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A fuel cell channel with variable cross-section

A fuel cell and variable cross-section technology, which is applied to fuel cells, circuits, electrical components, etc., can solve the problems of high airflow velocity, large pumping loss, and low airflow velocity, and achieves simple structure, increased pumping loss, and enhanced transmission. Effect

Active Publication Date: 2020-11-27
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The parallel straight channels are short, the air velocity is low, and there is no pressure difference between adjacent channels, which is not conducive to the removal of liquid water and the transmission of reaction gas in the porous electrode. The advantage is that the pressure difference between the inlet and outlet of the channel is small, and the pump gas The loss is small; the serpentine flow channel is longer and the air velocity is high, which is beneficial to the removal of liquid water in the porous electrode under the flow channel. At the same time, there is a pressure difference between adjacent flow channels, which can also eliminate the liquid water in the electrode below the bank of the flow field plate. , these characteristics are conducive to the transmission of the reaction gas in the electrode, but the disadvantage is that the pressure difference between the inlet and the outlet of the flow channel is large, the pumping loss is large, and the long flow channel will also make the distribution of the reaction gas along the length of the flow channel uneven.

Method used

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  • A fuel cell channel with variable cross-section
  • A fuel cell channel with variable cross-section
  • A fuel cell channel with variable cross-section

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] Embodiment 1: 5 rectangular blocks are equidistantly arranged in the same traditional parallel direct current channel as the comparative example, the block height is 0.8mm, the longitudinal width of the block is 0.8mm, the transverse width of the block is 1mm, and the ratio of the height of the block to the height of the flow channel The ratio of the longitudinal width of the block to the width of the channel is 0.8:1, the ratio of the lateral width of the block to the width of the channel is 1:1, and the surface contact angle of the block is 100°. The blocking block is arranged at the same position of the adjacent flow channel, such as Figure 4 shown. The battery test conditions were the same as those of the comparative example.

[0047] When the improved variable cross-section flow channel is used, under the same conditions, the distribution uniformity of the reactant gas in the electrode is significantly improved, and the concentration of the reactant gas is signif...

Embodiment 2

[0048] Embodiment 2: 5 rectangular blocks are set in the flow channel, and the height of the block increases sequentially from the inlet to the outlet of the flow channel, such as Figure 9 As shown, they are 0.1mm, 0.3mm, 0.5mm, 0.7mm and 0.9mm respectively. Blocks are equally spaced and arranged in the same position at intervals of a flow channel, such as Figure 5 shown. Under the same test conditions as the comparative example, when the tested output voltage is 0.52V, the net power of the battery in the second embodiment can be increased by 25% compared with the comparative example.

Embodiment 3

[0049] Embodiment 3: 5 trapezoidal blocks are set in the flow channel, the inclination angles on the left and right sides of the trapezoidal block are both 45°, the blocks are equally spaced, and the adjacent flow channels are misplaced, as shown in Image 6 shown. Under the same test conditions as the comparative example, when the tested output voltage is 0.52V, the net power of the battery in the third embodiment can be increased by 31% compared with the comparative example.

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Abstract

The invention relates to a variable cross-section fuel cell runner. The variable cross-section fuel cell runner comprises a cell runner arranged on a flow field plate, the cell runner comprises a runner inlet, a runner outlet, and stop blocks in the runner, and the structure of the cell runner is arranged in a way that different amount of differently distributed stop blocks with different cross sections at different heights and widths are arranged in the parallel direct runners in the direction of the cell runner. The structure of the cell runner is simple, the cell runner is easy to process,and the cost is relatively low. The local airflow velocity of the runner is strengthened under the condition that the pressure difference of the runner inlet and the runner outlet is not greatly increased, the pressure difference between the adjacent runners is established, the water removal capability of the parallel direct runner is reinforced, the transmission of a reaction gas to an electrodeis promoted, so that the transmission efficiency and the distribution uniformity of the reaction gas are improved, and the working performance of a fuel cell is improved. Compared with the traditionalparallel runner, the increase of the pressure drop of the runner provided with the stop block is not large, and the increase of pumping loss is not high, and is far less than the pumping loss of a snakelike runner. The advantages of the variable cross-section fuel cell runner are particularly remarkable on the electrode with a larger area at the higher working current density.

Description

technical field [0001] The invention relates to a variable-section fuel cell flow channel, in particular to a flow channel used for water removal and reaction gas transmission of the porous electrode of the fuel cell. Background technique [0002] The liquid water produced by the reaction in the porous electrode of the fuel cell needs to be removed in time to realize the effective transmission of the reactant gas and the efficient operation of the fuel cell. The flow channel of the fuel cell is an important transmission channel for reactant gases and reaction products, which directly affects the mass transfer efficiency of the entire fuel cell and the performance of the cell. [0003] Traditional fuel cell flow channels are all of equal cross-section, and the common forms are parallel straight channels (such as figure 1 shown) and serpentine runners (such as figure 2 shown). The parallel straight channels are short, the air velocity is low, and there is no pressure diffe...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): H01M8/0265
CPCH01M8/0265Y02E60/50
Inventor 秦彦周胡瑞王雪峰尹燕张俊锋
Owner TIANJIN UNIV