This set of Chemical Reaction Engineering Multiple Choice Questions & Answers (MCQs) focuses on “Conversion and Reactor Sizing – Problems on Ideal Reactors”.
1. If the rate of a reaction is given as (-rA) = \(\frac{k_1+C_A^2}{k_2×C_A} \frac{mol}{m^3 min} \), then the units of k1 and k2 respectively are ____
a) \(\frac{mol^2}{m^6} \) and min
b) min and \(\frac{mol^2}{m^6} \)
c) mol and min
d) m3 and mol
View Answer
Explanation: Two quantities of the same dimensions can only be added. As the unit of concentration is \(\frac{mol^2}{m^3} \) , k1 has the units \(\frac{mol^2}{m^6} \).
Equating the units of all known quantities on both sides, \(\frac{mol}{m^3 min} = \frac{mol^2}{m^6} × \frac{1}{k_2×(\frac{mol}{m^3})}. \) Hence, k2 has the unit of min.
2. State true or false.
For pure gaseous reactants, the best reactor suited for carrying out reaction is CSTR.
a) True
b) False
View Answer
Explanation: For pure gaseous reactants, \(\frac{C_p}{-∆H_r} \) is small, where Cp is the specific heat capacity of the gas and ∆Hr is the enthalpy change of reaction. CSTR gives a high conversion for small values of \(\frac{C_p}{-∆H_r}. \)
3. State true or false.
For a first order reaction, the conversion of the reaction is a function of CA0.
a) True
b) False
View Answer
Explanation: For a first order reaction, –\(\frac{dC_A}{dt} \) = kCA0
CA = CA0(1 – XA)
Differentiating on either sides, dCA = -CA0dXA
-CA0 \(\frac{dXA}{dt} \) = kCA0(1 – XA)
\(\frac{dXA}{(1 – XA)} \) = kdt
-ln(1-XA) = kt
Hence, conversion is not a function of CA0.
4. For a first order reaction, if the rate constant is 1 min-1 and the reaction time is 2 min, then the ratio of final to initial concentration is ____
a) 0.167
b) 0.135
c) 0.198
d) 0.764
View Answer
Explanation: –\(\frac{dC_A}{dt}\) = kCA
Integrating between initial and final concentrations,
CA = CA0e-kt
\(\frac{C_A}{C_{A0}} \) = e-2
\(\frac{C_A}{C_{A0}} \) = 0.135.
5. The residence time (in min) for the reactants at a flow rate of 5 \(\frac{litre}{min}\) inside a reactor of volume 10 litre is ____
a) 5
b) 1
c) 10
d) 2
View Answer
Explanation: Residence time = \(\frac{volume}{volumetric \, flow \, rate} = \frac{10}{5} \) = 2.
6. A second order reaction occurs in a CSTR. Determine the ratio of volumes required for 45% conversion to 90% conversion, provided initial concentration, flow rate and other parameters are constant.
a) 1.64
b) 60.5
c) 0.35
d) 0.0165
View Answer
Explanation: For a second order reaction occurring in a CSTR,
XA1 = (1-XA1)2 V1
\(\frac{0.45}{0.90} = \frac{(1-0.45)^2 V1}{(1-0.9)^2 V2} \)
\(\frac{V_1}{V_2} \) = 0.0165.
7. The present CSTR is replaced by another CSTR of double the volume. A first order liquid phase reaction occurs in both the reactors. If the conversion achieved in the old reactor is 75%, what is the conversion achieved in the new reactor?
a) 0.857
b) 0.675
c) 0.765
d) 0.99
View Answer
Explanation: \(\frac{0.75}{X_A} = \frac{0.25}{2(1-XA)} \)
XA = 0.857.
8. A liquid phase reaction occurring in a CSTR follows first order dynamics. The feed rate is 500m3/min. Initial concentration of the feed is 50mol/m3. If the reaction conversion is 50% and the reaction is carried out in a 0.5 m3 CSTR, what is the value of rate constant?
a) 40
b) 20
c) 10
d) 5
View Answer
Explanation: FA0 XA = (-rA)V
(-rA) = kCA0(1 – XA)
500 × 0.5 = k × 50 × (1-0.5) × 0.5
k = 20.
9. For a first order liquid phase reaction occurring in a CSTR, the initial concentration is 10 \(\frac{mol}{m^3} \) and the final concentration is 5 \(\frac{mol}{m^3} \). If the residence time is 100 minutes, then the value of reaction rate is ____
a) 0.75
b) 0.33
c) 0.4
d) 0.05
View Answer
Explanation: For a CSTR, the performance equation is FA0XA = (-rA)V
t = \(\frac{C_{A0}- CA}{(-rA)} \)
rA = \(\frac{10-5}{100} \) = 0.05.
10. A reaction of first order takes 10 minutes to achieve 50% conversion. The conversion achieved after 20 minutes is ____
a) 0.5
b) 0.75
c) 0.87
d) 0.9
View Answer
Explanation: -ln(1-XA) = kt
XA = 0.75.
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