Canadian Journal of Chemical Engineering, Vol.81, No.3-4, 338-350, 2003
Fluid dynamic studies in support of an industrial three-phase fluidized bed hydroprocessor
Reducing gas hold-up has been identified as a key objective to improve the performance of Syncrude's LC-Finer(SM) unit. Redesign of the liquid recycle pan in the freeboard region, aided by multiphase CFD simulation and tests in a kerosene cold model experimental system, led to reduced gas hold-ups. The addition of an anti-foam agent did not provide any improvement. Cold-flow dimensional similitude tests demonstrated the importance of gas density, distributor geometry, and interfacial phenomena. Grid redesign was undertaken to diminish swirl and provide improved radial distribution of gas. Dispersion tests indicate favourable catalyst mixing in the reactors.
Keywords:ebullated bed;fluidization;three-phase systems;gas hold-up;foam;recycle pan;computational fluid dynamics (CFD);grid fouling;dimensional similitude;mixing