Chemical Reactions Engineering Part 3 Flashcards
For the same residence time, which one will give the maximum conversion ?
Single stirred tank (v = 5 litres).
Two stirred tank (each of 2.5 litres) in series.
Stirred tank followed by tubular flow reactor (each of 2.5 litres).
Single tubular flow reactor (v = 5 litres).
Single tubular flow reactor (v = 5 litres).
__________ gas is normally employed in B.E.T.method of finding out the surface area of catalyst.
N2
H2
CO2
He
N2
The exit age distribution curve E(t) for an ideal CSTR with the average residence time, T, is given by
e^-t/T
[(e^-t/T)/T]
1 - e^-t/T
1-[(e^-t/T)/T]
[(e^-t/T)/T]
etTT
The rate constant of a reaction depends on the
initial concentration of reactants.
time of reaction.
temperature of the system.
extent of reaction.
temperature of the system.
For the reversible reaction A <–>2B, if the equilibrium constant K is 0.05 mole/litre; starting from initially 2 moles of A and zero moles of B, how many moles will be formed at equilibrium ?
0.253
0.338
0.152
0.637
0.338
For identical flow rate and feed composition, X plug flow reactors (PER) in series with a total volume V gives the same conversion as single
CSTR of volume V
PFR of volume V
CSTR of volume V/X
PFR of volume V/X
PFR of volume V
Time required for 50% decomposition of a liquid in an isothermal batch reactor following first order kinetics is 2 minutes. The time required for 75% decomposition will be about __________ minutes.
3
4
6
8
4
For a __________ order reaction, the units of rate constant and rate of reaction are the same.
zero
first
second
fractional
zero
In case of staged packed bed reactors carrying out exothermic reaction, use
high recycle for pure gas.
plug flow for dilute liquid requiring no large preheating of feed.
cold shot operations for a dilute solution requiring large preheating to bring the stream upto the reaction temperature.
all (a), (b) and (c).
all (a), (b) and (c).
Vegetable oils are hydrogenated in a __________ reactor.
slurry
plug flow
homogeneous catalytic
none of these
slurry
veg oil slurry
Pure A in gas phase enters a reactor 50% of this A is converted to B through the reaction, A –> 3B. Mole fraction of A in the exit stream is
1/2
1/3
1/4
1/5
1/3
gas 50% A3B 1/3 mole fraction
The rate of reaction does not decrease appreciably as the reaction proceeds in case of __________ reactions.
autocatalytic
exothermic
endothermic
autothermal
autocatalytic
For all positive reaction orders for a particular duty,
mixed reactor is always larger than the plug-flow reactor.
ratio of the volume of the mixed reactor to that of the plug-flow reactor decreases with order.
reactor size is independent of the type of flow.
density variation during reaction affects design.
mixed reactor is always larger than the plug-flow reactor.
The heat of reaction
depends on the pressure only.
depends on the mechanism of reaction only.
depends on both pressure and mechanism of reaction.
is independent of the mechanism of reaction.
is independent of the mechanism of reaction.
Which of the following does not produce a change in the value of rate constant of a reaction ?
Pressure
Temperature
Concentration and catalyst
None of these.
Concentration and catalyst
With increase in temperature, the equilibrium conversion of a reversible exothermic reaction
decreases
increases
remains unaffected
decreases linearily with temperature
decreases
In a CSTR __________ varies with time.
reaction rate
concentration
both (a) & (b)
neither (a) nor (b)
neither (a) nor (b)
The following gas phase reactions are carried out isothermally in a CSTR.
A –> 2R ; r1 = k1pA ;
k1 = 20mole/(sec.m3 bar)
A –> 3S ; r2 = k2 pA ;
k2 = 40mole/(sec.m3 .bar)
What is the maximum possible value of FR(mole/sec.) ?
1/3
1/2
2/3
2
2/3
As the chemical reaction proceeds, the rate of reaction
increases.
decreases.
remains same.
may increase or decrease depending on the type of reaction.
decreases.
Pick out the wrong statement.
A catalyst does not alter the final position of equilibrium in a reversible reaction.
A catalyst initiates a reaction.
A catalyst is specific in reaction.
A catalyst remains unchanged in chemical composition at the end the reaction.
A catalyst initiates a reaction.
In a first order reaction, the time required to reduce the concentration of reactant from 1 mole/litre to 0.5 mole/litre will be __________ that required to reduce it from 10 moles/litre to 5 moles/litre in the same volume.
more than
less than
same as
data insufficient; can’t be predicted.
same as
1 0.5 10 5 same as
Photo-chemical reactions occur in presence of
sunlight.
darkness.
solid catalysts.
monochromatic radiation only.
sunlight.
n’ number of plug flow reactors (P.F.R) in series with a total volume ‘V’ gives the same conversion as one P.F.R. of volume
V/n
V
V.n
1/V
V
Knudsen diffusion is directly proportional to
T
sqrt(T)
1/sqrt(T)
T^2
sqrt(T)
Fractional conversion __________ for an exothermic reversible chemical reaction, when the temperature is maximum.
increases
remains unchanged
decreases
unpredictable from the data
decreases
Non-catalytic fluid-solid reactions are represented by __________ model.
continuous reaction
unreacted core
both (a) and (b)
neither (a) and (b)
both (a) and (b)
A pulse tracer is introduced in an ideal CSTR (with a mean residence time ?) at time, t = 0. The time taken for the exit concentration of the tracer to reach half of its initial value will be
2T
0.5T
T/0.693
0.693T
2T
pulse tracer 2T
On application of pressure to the equilibrium system, ice <–> water ; which of the following phenomenon will occur ?
Water will evaporate
Equilibrium will not be attained
More ice will be formed
More water will be formed.
More water will be formed.
pressure ice water more water
Participation of __________ is involved in the occurrence of a chemical reaction.
protons
neutrons
electrons
none of these
electrons
Promoter.
initiates a chemical reaction and is a catalyst by itself.
atlers the position of equilibrium in a reversible reaction.
increases the number of active centres by increasing the unevenness of catalyst surface and by creating discontinuities in the crystals.
all (a), (b) and (c).
increases the number of active centres by increasing the unevenness of catalyst surface and by creating discontinuities in the crystals.
The rate constant of a reaction is a function of the
time of reaction.
temperature of the system.
extent of reaction.
initial concentration of the reactants.
temperature of the system.
Mean residence time is equal to the space time, when
the feed rate is measured at temperature and pressure in the reactor.
the temperature, pressure and the density of reaction mixture remains constant throughout the reactor.
there is no change in number of moles in gaseous reaction.
all (a), (b) and (c).
all (a), (b) and (c).
If ‘n’ is the order of reaction, then unit of rate constant is
1/(time)(concentration)^n - 1
(time)^-1 (concentration)^n - 1
(time)^n - 1 (concentration)
none of these
1/(time)(concentration)^n - 1
Batch process is preferred over continuous process, when the
product yields and quality can not be achieved in continuous process, because of long residence time.
sales demand of product is not steady.
same equipment can not be used for several processes of the same nature.
all (a), (b) & (c)
all (a), (b) & (c)
The value of ‘n’ for a chemical reaction A –> B, whose reaction rate is –>CAn, will be __________ if the rate of the reaction increases by a factor of 8, when the concentration of is doubled.
0
1
2
3
3
With the same reaction time, initial concentration and feed rate, the reaction 2A –>B is carried out separately in CSTR and P.F. reactor of equal volumes. The conversion will be
higher in P.F. reactor
higher in CSTR
same in both the reactors
data insufficient; can’t be predicted
higher in P.F. reactor
For any reaction, we may write conversion as a function of
time
temperature
concentration
all (a), (b) & (c)
all (a), (b) & (c)
The use of space time is preferred over the mean residence time in the design of a/an
batch reactor
ideal tubular-flow reactor
slurry reactor
CSTR
ideal tubular-flow reactor
space time preferred - ideal tubular-flow
Autocatalytic reactions are best carried out in a
CSTR
CSTR in series
plug flow reactor
recycle reactor
recycle reactor
The gas phase reaction 2A <–> B is carried out in an isothermal plug flow reactor. The feed consists of 80 mole % A and 20 mole % inerts. If the conversion of A at the reactor exit is 50%, then CA/CA0 at the outlet of the reactor is
2/3
5/8
1/3
3/8
5/8
2AB 80% 20% 50% 5/8
A batch reactor suffers from following disadvantage.
Poor product quality control.
High labour and handling cost.
High shutdown time requirement for emptying, cleaning and refilling.
All (a), (b)and(c).
All (a), (b)and(c).
A first order reaction is to be treated in a series of two mixed reactors. The total volume of the two reactors is minimum, when the reactors are
equal in size.
of different sizes.
of such size that the ratio of their volumes is < 5.
none of these.
equal in size.
Half life period of a chemical reaction is proportional to CA0-1 , if the reaction is of __________ order.
first
zero
second
third
second
The irreversible reaction, X –> Y, is the special case of the reversible reaction, X <–>Y, in which the
equilibrium constant is infinite.
fractional conversion of ‘A’ at equilibrium is unity.
concentration of ‘A’ at equilibrium is zero.
all (a), (b) and (c).
all (a), (b) and (c).
The equilibrium constant K of a chemical reaction depends on
temperature only.
pressure only.
temperature and pressure.
ratio of reactants.
temperature only.
The reaction rate almost gets doubled for 10 C rise in temperature. This is due to the fact that the
increased temperature reduces the activation energy.
fraction of molecules having threshold energy increases.
collision frequency increases.
value of threshold energy decreases.
fraction of molecules having threshold energy increases.
Which of the following is not a unit of reaction rate ?
Moles for med/(surface of catalyst) (time)
Moles formed/volume of reactor) (time)
Mole formed/volume of catalyst) (time)
None of these
None of these
Brunaur, Emmet and Teller (BET) equation is used to determine the specific surface area of a porous particle but not the pore volume & the porosity of the catalyst bed. Which of the following postulates is not used to derive BET equation ?
Langmuir’s assumption applies to every adsorbed layer.
There is no dynamic equilibrium between successive layer.
The adsorbed layer may be polymolecular in thickness and the heat of adsorption in each layer (except the first one) is involved in each of the evaporation process.
none of these.
There is no dynamic equilibrium between successive layer.
not BET no dynamic
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
15, 10, 5
5, 10, 15
10, 5, 15
10, 15, 5.
15, 10, 5
5, 10 and 15 = 15, 10, 5
The following half life data are available for the irreversible liquid phase reaction A products.
Initial Concentrations (K.mol/m^3): 2 and 8 and Half-lifes: 2 and 1, respectively. The overall order of reaction is
0.5
1
1.5
2
1.5
A non-catalytic chemical reaction of the type A –+Z,K1–> B –+Z,K2–> C –+Z,K–> D is called a __________ reaction.
parallel
series
series-parallel
none of these
series-parallel
The unit of frequency factor in Arhenious equation is
same as that of rate constant.
same as that of activation energy.
dimensionless.
none of these.
same as that of rate constant.
With increase in the order of reaction (for all positive reaction orders), the ratio of the volume of mixed reactor to the volume of plug flow reactor (for identical feed composition, flow rate and conversion)
increases
decreases
remains same
increases linearly
increases
Reaction of benzene with chlorine gas to produce tri-chlorobenzene exemplifies a/an __________ reaction.
elementary
parallel
consecutive
none of these
consecutive
For the gaseous reaction 2A –> B, where the feed consists of 50 mole % A and 50 mole % inerts, the expansion factor is
1
-0.5
-0.25
0
-0.25
The molecularity and the order of reaction respectively, for the hydrolysis of methyl acetate in presence of acids are
2 & 1
11 & 2
2 && 2
1 & 1
2 & 1