿中冷系统额定工作状态下增湿中冷器内腔喷嘴出口处空气压力的压力差,ΔP is the pressure difference between the outlet pressure of the cooling water pump and the air pressure at the nozzle outlet of the inner chamber of the humidification intercooler under the rated working condition of the air supply humidification intercooler system,
Ppump是所述冷却水泵出口压力,P pump is the outlet pressure of the cooling water pump,
Phumidifier是所述空气供气增湿中冷系统额定工作状态下增湿中冷器内腔喷嘴出口处空气压力,P humidifier is the air pressure at the outlet of the nozzle of the inner chamber of the humidification intercooler under the rated working condition of the air supply humidification intercooler system,
若ΔP<1bar,所述空气供气增湿中冷系统还包括布置在所述增湿中冷器冷却水入口之前的增压水泵;If ΔP<1 bar, the air supply humidification intercooler system further includes a booster water pump arranged before the cooling water inlet of the humidification intercooler;
若ΔP≥1bar,所述空气供气增湿中冷系统无需增设所述增压水泵。If ΔP≥1 bar, the air supply humidification and intercooling system does not need to add the booster water pump.
进一步地,所述增压水泵具有增压水泵入口及增压水泵出口,通过保持所述增压水泵出口的水压恒定值,以保证所述的增湿中冷器的冷却水入口水压恒定。Further, the booster water pump has a booster water pump inlet and a booster water pump outlet, and by keeping the water pressure at the outlet of the booster water pump at a constant value, the water pressure at the cooling water inlet of the humidifying intercooler is guaranteed to be constant. .
进一步地,所述增湿中冷器与所述气水分离器在普通工作状态下均沿竖直方向布置,所述增湿中冷器空气出口与所述气水分离器入口固联,所述气水分离器排水口竖直向下。Further, the humidification intercooler and the air-water separator are arranged in a vertical direction under normal working conditions, and the air outlet of the humidification intercooler is fixedly connected with the inlet of the air-water separator. The outlet of the air-water separator is vertically downward.
进一步地,所述增湿中冷器包括:Further, the humidifying intercooler includes:
壳体,其上具有所述增湿中冷器空气入口及所述增湿中冷器空气出口;a shell with the air inlet of the humidification intercooler and the air outlet of the humidification intercooler;
顶盖,覆盖在所述壳体的顶部,并与所述壳体固定连接;a top cover, covering the top of the housing, and fixedly connected with the housing;
压力雾化喷嘴,安装在所述顶盖处,其具有入口及出口,所述入口即为所述增湿中冷器冷却水入口;和A pressure atomizing nozzle installed at the top cover, which has an inlet and an outlet, and the inlet is the cooling water inlet of the humidifying intercooler; and
导流翅片,安装在所述壳体的内部并位于所述压力雾化喷嘴的下方。The guide fins are installed inside the housing and located below the pressure atomizing nozzle.
进一步地,所述压力雾化喷嘴的入口、出口压力固定,维持固定喷雾水量,该水量最小值为空气流量最大时所对应的饱和增湿水量,计算公式为:Further, the pressure at the inlet and outlet of the pressure atomizing nozzle is fixed to maintain a fixed spray water volume, the minimum water volume is the saturated humidification water volume corresponding to the maximum air flow rate, and the calculation formula is:
式中, In the formula,
为压力雾化喷嘴最小喷雾水量,单位:g/s; is the minimum spray water volume of the pressure atomizing nozzle, unit: g/s;
Psat,T为在电堆工作温度T下的饱和蒸气压,单位:Pa;P sat,T is the saturated vapor pressure at the working temperature T of the stack, unit: Pa;
Pair,in为空气入堆压力,单位:Pa;P air,in is the pressure of air entering the stack, unit: Pa;
为最大空气流量,单位:SLPM。 is the maximum air flow, unit: SLPM.
进一步地,所述导流翅片的数量为多个且呈交错布置,以强迫空气在所述增湿中冷器内部作曲折流动,延长空气运动长度。Further, the number of the guide fins is multiple and arranged in a staggered manner, so as to force the air to make zigzag flow inside the humidification intercooler and prolong the length of the air movement.
进一步地,所述气水分离器为压缩空气气水分离器,以分离出增湿空气中的液态水,并保证在不影响空气压力的情况下自动排出所述液态水。Further, the gas-water separator is a compressed air gas-water separator to separate the liquid water in the humidified air and ensure that the liquid water is automatically discharged without affecting the air pressure.
进一步地,所述增湿中冷器内部聚集的液态水在空气吹扫和重力作用下排入所述气水分离器,被分离后自动排出,所述气水分离器同时起到排除所述增湿中冷器内腔余水和增湿空气去水后处理的作用。Further, the liquid water accumulated inside the humidifying intercooler is discharged into the gas-water separator under the action of air blowing and gravity, and is automatically discharged after being separated. The gas-water separator simultaneously functions to eliminate the The effect of the residual water in the humidification intercooler and the dehydration of the humidified air.
本实用新型空气供气增湿中冷系统中的加湿中冷器集有效增湿和中冷功能于一体,避免了在增湿器外另外使用中冷器的复杂设计,简化了系统结构;本实用新型直接利用冷却水路为增湿中冷器提供液态水,省去了为增湿中冷器另外增设的复杂水路,简化了冷却水喷雾增湿的系统结构,且提供的冷却水泵出口冷却水温度较高,可以增强增湿效果;本实用新型空气供气增湿中冷系统的降温增湿环节无需任何控制,提升了系统的可靠性。The humidification intercooler in the air supply humidification intercooling system of the utility model integrates effective humidification and intercooling functions, avoids the complicated design of using an intercooler outside the humidifier, and simplifies the system structure; The utility model directly uses the cooling water circuit to provide liquid water for the humidification intercooler, which saves the additional complicated water circuit for the humidification intercooler, simplifies the system structure of cooling water spray humidification, and provides cooling water at the outlet of the cooling water pump The temperature is higher, which can enhance the humidification effect; the cooling and humidification link of the air supply humidification intercooling system of the utility model does not need any control, which improves the reliability of the system.
本实用新型的附加方面和优点将在下面的描述中部分给出,部分将从下面的描述中变得明显,或通过本实用新型的实践了解到。Additional aspects and advantages of the invention will be set forth in the description which follows, and in part will be obvious from the description, or may be learned by practice of the invention.
附图说明Description of drawings
本实用新型的上述和/或附加的方面和优点从结合下面附图对实施例的描述中将变得明显和容易理解,其中:The above and/or additional aspects and advantages of the present utility model will become apparent and easy to understand from the description of the embodiments in conjunction with the following drawings, wherein:
图1是本实用新型实施例的用于质子交换膜燃料电池的空气供气增湿中冷系统结构示意图;Fig. 1 is the structural schematic diagram of the air supply humidification intercooler system for the proton exchange membrane fuel cell of the utility model embodiment;
图2是图1中的增湿中冷器与气水分离器的装配结构示意图;Fig. 2 is a schematic diagram of the assembly structure of the humidifying intercooler and the gas-water separator in Fig. 1;
图3是图1中的增湿中冷器组成结构示意图。Fig. 3 is a schematic diagram of the composition and structure of the humidifying intercooler in Fig. 1 .
附图标记:Reference signs:
1空气滤清器,1 air filter,
2空压机,2 air compressors,
3增湿中冷器,3 humidifying intercoolers,
31顶盖,32压力雾化喷嘴,33壳体,34导流翅片,35增湿中冷器空气入口,36增湿中冷器空气出口,37增湿中冷器冷却水入口,31 Top cover, 32 Pressure atomizing nozzle, 33 Housing, 34 Guide fins, 35 Humidification intercooler air inlet, 36 Humidification intercooler air outlet, 37 Humidification intercooler cooling water inlet,
4气水分离器,4 gas water separator,
41气水分离器入口,42气水分离器出口,43气水分离器排水口,41 gas-water separator inlet, 42 gas-water separator outlet, 43 gas-water separator outlet,
5燃料电池堆,5 fuel cell stacks,
51电堆冷却水入口,52电堆空气入口,53电堆冷却水出口,51 stack cooling water inlet, 52 stack air inlet, 53 stack cooling water outlet,
6散热器,6 radiators,
7冷却水泵,7 cooling water pumps,
8增压水泵。8 Booster water pumps.
具体实施方式Detailed ways
下面详细描述本实用新型的实施例,所述实施例的示例在附图中示出,其中自始至终相同或类似的标号表示相同或类似的元件或具有相同或类似功能的元件。下面通过参考附图描述的实施例是示例性的,仅用于解释本实用新型,而不能理解为对本实用新型的限制。Embodiments of the present invention are described in detail below, examples of which are shown in the drawings, wherein the same or similar reference numerals represent the same or similar elements or elements having the same or similar functions throughout. The embodiments described below with reference to the accompanying drawings are exemplary and are only used to explain the present utility model, but should not be construed as limiting the present utility model.
图1是本实用新型实施例的用于质子交换膜燃料电池的空气供气增湿中冷系统结构示意图。一种用于质子交换膜燃料电池的空气供气增湿中冷系统,连接在燃料电池堆5处,所述燃料电池堆5具有电堆冷却水入口51、电堆冷却水出口53及电堆空气入口52,所述燃料电池堆5具有冷却回路以循环冷却水。其中,冷却水经过冷却水泵7,从所述电堆冷却水入口51进入所述燃料电池堆5,经所述电堆冷却水出口53进入散热器6,散热后经所述冷却水泵7进入所述电堆冷却水入口51实现循环。所述空气供气增湿中冷系统包括:增湿中冷器3、增湿支路和气水分离器4。增湿中冷器3连接在包括空气滤清器1和空压机2的供气支路上,用于冷却并加湿进入所述燃料电池堆5之前的空气,所述增湿中冷器3具有增湿中冷器冷却水入口37、增湿中冷器空气入口35及增湿中冷器空气出口36。增湿支路连通所述冷却水泵7的出口及所述增湿中冷器冷却水入口37,用于为所述增湿中冷器3输送冷却水。气水分离器4连通所述增湿中冷器空气出口36及所述电堆空气入口52,用于分离增湿空气中的液态水,具有气水分离器入口41、气水分离器出口42及气水分离器排水口43。其中,空气依次经所述空气滤清器1、所述空压机2进入所述增湿中冷器3,增湿中冷器3喷射液态水,液态水气化的同时将空气增湿并冷却,之后增湿空气经所述气水分离器4去除液态水后,从所述电堆空气入口52进入所述燃料电池堆5参与阴极反应。Fig. 1 is a schematic structural diagram of an air supply, humidification and intercooling system for a proton exchange membrane fuel cell according to an embodiment of the present invention. An air supply humidification intercooling system for proton exchange membrane fuel cells, connected to a fuel cell stack 5, the fuel cell stack 5 has a stack cooling water inlet 51, a stack cooling water outlet 53 and a stack Air inlet 52, the fuel cell stack 5 has a cooling circuit to circulate cooling water. Wherein, the cooling water passes through the cooling water pump 7, enters the fuel cell stack 5 from the stack cooling water inlet 51, enters the radiator 6 through the stack cooling water outlet 53, and enters the fuel cell stack 5 through the cooling water pump 7 after dissipating heat. The stack cooling water inlet 51 realizes circulation. The air supply humidification and intercooling system includes: a humidification intercooler 3 , a humidification branch and an air-water separator 4 . The humidifying intercooler 3 is connected to the air supply branch road including the air filter 1 and the air compressor 2, and is used for cooling and humidifying the air before entering the fuel cell stack 5. The humidifying intercooler 3 has The cooling water inlet 37 of the humidifying intercooler, the air inlet 35 of the humidifying intercooler and the air outlet 36 of the humidifying intercooler. The humidification branch connects the outlet of the cooling water pump 7 and the cooling water inlet 37 of the humidification intercooler, and is used for delivering cooling water to the humidification intercooler 3 . The gas-water separator 4 communicates with the air outlet 36 of the humidifying intercooler and the air inlet 52 of the stack, and is used to separate the liquid water in the humidified air, and has a gas-water separator inlet 41 and a gas-water separator outlet 42 And gas-water separator outlet 43. Wherein, the air enters the humidification intercooler 3 through the air filter 1 and the air compressor 2 successively, and the humidification intercooler 3 sprays liquid water, and the air is humidified and dehumidified while the liquid water is vaporized. After cooling, the humidified air passes through the gas-water separator 4 to remove liquid water, and enters the fuel cell stack 5 from the stack air inlet 52 to participate in the cathode reaction.
本实用新型空气供气增湿中冷系统采用喷雾增湿法为空压机2排出的高热低湿空气降温增湿。加湿中冷器集有效增湿和中冷功能于一体,避免了在增湿器外另外使用中冷器的复杂设计,简化了系统结构。本实用新型直接利用冷却水路为增湿中冷器3提供液态水,省去了为增湿中冷器3另外增设的复杂水路,简化了冷却水喷雾增湿的系统结构,且提供的冷却水泵7出口冷却水温度较高,可以增强增湿效果。本实用新型空气供气增湿中冷系统的降温增湿环节无需任何控制,提升了系统的可靠性。本实用新型适用于大功率燃料电池系统且有助于大幅缩减系统成本。The air supply humidification and intercooling system of the utility model adopts the spray humidification method to cool and humidify the high-heat and low-humidity air discharged from the air compressor 2 . The humidification intercooler integrates effective humidification and intercooling functions, which avoids the complicated design of using an intercooler outside the humidifier and simplifies the system structure. The utility model directly uses the cooling water path to provide liquid water for the humidification intercooler 3, which saves the additional complicated water path for the humidification intercooler 3, simplifies the system structure of cooling water spray humidification, and provides a cooling water pump 7 The outlet cooling water temperature is higher, which can enhance the humidification effect. The air supply humidification intercooling system of the utility model does not need any control in the cooling and humidification link, which improves the reliability of the system. The utility model is suitable for a high-power fuel cell system and helps to greatly reduce the system cost.
进一步地,如图1所示,本实施例中,所述冷却水泵7流量固定,通过控制所述散热器6中的冷却风扇起停和转速来控制冷却水温度,以此保证所述冷却水泵7的出口的水压恒定。Further, as shown in FIG. 1 , in this embodiment, the flow rate of the cooling water pump 7 is fixed, and the temperature of the cooling water is controlled by controlling the cooling fan in the radiator 6 to start, stop and rotate, so as to ensure that the cooling water pump The water pressure of the outlet of 7 is constant.
进一步地,如图1所示,本实施例中,进一步地,所述的空气供气增湿中冷系统中,Further, as shown in Figure 1, in this embodiment, further, in the air supply humidification and intercooling system,
ΔP=Ppump-Phumidifier ΔP=P pump -P humidifier
ΔP是所述冷却水泵7出口压力与所述的空气供气增湿中冷系统额定工作状态下增湿中冷器3内腔喷嘴出口处空气压力的压力差,ΔP is the pressure difference between the outlet pressure of the cooling water pump 7 and the air pressure at the outlet of the inner cavity nozzle of the humidification intercooler 3 under the rated working condition of the air supply humidification intercooler system,
Ppump是所述冷却水泵7出口压力,P pump is the outlet pressure of the cooling water pump 7,
Phumidifier是所述空气供气增湿中冷系统额定工作状态下增湿中冷器3内腔喷嘴出口处空气压力,P humidifier is the air pressure at the outlet of the inner cavity nozzle of the humidification intercooler 3 under the rated working condition of the air supply humidification intercooler system,
若ΔP<1bar,所述空气供气增湿中冷系统还包括布置在所述增湿中冷器冷却水入口37之前的增压水泵8;If ΔP<1 bar, the air supply humidification intercooler system further includes a booster water pump 8 arranged before the cooling water inlet 37 of the humidification intercooler;
若ΔP≥1bar,所述空气供气增湿中冷系统无需增设所述增压水泵8。更进一步地,所述增压水泵8具有增压水泵入口及增压水泵出口,通过保持所述增压水泵出口的水压恒定值,以保证所述增湿中冷器冷却水入口37水压恒定。If ΔP≥1 bar, the air supply humidification and intercooling system does not need to add the booster water pump 8 . Furthermore, the booster water pump 8 has a booster water pump inlet and a booster water pump outlet, and by maintaining a constant value of the water pressure at the outlet of the booster water pump, the hydraulic pressure of the cooling water inlet 37 of the humidification intercooler is guaranteed. constant.
图2是图1中的增湿中冷器与气水分离器的装配结构示意图。图3是图1中的增湿中冷器组成结构示意图。参见图2,还可以参见图3,进一步地,本实施例中,所述增湿中冷器3与所述气水分离器4在普通工作状态下均沿竖直方向布置,所述增湿中冷器空气出口36与所述气水分离器入口41固联,所述气水分离器排水口43竖直向下。更进一步地,所述气水分离器4为压缩空气气水分离器,以分离出增湿空气中的液态水,并保证在不影响空气压力的情况下自动排出所述液态水。更进一步地,所述增湿中冷器3内部聚集的液态水在空气吹扫和重力作用下排入所述气水分离器4,被分离后自动排出,所述气水分离器4同时起到排除所述增湿中冷器3内腔余水和增湿空气去水后处理的作用。Fig. 2 is a schematic diagram of the assembly structure of the humidifying intercooler and the gas-water separator in Fig. 1 . Fig. 3 is a schematic diagram of the composition and structure of the humidifying intercooler in Fig. 1 . Referring to Fig. 2 and Fig. 3, further, in this embodiment, the humidification intercooler 3 and the gas-water separator 4 are arranged in the vertical direction under normal working conditions, and the humidification The air outlet 36 of the intercooler is fixedly connected with the inlet 41 of the air-water separator, and the water outlet 43 of the air-water separator is vertically downward. Furthermore, the gas-water separator 4 is a compressed air gas-water separator to separate the liquid water in the humidified air and ensure that the liquid water is automatically discharged without affecting the air pressure. Furthermore, the liquid water accumulated inside the humidifying intercooler 3 is discharged into the gas-water separator 4 under the action of air blowing and gravity, and is automatically discharged after being separated, and the gas-water separator 4 simultaneously To get rid of the residual water in the inner cavity of the humidifying intercooler 3 and the post-treatment of humidifying air to remove water.
本实用新型中,利用空气吹扫和重力作用将增湿中冷器3内部集聚的液态水排入气水分离器4,气水分离器4同时起到增湿中冷器3内部余水排除和增湿空气去水后处理的作用,无需对增湿中冷器3内部液态水量进行控制,并且可有效避免供给电堆的空气中带有液态水。以此简化系统结构并提高系统可靠性。In the utility model, the liquid water accumulated inside the humidifying intercooler 3 is discharged into the gas-water separator 4 by using air purging and gravity, and the gas-water separator 4 simultaneously functions to remove the remaining water inside the humidifying intercooler 3 And the role of dehydration post-treatment of humidified air, no need to control the amount of liquid water inside the humidified intercooler 3, and can effectively avoid liquid water in the air supplied to the stack. In this way, the system structure is simplified and the system reliability is improved.
进一步地,所述增湿中冷器3包括:壳体33、顶盖31、压力雾化喷嘴32和导流翅片34。壳体33上具有所述增湿中冷器空气入口35及所述增湿中冷器空气出口36。顶盖31覆盖在所述壳体33的顶部,并与所述壳体33固定连接。本实施例中,通过紧固件连接。压力雾化喷嘴32安装在所述顶盖31处,其具有入口及出口,所述入口即为所述增湿中冷器冷却水入口37,冷却水泵7出口直接与增湿中冷器冷却水入口37连接向压力雾化喷嘴32供应液态水。导流翅片34安装在所述壳体33的内部并位于所述压力雾化喷嘴32的下方。本实施例中,所述压力雾化喷嘴32的液态水来自于冷却回路,利用冷却水较高的温度强化增湿效果。Further, the humidifying intercooler 3 includes: a housing 33 , a top cover 31 , a pressure atomizing nozzle 32 and a guide fin 34 . The housing 33 has the humidification intercooler air inlet 35 and the humidification intercooler air outlet 36 . The top cover 31 covers the top of the housing 33 and is fixedly connected with the housing 33 . In this embodiment, they are connected by fasteners. The pressure atomizing nozzle 32 is installed at the top cover 31, and has an inlet and an outlet, the inlet is the cooling water inlet 37 of the humidifying intercooler, and the outlet of the cooling water pump 7 is directly connected to the cooling water of the humidifying intercooler. The inlet 37 is connected to supply liquid water to the pressure atomizing nozzle 32 . The guide fins 34 are installed inside the housing 33 and located below the pressure atomizing nozzle 32 . In this embodiment, the liquid water of the pressure atomizing nozzle 32 comes from the cooling circuit, and the high temperature of the cooling water is used to enhance the humidification effect.
进一步地,若冷却水泵7扬程不能满足喷嘴雾化压力要求,则冷却水泵7出口冷却水可经增压水泵8增压后流向压力雾化喷嘴32。所述压力雾化喷嘴32的入口、出口压力固定,维持固定喷雾水量,该水量最小值为空气流量最大时所对应的饱和增湿水量,计算公式为:Further, if the lift of the cooling water pump 7 cannot meet the nozzle atomization pressure requirement, the cooling water at the outlet of the cooling water pump 7 can be boosted by the booster water pump 8 and then flow to the pressure atomization nozzle 32 . The inlet and outlet pressures of the pressure atomizing nozzle 32 are fixed to maintain a fixed spray water volume. The minimum water volume is the saturated humidification water volume corresponding to the maximum air flow rate. The calculation formula is:
式中, In the formula,
为压力雾化喷嘴32最小喷雾水量,单位:g/s; is the minimum spray water volume of pressure atomizing nozzle 32, unit: g/s;
Psat,T为在电堆工作温度T下的饱和蒸气压,单位:Pa;P sat,T is the saturated vapor pressure at the working temperature T of the stack, unit: Pa;
Pair,in为空气入堆压力,单位:Pa;P air,in is the pressure of air entering the stack, unit: Pa;
为最大空气流量,单位:SLPM(标准升每分钟)。 is the maximum air flow, unit: SLPM (standard liters per minute).
进一步地,如图3所示,本实施例中,本实用新型重新设计了压力雾化喷嘴32的喷雾容腔内部结构,所述导流翅片34的数量为多个且呈交错布置,以增强水气接触效果并辅助散热,有效强化降温和增湿性能。具体实施时,所述导流翅片34用于强迫空气在所述增湿中冷器3内部作曲折流动,延长空气运动长度。所述导流翅片34用于强化内部涡流的形成,利用涡流有效保水,增强水气接触效果。所述导流翅片34用于增强增湿中冷器3对流换热效果,有辅助散热作用。Further, as shown in Figure 3, in this embodiment, the utility model redesigns the internal structure of the spray chamber of the pressure atomizing nozzle 32, and the number of the guide fins 34 is multiple and arranged in a staggered manner, so as to Enhance the water vapor contact effect and assist heat dissipation, effectively enhance the cooling and humidification performance. During specific implementation, the guide fins 34 are used to force the air to flow zigzag inside the humidifying intercooler 3 to prolong the length of the air movement. The guide fins 34 are used to strengthen the formation of the internal vortex, utilize the vortex to effectively retain water, and enhance the water-air contact effect. The deflector fins 34 are used to enhance the convective heat transfer effect of the humidifying intercooler 3 and have the effect of assisting heat dissipation.
在本说明书的描述中,参考术语“一个实施例”、“一些实施例”、“示意性实施例”、“示例”、“具体示例”、或“一些示例”等的描述意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本实用新型的至少一个实施例或示例中。在本说明书中,对上述术语的示意性表述不一定指的是相同的实施例或示例。而且,描述的具体特征、结构、材料或者特点可以在任何的一个或多个实施例或示例中以合适的方式结合。In the description of this specification, references to the terms "one embodiment," "some embodiments," "exemplary embodiments," "example," "specific examples," or "some examples" are intended to mean that the implementation Specific features, structures, materials or characteristics described in an embodiment or example are included in at least one embodiment or example of the present invention. In this specification, schematic representations of the above terms do not necessarily refer to the same embodiment or example. Furthermore, the specific features, structures, materials or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
尽管已经示出和描述了本实用新型的实施例,本领域的普通技术人员可以理解:在不脱离本实用新型的原理和宗旨的情况下可以对这些实施例进行多种变化、修改、替换和变型,本实用新型的范围由权利要求及其等同物限定。Although the embodiments of the present invention have been shown and described, those skilled in the art can understand that various changes, modifications, substitutions and modifications, the scope of the present invention is defined by the claims and their equivalents.
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| CN108448136A (en) * | 2018-02-08 | 2018-08-24 | 清华大学 | A kind of air gas supply humidification ICS intercooler system for Proton Exchange Membrane Fuel Cells |
| CN109597452A (en) * | 2018-11-30 | 2019-04-09 | 安徽明天氢能科技股份有限公司 | A kind of high power fuel cell test platform gas humiture control system |
| CN110212229A (en) * | 2019-06-26 | 2019-09-06 | 奇瑞商用车(安徽)有限公司 | Vehicle-mounted fuel cell system and fuel cell car |
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| CN108448136A (en) * | 2018-02-08 | 2018-08-24 | 清华大学 | A kind of air gas supply humidification ICS intercooler system for Proton Exchange Membrane Fuel Cells |
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| CN109597452A (en) * | 2018-11-30 | 2019-04-09 | 安徽明天氢能科技股份有限公司 | A kind of high power fuel cell test platform gas humiture control system |
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| CN111082107A (en) * | 2019-12-31 | 2020-04-28 | 潍柴动力股份有限公司 | Thermal management method and related device |
| CN111082107B (en) * | 2019-12-31 | 2021-08-20 | 潍柴动力股份有限公司 | A thermal management method and related device |
| CN112290052A (en) * | 2020-11-20 | 2021-01-29 | 上海羿沣氢能科技有限公司 | Cooling and humidifying integrated system of fuel cell |
| CN112751056B (en) * | 2020-12-31 | 2021-11-26 | 安徽江淮汽车集团股份有限公司 | Fuel cell purging system and control method |
| CN112751056A (en) * | 2020-12-31 | 2021-05-04 | 安徽江淮汽车集团股份有限公司 | Fuel cell purging system and control method |
| CN114142062A (en) * | 2021-11-24 | 2022-03-04 | 中汽创智科技有限公司 | Air conditioning system and control method of fuel cell |
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Granted publication date: 20180921 Termination date: 20210208 |