Liquid-liquid extraction is a typical separation process that is widely used in various chemical processes. However, the effect of two-liquid feeding mode on the liquid–liquid Murphree efficiency (E) of rotating packed bed (RPB) remains unclear, limiting its applications. In this work, liquid–liquid distributor with different impinging angles (2θ) of two feeding liquid jets in the RPB was designed to evaluate the E, taking water as the extractant to extract benzoic acid from kerosene into the aqueous phase. The effects of operating conditions such as the 2θ, high gravity level (β), and liquid initial velocity (u0) on the E and overall volumetric mass transfer coefficient (KLa) of the RPB were studied. Experimental results revealed that both E and KLa increased with the increase of 2θ, β, and u0. In particular, when 2θ = 90°, E and KLa exhibit optimal values. At β = 49.25, u0 = 1.75 m/s, and 2θ = 90°, since the average diameter of the daughter droplets was smaller and the effective mass transfer area was larger, E reached a maximum of 64.7 % and KLa was 0.489 s−1. A correlation for predicting KLa has been established, with deviations falling within ± 20 %. This work provides theoretical basis for guiding the enhancement of mass transfer in liquid–liquid systems.
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