Derive equation of exist concentration from reactor starting from zero order equation
The reactor is assumed to CSTR
For a CSTR operated under steady state conditions
Rate of moles of A reactant in (FA)= Rate of moles of reactants out (FA)+ rate of loss of reactant due to Zero order reaction
FAO= FA+(-rA)V (1)
For a first order reaction (-rA)= K
FA =Molar flow rate of A at any time T =FAO*(1-XA)
FAO= initial molar flow rate of A
FAO= FAO*(1-XA)+ KV
FAOXA= KV (1)
but T= space time, =V/VO, VO= Volumetric flow rate of reactant =VCAO/FAO
FAO= VCAO/T ,CAO= Initial concentration of reactant A
V= Volume of reactor and XA = Conversion
Eq.1 becomes
(VCAO/T )*XA= KV
T= CAOXA/K
for a PFR
The concentration changes along the length of the reactor and hence balance will have to be written for a differential volume of element
FA= FA+dFA+ KdV
dFA= KdV
FA= FAO*(1-XA)
dFA= FAO*(-dXA)
-dFA= FAO*dXA
FAO*dXA= KdV
dV= FAO*dXA/K
Intergrating V= (FAO/K)*dXA
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