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A liquid‐liquid cyclone reactor was proposed for ionic liquid‐catalyzed isobutane alkylation to improve the mixing efficiency and accelerate the separation between alkylate and ionic liquid. The Eulerian‐Eulerian multiphase flow model and Reynolds stress model (RSM) were used to simulate the flow field in the reactor. A parameter, named the dispersion uniformity of dispersed phase, β, was used to...
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