“…In this work, for the first time, the LBM is adopted to simulate the electrochemical processes (both reaction and transport) in a CL under PEMFC cathode conditions. The evolution equation for the concentration distribution function is as follows g i ðx þ c i Dt; t þ DtÞ À g i ðx; tÞ ¼ À 1 t g ðg i ðx; tÞ À g eq i ðx; tÞÞ þ a i S O 2 Dt (12) where g i is the distribution function with velocity c i at the lattice site x and time t. It is worth mentioning that for simple geometries, a D3Q7 (3 dimensional 7 lattice directions) lattice model (or D2Q5 model in 2D) is sufficient to accurately predict the diffusion process and properties, which can greatly reduce the computational resources, compared with D3Q19 (or D2Q9 in 2D), as proven by our previous work [29,33,34,[50][51][52][53]. For complex porous structures, especially for those with relatively low porosity such as CL, using a reduced lattice model will damage the connectivity of certain phases, thus leading to underestimated effective transport properties.…”