A. Constant residence time
B. Variation in extent of reaction and properties of the reaction mixture with time
C. Variation in reactor volume
D. Very low conversion
A. The feed rate is measured at temperature and pressure in the reactor
B. The temperature, pressure and the density of reaction mixture remains constant throughout the
reactor
C. There is no change in number of moles in gaseous reaction
D. All A., B. and C.
A. An ordinary non-linear differential equation
B. An algebraic differential equation
C. A linear partial differential equation
D. A non-linear partial differential equation
A. More
B. Less
C. Same
D. Either A. or B., depends on other factors
A. η and θ are always equal
B. η = θ, when the fluid density changes in the reactor
C. η = θ, for an isothermic tubular reactor in which the density of the process fluid is constant
D. η = θ, for a non-isothermal reactor
A. ∞
B. 0
C. 1
D. > 1
A. Not feasible
B. Just feasible
C. Very much feasible
D. Unpredictable as ΔG is no measure of feasibility of a reaction