rA = 0.4 CA, rB = 0.3 CB - 0.4 CC
Three tanks of different sizes are available. At the desired production rate, the residence times of 5 min, 10 min and 15 min, are maintained in the successive stages of the CSTR battery. The feed concentrations are CAo = 0.9; CBo = 1.2 and CCo = 0. Find the concentration of B in the effluent from each tank.
Formula's limitation is : we can use it only for first order reaction.
units of CB1 will
be same of
CB0
The reaction A --> B --> C has the rate equations. rA = 0.4 CA, rB...
2. Derive equations quantifying concentrations of Ca and C in the effluent from a CSTR if you know that Cao is the influent substrate concertation; V is volume of the reactor, F is flow rate; k is reaction rate constant, and they are all known. The reaction in the reactor A Reaction is of first order with the rate rA-k. CA CSTR CA, CB CAO
Question 1: Design of isothermal reactors 30 Marks The irreversible, gas-phase reaction A+B D is to be carried out in an isotherma °C) plug-flow reactor (PFR) at 5.0 atm. The mole fractions of the feed streams are A 0 B 0.50, and inerts 0.30. The activation energy for the above reaction is 80 000 cal/mol. the pressure drop due to fluid friction in the reactor is so small that it can be ignored, perform the following tasks: 2T a s...