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An enzyme acts as a catalyst in the fermentation of A to form product R. An aqueous feed stream containing the enzyme and compound A flows into a CSTR at 25 L/min, and the initial concentration of A is 2 mol*L-1 . Determine the volume of the CSTR (in Liters, expressed to the nearest integer ) needed to achieve 98% conversion of reactant A. You may assume that the enzyme concentration and volumetric flowrates are constant. The maximum rate of destruction of the substrate is 0.4 mol/(L min). When the substrate concentration is 0.5 mol/L, the rate of destruction of the substrate is 0.2 mol/(L min), i.e. half of the maximum rate.
The design equation for a CSTR is:
V / (F CAo) = XA / r
where;
V = volume of CSTR
F = volumetric flowrate = 25 L / min
CAo = initial concentration of A = 2 mol / L
r = rate of reaction
XA = conversion of reactant A = 0.98
The enzymatic reactions follow the Michaelis-Menten Kinetics which is given by:
r = vmax CA / (KM + CA)
where;
vmax = maximum rate of destruction of substrate = 0.4 mol / (L min)
KM = substrate concentration when rate of destruction of substrate is half of the maximum value = 0.5 mol/L
We know;
CA = CAo (1 - XA)
Using this in the rate expression:
r = vmax CAo (1 - XA) / (KM + CAo (1 - XA))
Substituting the values of all the variables:
r = 0.4 X 2 X (1 - 0.98) / (0.5 + 2(1 - 0.98))
which on solving gives:
r = 0.0296 mol / L.min
Substituting this in the CSTR design equation:
V / (F CAo) = XA / r
V / (25 X 2) = 0.98 / 0.0296
V / 50 = 33.11
V = 33.11 X 50
V = 1655 L
which is the volume of the CSTR.