A second order liquid phase reaction, A → B, is carried out in a mixed
flow reactor operated in semi batch mode (no exit stream). The reactant A
at concentration CAF is fed to the reactor at a volumetric flow rate of F. The
volume of the reacting mixture is V and the density of the liquid mixture is
constant. The mass balance for A is
(A) d(VCA
)/dt = -F (CAF
- CA
) - kCA
2V
(B) d(VCA
)/dt = F (CAF
- CA
) - kCA
2V
(C) d(VCA
)/dt = -FCA
- kCA
2V
(D) d(VCA
)/dt = FCAF
- kCA
2V
flow reactor operated in semi batch mode (no exit stream). The reactant A
at concentration CAF is fed to the reactor at a volumetric flow rate of F. The
volume of the reacting mixture is V and the density of the liquid mixture is
constant. The mass balance for A is
(A) d(VCA
)/dt = -F (CAF
- CA
) - kCA
2V
(B) d(VCA
)/dt = F (CAF
- CA
) - kCA
2V
(C) d(VCA
)/dt = -FCA
- kCA
2V
(D) d(VCA
)/dt = FCAF
- kCA
2V