Reaction Engineering (Set 4) Flashcards
Concepts necessary for reactor design, operation, and maintenance.
The minimum energy required to allow a chemical reaction to proceed is termed as the ‘threshold energy ‘. Chemical reaction with low activation energy are
insensitive to temperature changes.
If Thiele modulus is ____ , then the pore diffusion resistance in a catalyst may be considered as negligible.
< 0.5
From collison theory, the reaction rate constant is proportional to
T^rn.exp(-E/RT)
For a mixed flow reactor operating at steady state, the rate of reaction is given by
FAo/V . XA
Catalytic action in a catalytic chemical reaction follows from the ability of catalyst to change the
activation energy
In Langmuir treatment of adsorption,
whole surface of the catalyst is essentially uniform and the adsorbed molecule has no effect on the rate of adsorption per site.
Organic catalysts differ from the inorganic catalyst in the sense that the former is
proteinous in nature.
An endothermic aqueous phase first order irreversible reaction is carried out in an adiabatic plug flow reactor. The rate of reaction
is maximum at the inlet of the reactor.
Pick out the wrong statement.
A catalyst increases the potential energy barrier over which the reactants must pass to form products.
For an ideal plug flow reactor, the value of Peclet number is
0
An endothermic second order reaction is carried out in an adiabatic plug flow reactor. The rate of heat generation is
maximum at the inlet of the reactor.
Equilibrium of a chemical reaction as viewed by kinetics is a ____ state.
dynamic steady
The conversion in a mixed reactor/accomplishing a reaction A –>3R is 50% when gaseous reactant ‘A’ is introduced at the rate of 1 litre/second and the leaving flow rate is 2 litres/second. The holding time for this operation is ____ second.
0.5
The size of plug flow reactor (PFR) for all positive reaction orders and for any given duty, is ____ that of mixed reactor.
smaller than
A space time of 3 hours for a flow reactor means that
the time required to process one reactor volume of feed (measured at specified conditions) is 3 hours.
If the time required for half change is inversely proportional to the square of initial concentration and the velocity depends on the units in which the concentration term is expressed, then the order of reaction is
3
The experimentally determined overall order of the reaction, A + B –> C + D, is two. Then the
reaction is elementary with a molecularity of 2.
In a continuous flow stirred tank reactor, the composition of the exit stream
is same as that in the reactor.
Recycling back of outlet stream to the reactor from an ideal CSTR carrying out a first order liquid phase reaction will result in ____ in conversion.
no change
The energy balance equation over a tubular reactor under transient conditions is
a linear partial differential equation.
Which of the following factors control the deactivation of a porous catalyst pellet ?
All (a), (b) and (c).
For the reaction, A + B –>2B + C,
rA = -rB
Transition state theory gives the rate constant as
K α T . e^-E/RT
A liquid phase reaction is to be carried out under isothermal conditions. The reaction rate as a function of conversion has been determined experimentally and is shown in the figure given below. What choice of reactor or combination of reactors will require the minimum overall reactor volume, if a conversion of 0.9 is desired ?
PFR followed by a CSTR