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For, A→ R, liquid phase reaction carried out in a 1000 liter MFR with CAo=10 mol/lit, v=10 lit/min, -rA = 0.09 mol .lit¹.min¹ ,what is the exit concentration of A (mol/liter)?




A)1



B)3



C)5



D)7

For 2A→R , with pure gas A as feed to a PFR ,what is εA=?


A)-0.5


B)0.5


C)2


D)-2

For a liquid phase reaction ,2A+B→R. Take CRo=0 and CAo=CBo., if the conversation of A is 80% then what is the conversion of B?_____________________




A)80%



B)40%



C)60%



D)50%

14)An aqueous feed containing reactant A with concentration of 5 mol/lit is taken in a batch reactor. The reaction is first order with rate constant of 0.5 min¹. What is the concentration (in mol/lit) at end of 5 min? A) 4.1


B) 0.41


C) 0.082


D)3

13)An aqueous feed containing reactant A with concentration of 1 mol/lit is taken in a batch reactor. The reaction is first order


rate constant of 0.5min^{1}


What is the time (in min)


required for 90% conversion?



A) 2.3


B) 4.6


C)2.0


D)4.0

12)What is the best arrangement of reactors: PFR, small MFR and large MFR, for reaction orders n>1?_____________

Consider an elementary aqueous reversible reaction system, A↔︎B. The equilibrium constant at 62°C is 11.5. What is the equilibrium conversions at temperature 62°C ?______________

10)In case of endothermic reversible reactions, equilibrium conversion_____________(decreases ,increases) as the temperature increased?

The thermodynamic (reaction) equilibrium constant is function of ______________ (temperature only/pressure only/both temperature and pressure)?

Refrigerant-134a is to be cooled by water in a condenser. The refrigerant enters the condenser with a mass flow rate of 6 kg/min at 1 MPa and 70ºC and leaves at 35°C. The cooling water enters at 300 kPa and 15°C and leaves at 25ºC. Neglecting any pressure drops, determine (a) the mass flow rate of the cooling water required and (b) the heat transfer rate from the refrigerant to water


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