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Bubble column slurry reactors are widely used in industry. Often in practice, high catalyst loadings are used, and the liquid phase is usually an organic liquid. Literature correlations are not reliable enough for commercial scale up. In this paper, we develop a scale-up procedure that relies on the use of computational fluid dynamics (CFD), with Eulerian descriptions of the gas and slurry phases...
For successful scale-up of the bubble column slurry reactor for Fischer–Tropsch synthesis, we need to have proper description of hydrodynamics and transport phenomena (gas and liquid holdups, liquid-phase residence time distribution, gas–liquid mass transfer, heat transfer to cooling tubes) as a function of reactor scale (column diameter and height) and operating conditions (superficial gas velocity,...
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