Chemical Reaction Engineering (CRE) studies chemical reaction rates and mechanisms and reactor design. It is important for many industries like chemicals, pharmaceuticals, and medicine. The document discusses mole balance equations for batch reactors, continuously stirred-tank reactors (CSTR), plug flow reactors (PFR), and packed bed reactors (PBR). It also covers reaction rates and examples.
20. Reaction Rate Consider the isomerization A ï B r A = the rate of formation of species A per unit volume -r A = the rate of a disappearance of species A per unit volume r B = the rate of formation of species B per unit volume
34. Plug Flow Reactor Mole Balance PFR: The integral form is: This is the volume necessary to reduce the entering molar flow rate (mol/s) from F A0 to the exit molar flow rate of F A .
35. Packed Bed Reactor Mole Balance PBR The integral form to find the catalyst weight is:
79. Plug Flow Reactor Mole Balance PFR: The integral form is: This is the volume necessary to reduce the entering molar flow rate (mol/s) from F A0 to the exit molar flow rate of F A .
98. Chemical Reaction Engineering Asynchronous Video Series Chapter 1: General Mole Balance Equation Applied to Batch Reactors, CSTRs, PFRs, and PBRs H. Scott Fogler, Ph.D.
107. Compartments for perfusion Perfusion interactions between compartments are shown by arrows. V G , V L , V C , and V M are -tissue water volumes for the gastrointestinal, liver, central and muscle compartments, respectively. V S is the stomach contents volume. Stomach V G = 2.4 l Gastrointestinal V G = 2.4 l t G = 2.67 min Liver Alcohol V L = 2.4 l t L = 2.4 min Central V C = 15.3 l t C = 0.9 min Muscle & Fat V M = 22.0 l t M = 27 min
110. Reaction Rate Consider the isomerization A ï B r A = the rate of formation of species A per unit volume
111. Reaction Rate Consider the isomerization A ï B r A = the rate of formation of species A per unit volume -r A = the rate of a disappearance of species A per unit volume