Minimizing Specific Energy Consumption of Electrochemical Hydrogen Compressor at Various Operating Conditions Using Pseudo-2D Model Simulation

被引:4
|
作者
Kim, Changhyun [1 ]
Gong, Myungkeun [1 ]
Lee, Jaewon [1 ]
Na, Youngseung [1 ]
机构
[1] Univ Seoul, Dept Mech & Informat Engn, Seoul 02504, South Korea
关键词
pseudo-two-dimensional model; electroosmotic drag; hydrogen crossover; specific energy consumption; NAFION(R) MEMBRANES; CELL; PERFORMANCE; PUMP;
D O I
10.3390/membranes12121214
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
With the increased usage of hydrocarbon-based fossil fuels, air pollution and global warming have accelerated. To solve this problem, renewable energy, such as hydrogen technology, has gained global attention. Hydrogen has a low volumetric density and thus requires compression technologies at high pressures to reduce storage and transportation costs. Techniques for compressing hydrogen include using mechanical and electrochemical hydrogen compressors. Mechanical compressors require higher specific energy consumption than electrochemical hydrogen compressors. Here, we used an electrochemical hydrogen compressor as a pseudo-two-dimensional model focused on electroosmotic drag, water back-diffusion, and hydrogen crossover flux at various temperatures, polymer electrolyte membrane thicknesses, and relative humidity conditions. To date, there have been few studies based on various operating conditions to find the optimal conditions. This study was conducted to determine the optimal parameters under various operating conditions. A numerical analysis demonstrated that the specific energy consumption was low in a specific current density section when the temperature was decreased. At the above-mentioned current density, the specific energy consumption decreased as the temperature increased. The polymer electrolyte membrane thickness yielded similar results. However, according to the relative humidity, it was confirmed that the higher the relative humidity, the lower the specific energy consumption in all of the current density sections. Therefore, when comparing temperatures of 30 degrees C and 80 degrees C at 145 A/m(2), operating at 30 degrees C reduces the specific energy consumption by 12.12%. At 3000 A/m2 and 80 degrees C, the specific energy consumption is reduced by 11.7% compared to operating at 30 degrees C. Using N117 compared to N211 at 610 A/m(2) for polymer electrolyte membranes can reduce specific energy consumption by 10.4%. Using N211 in the 1500 A/m(2) condition reduces the specific energy demand by 9.6% compared to N117.
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页数:16
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