Panel : Prof. JC, Prof. Atta, Prof. Gargi Das
JC:
Write Taylor Series?
Now, from the Taylor Series, can you derive the first principle of derivative?
What is the series expansion of exponential?
He then wrote a non-homogeneous first order ODE and asked:
What is the order of this ODE?
Is it homogeneous or non-homogeneous?
How do you solve it?
He drew a CSTR and asked to write the modelling equations for the CSTR
What is the transient part in the modelling equation?
Now some IPC, What is the function of derivative part in a PID controller?
Is it always advantageous to have a derivative action? Ans : No, if the errors are small but changing very frequently, then d(error)/dt will be large and would cause unnecessary control action.
What are some temperature measurement devices?
What is the difference between Thermistor and Thermocouple?
In which cases would you use them? what is the advantage of both?
Atta:
Major part of the viva was different kinds of Reynolds numbers and their ranges for laminar and turbulent cases.
What is Hydraulic radius?
What is the relation between hydraulic radius and hydraulic diameter? Ans: Its not D=2R, its D=4R
How do you define Re in case of convection currents over a flat plate?
What is particle Re?
In a packed bed, how do you evaluate the pressure drop?
In Unit operations for size reduction, what is the difference between crushing and milling?
What kind of forces cause the size reduction?
Do you remember any laws related to size reduction?( I said Bond's, Ritinger's and Kick's law)
Elaborate the said laws, in which case would you use Bond's law?
Gargi Das:
Do you know what is fugacity?
Why is fugacity required? How is it different from the physical pressure read by a barometer?
What is an ideal solution?
How about non-ideal? What causes non-ideality?
Draw a composition vs pressure diagram for a ideal binary liquid mixture.
How about introducing some deviation there?
What are azeotropes?
Will any non-ideal mixture make an azeotrope?
What is LMTD correction factor?
What do you correct using an LMTD correction factor?
Let's say the correction factor is 0.6, what would you change in your design of Heat Exchanger?
Draw a Sieve Tray Layout.
Do you have holes on the whole plate?
Where are the weir and down-comer?
Won't the liquid just flow through the holes?
What stops the liquid from doing that?
Finally, what are some important dimensionless numbers related to convection?
Since I mentioned Graetz and Grasshoff Number for free convection calculations, she asked about their significance.