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Consider the aforementioned liquid phase reaction which takes place now in an ideal semi-batch reactor. The initial volume of liquid HMF/water solution in the reactor is V0 and the initial concentration of HMF is [HMF]0. Liquid mixture of HMF/water is fed continuously to the reactor at a volumetric flow rate Ï . The concentration of HMF in this feed is [HMF]feed.
Derive the design equation for this system (semi-batch reactor) by carrying out material balance on HMF (work in terms of concentrations) (40 points)
HMF RXN2 Humins Levulinic Acid RXN 1. HO Formic Acid
Consider the aforementioned liquid phase reaction which takes place now in an ideal semi-batch reactor. The initial volume of liquid HMF/water solution in the reactor is V0 and the initial concentration of HMF is [HMF]0. Liquid mixture of HMF/water is fed continuously to the reactor at a volumetric flow rate Ï . The concentration of HMF in this feed is [HMF]feed.
Derive the design equation for this system (semi-batch reactor) by carrying out material balance on HMF (work in terms of concentrations) (40 points)
HMF RXN2 Humins Levulinic Acid RXN 1. HO Formic Acid
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