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9)At present we have 90% conversion of the liquid feed (n-1. CA0-10 mol/l) to our mixed flow reactor with a recycle of product(R-2). If we shut off the recycle stream, by how much the conversion decreases for the same processing rate?
8)What is prerequisite to find the minimum reactor for any given different combinations?
7)"For a liquid phase reactions, the residence times for the ideal batch and plug flow reactors are same", State the reason for this statement.
5)Write all the factors that are influencing the rate of reaction.
4)What are the different contacting patterns?
3. For a gas reaction at 400K, the rate is expressed a dpA/dt 3.66 atm.h-. What is the unit for the rate constant?
2)What is the steady state approximation?
1)For the reaction A products, the temperature is increased from 300°C to 500°C, and then the times of reaction have been doubled What is the activation energy for the particular reaction? (se Arthenius theory)
Define selectivity and yield.?
Derive an performance equation for recycle reactor along with graphical representation.
