阅读说明：本技术 高效能的质子交换膜燃料电池多孔输运层 (High-efficiency porous transport layer of proton exchange membrane fuel cell ) 是由 杜青 侯昱泽 李兴 焦魁 于 2020-04-23 设计创作，主要内容包括：本发明提出了一种高效能的质子交换膜燃料电池多孔输运层,其技术方案是,燃料电池阴极的气体扩散层与无裂痕微孔层叠加在一起制成多孔输运层。选择孔隙率为60～65％的碳纸作为气体扩散层,无裂痕微孔层的孔隙率为50～55％,由直径为20～40纳米的碳颗粒制成。在多孔输运层平面的流道沟下纵横均匀间隔1毫米加工有贯穿孔。该结构可以分离液态水与反应气体：液态水通过贯穿微孔输运,反应气体通过多孔输运层的孔隙运输。可以在加快多孔输运层水的排除速度同时保持膜的导电率,同时减小气体的传输阻力。由于贯穿孔地均匀排布,缓解了多孔输运层应力不均匀导致的疲劳问题。(The invention provides a high-efficiency proton exchange membrane fuel cell porous transport layer, which adopts the technical scheme that a gas diffusion layer of a fuel cell cathode and a crack-free microporous layer are superposed together to form the porous transport layer. The carbon paper with the porosity of 60-65% is selected as a gas diffusion layer, the porosity of the crack-free microporous layer is 50-55%, and the crack-free microporous layer is made of carbon particles with the diameter of 20-40 nanometers. Through holes are processed under the runner channels of the porous transport layer at uniform intervals of 1 mm vertically and horizontally. This structure can separate liquid water and reaction gas: liquid water is transported through the through micropores, and reaction gas is transported through the pores of the porous transport layer. The water removal speed of the porous transport layer can be accelerated, the electric conductivity of the membrane can be kept, and the gas transmission resistance can be reduced. Due to the fact that the through holes are uniformly distributed, the fatigue problem caused by uneven stress of the porous transport layer is relieved.)

1. The porous transport layer of proton exchange membrane fuel cell of high performance, its characteristic is: a gas diffusion layer (1) and a crack-free microporous layer (2) of a fuel cell cathode are overlapped to form a porous transport layer, carbon paper with the porosity of 60-65% is selected as the gas diffusion layer, the crack-free microporous layer is 50-55% in porosity and is made of carbon particles with the diameter of 20-40 nanometers.

2. The high performance pem fuel cell porous transport layer of claim 1, wherein: and processing through holes with the diameter of 10-12 microns at uniform intervals of 1 mm vertically and horizontally under the runner channel (3) of the porous transport layer plane.

Technical Field

The invention belongs to the field of electrochemical fuel cells, and particularly relates to a high-efficiency porous transport layer of a proton exchange membrane fuel cell.

Background

Fuel cells are considered to be an ideal driving device for next-generation power machines as a clean, efficient and energy conversion device with high power density. The cell takes hydrogen as fuel and the resultant is water, so that the problem of air pollution can be relieved to a great extent. And hydrogen energy can be obtained by conversion in various ways, and is an ideal energy storage medium. Therefore, the popularization of the fuel cell technology is also very important for the multi-aspect development of world energy sources and the storage.

The proton exchange membrane in the fuel cell must keep a certain water content to keep its high performance, and most of the common water distribution studies inside the fuel cell divide the fuel cell into a membrane electrode and a flow channel, wherein the membrane electrode includes: a gas diffusion layer, a microporous layer, a catalytic layer, and a proton exchange membrane. Proton exchange membrane fuel cell water is generated only at the cathode, and under high current density, flooding is likely to occur, thus reducing fuel cell performance. Therefore, the optimal design of the internal structure of the fuel cell is a key factor for improving the performance and the service life of the fuel cell.

In 2002, the first generation fuel cell stacks were marketed with a volumetric power density of 1kw L^-1Through the material structure optimization of the convection field plate, the volume power density of the second generation of the electric pile reaches 1.5kw L^-1Next, by optimizing the electrode thickness, the third generation of the stack in 2014 reached a volumetric power density of 3kw L^-1. With the increasing volume power density of the stack, the requirements for gas diffusion layers, microporous layers and the like of fuel cells are also increasing, and more efficient heat and mass transfer technology and more intelligent (inside of the cell) water management are required. Therefore, optimizing the membrane electrode of the fuel cell is very important to further increase the volumetric power density of the stack.

Disclosure of Invention

The invention aims to provide a high-efficiency porous transport layer device of a proton exchange membrane fuel cell, so that the efficiency of gas transport and liquid water transport in the fuel cell is effectively enhanced.

The technical scheme of the porous transport layer device of the high-efficiency proton exchange membrane fuel cell is that a gas diffusion layer of a cathode of the fuel cell and a crack-free microporous layer are superposed together to form the porous transport layer. The carbon paper with the porosity of 60-65% is selected as a gas diffusion layer, the porosity of the crack-free microporous layer is 50-55%, and the crack-free microporous layer is made of carbon particles with the diameter of 20-40 nanometers.

The proton exchange membrane fuel cell has the structure that a proton exchange membrane is arranged between a cathode plate and an anode plate, namely, a cathode and an anode are separated by the proton exchange membrane, and the cathode plate and the anode plate are respectively provided with a cathode runner and an anode runner. A catalyst layer, a microporous layer and a gas diffusion layer are correspondingly arranged between the proton exchange membrane and the cathode plate and the anode plate. Since water is generated only at the cathode of the proton exchange membrane fuel cell, the invention adds the gas diffusion layer and the non-crack microporous layer of the cathode of the fuel cell together to form a porous transport layer, and carries out specific microstructure optimization to facilitate the water transmission.

And drilling through holes on the porous transport layer at intervals of 1 mm to prepare porous layers with uniformly distributed through holes, so that the porous transport layer is convenient to drain. In the porous transport layer previously equipped with a fracture microporous layer, part of liquid water is left in the electrode, and part of liquid water flows into the diffusion layer through the fracture to occupy part of the gas transmission path, which is the scheme adopted by most of the fuel cells at present, but because the generation of the fracture cannot be artificially controlled, the distribution of the liquid water in the electrode and in the microporous layer is still uneven, and the unevenly distributed fracture can cause uneven stress in the whole porous transport layer, and can cause a durability problem. The porous transport layer comprises a crack-free microporous layer with the porosity of 50-55%, and the crack-free microporous layer plays a role in wetting the membrane and ensuring the proton conductivity in order to lock part of liquid water in the electrode. The redundant liquid water can be quickly discharged out of the porous conveying layer through the through holes, and the transmission of gas in the rest pores is not influenced.

The invention has the characteristics and beneficial effects that: the optimized design can accurately control the transmission path of the liquid water in the porous transport layer in the process of discharging the liquid water out of the cathode, the liquid water can be transported only along macroscopic straight holes in the porous transport layer, the path for discharging the liquid water is shortened, the liquid water is guaranteed not to be immersed into micropores in the porous transport layer, and therefore the transportation of reaction gas is not influenced, and meanwhile, the efficient transmission of the reaction gas and the liquid water is guaranteed. Compared with the conventional irregular crack structure, the regular structural design can relieve the stress fatigue in the porous transport layer and improve the durability.

Drawings

Fig. 1 is a schematic diagram of a porous transport layer structure.

Fig. 2 is a processing size diagram of a porous transport layer with through holes.

FIG. 3 is a comparison of the liquid water flow state of the porous transport layer obtained by a numerical simulation method and the original transport layer.

FIG. 4 is a graph comparing the gas transport pores of the transport layer of the present invention with the original transport layer under liquid water transport.

Detailed Description

The structure of the present invention will be further described by way of example with reference to the accompanying drawings.

The porous transport layer of the proton exchange membrane fuel cell with high performance has the structure that: a gas diffusion layer 1 and a crack-free microporous layer 2 of a fuel cell cathode are overlapped to form a porous transport layer, carbon paper with the porosity of 60-65% is selected as the gas diffusion layer, the crack-free microporous layer is 50-55% in porosity and is made of carbon particles with the diameter of 20-40 nanometers.

Through holes are processed under the runner channels 3 of the porous transport layer plane at uniform intervals of 1 mm in length and breadth, and the diameter of each through hole is 10-12 microns.

As an example, a microporous layer with a porosity of 50% and no cracks is covered on a carbon paper diffusion layer with a porosity of 60% to form a porous transport layer, and through holes with a diameter of 10 microns are punched on the porous transport layer at intervals of 1 mm under a channel groove by using a laser drilling technology to form the porous transport layer with all through holes.

To test the effect of the porous transport layer, liquid water transport was compared to the prior art structure and the experimental results were verified as shown in fig. 3. The comparison graph of the liquid water flow state of the porous transport layer and the original transport layer obtained by using a numerical simulation method shows the liquid water state under different transport time intervals (microseconds).

It can be seen that in the construction where the transfer layer is carbon-only paper (first row in the figure), a significant amount of water penetrates into the voids and occupies the gas transport path, creating additional gas transport resistance. In the structure (the second row in the figure) that the transmission layer is carbon paper and a non-crack microporous layer, liquid water is prevented from soaking into the microporous layer due to the extremely high capillary force in the non-crack microporous layer, the transmission of gas in the microporous layer is not influenced, but excessive liquid water is accumulated in the electrode to cause flooding inside the electrode, so that the catalyst cannot normally work, and the performance of the battery is influenced. In the structure where the transfer layer is carbon paper with a cracked microporous layer (third row in the figure), part of the liquid water enters the microporous layer along the crack, and the carbon paper is slightly flooded with water. In the porous transport layer (the fourth row in the figure), part of liquid water is blocked in the electrode under the action of local capillary force, so that the porous transport layer plays a role of wetting the membrane and ensuring proton conductivity, and redundant liquid water can be quickly discharged out of the porous transport layer through the through holes. Because the local capillary force at the through hole is far smaller than that of the nano-scale micropores at the other part of the micropore layer, the liquid water is only transmitted through the through hole, the transmission of gas in the rest pores is not influenced, and the gas-liquid separation transmission in the porous transport layer is realized.

Fig. 4 shows the comparison between the porous transport layer and the currently used structure in liquid water transport, and it can be seen that the novel porous transport layer can fast and orderly drain liquid water out of the porous transport layer, and due to the small local capillary force in the through holes, the liquid water can only be transported along the through holes, and the transport of the reaction gas is not affected. After the liquid water is stably transmitted, the proportion of the dry pores is distributed in the thickness direction of the porous transport layer as shown in fig. 4, and under the working condition that the liquid water can be normally discharged, the porous transport layer can retain the dry pores with the maximum proportion inside for ensuring the normal transport of the reaction gas, so that the mass transfer resistance is lowest.