As the main form of energy storage for new energy automobile, the performance of lithium-ion battery directly restricts the power, economy, and safety of new energy automobile. The heat-related problem of the battery is a key factor in determining its performance, safety, longevity, and cost. In this paper, parallel liquid cooling battery thermal management system with different flow path is designed through changing the position of the coolant inlet and outlet, and the influence of flow path on heat dissipation performance of battery thermal management system is studied. The results and analysis show that when the inlet and the outlet are located in the middle of the first collecting main and the second collecting main, respectively; system can achieve best heat dissipation performance, the highest temperature decrease by 0.49 C, while the maximum temperature difference of system decreases by 0.52 C compared with typical Z-type BTMS under the discharge rate of 1 C. Then an optimization strategy is put forward to improve cooling efficiency compared with single-inlet and single-outlet symmetrical liquid cooling BTMS; the highest temperature of three-inlet and three-outlet is 27.98 C while the maximum temperature difference of three-inlet and three-outlet is 2.69 C, decrease by 0.7 and 0.67 C, respectively.
K E Y W O R D Sflow path, heat dissipation performance, optimization strategy, parallel liquid cooling plate, thermal management system
Summary
The proton conducting membrane is the core component of the fuel cell. It needs water to maintain conductivity. Excessive water content inside the fuel cell will block the membrane surface and reduce the output power of the fuel cell. On the other hand, if the water content is too low, the internal resistance of the fuel cell will increase, which will reduce the performance and service life of the fuel cell. Considering the above problems, it is necessary to humidify the air and hydrogen gas before entering the fuel cell, but humidification is to prevent the membrane at the gas inlet from becoming dry. Although proton exchange membrane fuel cell (PEMFC) generates enough water, most of the gas is not completely saturated. This paper designs a self‐humidifying channel to redistribute the distribution of humid gas between different channels, and used FLUENT to simulate the heat and mass transfer, electrical conduction in the fuel cell. The effect of the self‐humidifying flow channel location on the PEMFC water and heat distribution is analyzed and evaluated.
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