For a tubular flow reactor with uniform concentration and temperature, the independent variable is Length Time None of these Diameter TRUE ANSWER : ? YOUR ANSWER : ?
For a packed bed reactor; the presence of a long tail in the residence time distribution curve is an indication of Bypass Ideal plug flow Chanelling Dead zone TRUE ANSWER : ? YOUR ANSWER : ?
The sequence in which three CSTR's of volumes 5, 10 and 15 m³ will be connected in series to obtain the maximum production in a second order irreversible reaction is 5, 10, 15 15, 10, 5 10, 5, 15 10, 15, 5 TRUE ANSWER : ? YOUR ANSWER : ?
Catalyst is a substance, which __________ chemical reaction. Decreases the speed of a Alters the value of equilibrium constant in a reversible Can either increase or decrease the speed of a Increases the speed of a TRUE ANSWER : ? YOUR ANSWER : ?
For a first order reaction carried out in a plug flow reactor, the space time is 1/K In C/C0 K In C/C0 1/K In C0/C K In C0/C TRUE ANSWER : ? YOUR ANSWER : ?
A backmix reactor Is same as ideal stirred tank reactor Is same as plug-flow reactor Is most suitable for gas phase reaction Employs mixing in axial direction only TRUE ANSWER : ? YOUR ANSWER : ?
In an ideal P.F.R. at steady state conditions The composition of reactants remains constant along a flow path There is no lateral mixing of fluid The conversion of the reactant varies from point to point along a flow path There may be diffusion along the flow path TRUE ANSWER : ? YOUR ANSWER : ?
According to Arhenious equation of temperature dependency of rate constant for an elementary reaction K ∝ √T None of these K ∝ T e-E/RT K ∝ e-E/RT TRUE ANSWER : ? YOUR ANSWER : ?
The fractional volume change of the system for the isothermal gas phase reaction, A 3B , between no conversion and complete conversion is 0.5 1 2 3 TRUE ANSWER : ? YOUR ANSWER : ?
Fluid flow in a real packed bed can be approximated as __________ model. Dispersion Plug flow Mixed flow Tank in series TRUE ANSWER : ? YOUR ANSWER : ?