The effectiveness factor for large value of Thiele modulus [L√(K/D1)] of a solid catalysed first order reaction is equal to (where, L = length of the reactor, cm, D1 = diffusion co-efficient, cm2/second) ?
A. L √(K/D1)
B. 1/[L√(K/D1)]
C. 1
D. ∞
A. L √(K/D1)
B. 1/[L√(K/D1)]
C. 1
D. ∞
A. Combustion of coal particles
B. Roasting of sulphide ores
C. Manufacture of carbon disulphide from elements
D. None of these
‘Unreacted core model’ represents the reaction involving ______________________? Read More »
Chemical Reaction A. 1.0 to 10-8
B. 1.1 to 102
C. 0.1 to 0.9
D. None of these
A. More uniform operating conditions
B. Permits operation at the optimum temperature for a long reaction time
C. Higher overall selectivity for a first order consecutive reaction
D. All A., B. and C.
A stirred tank reactor compared to tubular-flow reactor provides____________________? Read More »
Chemical Reaction A. Plot of – rA Vs CA is a straight line with slope k
B. Plot of – rA Vs CA is a hyperbola
C. Rate of disappearance of reactant A is maximum, where CA = CB
D. Both B & C
A. Plug flow
B. Dispersion
C. Mixed flow
D. Tank in series
Fluid flow in a real packed bed can be approximated as ________________ model? Read More »
Chemical Reaction A. dXA/dt = k1 (1 – XA)2 (1 + 2XA)
B. dXA/dt = k1 (1 – XA) (1 + 0.5XA)
C. dXA/dt = k1 (1 – XA)
D. dXA/dt = k1 (1 – XA)/(1 + XA)
A. 100
B. 150
C. 200
D. 225
A. Be more in CSTR than in PFR
B. Be more in PFR than in CSTR
C. Be same in both cases
D. Depend on the temperature
A. UAE
B. Saudi Arabia
C. Turkey
D. China