“…Δ C can be estimated from the interface supersaturation model proposed by H. Vogt, 53,65–68
where z is the stoichiometric number and it is taken as z = 4 in this paper, f G is the gas evolution efficiency and f G = 1 − (1 − θ c ) 2.5 , θ c is the rate of bubble coverage and θ c =
, and
is the contact radius. k e is the mass transfer coefficient of dissolved oxygen in the liquid phase, whose unit is m s −1 , which is related to the micro-convection term k b caused by bubbles and the single-phase mass transfer term k s caused by the concentration difference, 49,67,69 ![]()
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where D is the diffusion coefficient of dissolved oxygen in the electrolyte, whose unit is m 2 s −1 , and D = 2.01 × 10 −9 m 2 s −1 in this paper. d b is the bubble diameter, whose unit is m. Re is the Reynolds number and Sc is the Schmidt number.…”