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This section includes 11 Mcqs, each offering curated multiple-choice questions to sharpen your Mass Transfer knowledge and support exam preparation. Choose a topic below to get started.
1. |
In sulphuric acid plants dry air is used for burning of sulphur. Air is dried in contact with concentrated Sulphuric acid. Moisture diffuses through a layer of air, reaches the surface and gets absorbed in it. Here air is said to be non-diffusing were as moisture is diffusing. Which of the following statements are correct? |
A. | Moisture has a source and a sink whereas dry air has a source but no sink |
B. | Moisture as well as dry air have a sink |
C. | Moisture has a source but no sink whereas dry air has a source as well as sink |
D. | Moisture as well as dry sir have no sink |
Answer» B. Moisture as well as dry air have a sink | |
2. |
The value of a ratio of N flux of A to the total N flux for a steady state equimolar counter diffusion is |
A. | 0 |
B. | Infinity |
C. | 1 |
D. | None of the mentioned |
Answer» C. 1 | |
3. |
For a steady state equimolar counter diffusion of A and B. The N flux of A is ________ |
A. | – N flux of A |
B. | N flux of A |
C. | – N flux of B |
D. | N flux of B |
Answer» D. N flux of B | |
4. |
What is the value of the flux (kmol/m3.s) of water vapor through a stagnant film of estimated thickness 1.5mm on the water surface? |
A. | 1.36*10-5 |
B. | 1.96*10-5 |
C. | 1.96*10-1 |
D. | 1.96*10-7 |
Answer» C. 1.96*10-1 | |
5. |
What will be the values of the diffusivities (in cm2/s) at the mean gas-film temperature? |
A. | 0.923,0.267 |
B. | 0.483,1.351 |
C. | 0.294,0.368 |
D. | 1.381,0.364 |
Answer» B. 0.483,1.351 | |
6. |
A mixture undergoing multicomponent diffusion is analyzed through the Maxwell-Stefan approach. With regard to this approach which among the following statements are incorrect? The difference in the partial pressure of the Component A over a small distance ∆z (AB)is proportional to |
A. | The molar concentration at the two points |
B. | Length of the diffusion path |
C. | Velocity at the point A |
D. | Difference in the velocities at point A and B |
Answer» D. Difference in the velocities at point A and B | |
7. |
For a steady state equimolar counter diffusion of A and B. The N flux of A is _______? |
A. | – N flux of A |
B. | N flux of A |
C. | – N flux of B |
D. | N flux of B |
Answer» B. N flux of A | |
8. |
What is the value of the flux (kmol/m3.s) of water vapor through a stagnant film of estimated thickness 1.5mm on the water surface? |
A. | 1.36*10<sup>-5</sup> |
B. | 1.96*10<sup>-5</sup> |
C. | 1.96*10<sup>-1</sup> |
D. | 1.96*10<sup>-7</sup> |
Answer» C. 1.96*10<sup>-1</sup> | |
9. |
What will be the values of the diffusivities (in cm2/s) at the mean gas-film temperature? |
A. | 0.923,0.267 |
B. | 0.483,1.351 |
C. | 0.294,0.368 |
D. | 1.381,0.364 |
Answer» D. 1.381,0.364 | |
10. |
If all the components except 1 of the multicomponent diffusing mixture are inert, then what will be the expression for Diffusivity of component 1 in the mixture? |
A. | D<sub>1m</sub>=(N<sub>1</sub>-Y<sub>1</sub>‚àëN<sub>j</sub>)/(‚àë(Y<sub>j</sub>N<sub>1</sub>-Y<sub>1</sub>N<sub>j</sub>)/D<sub>ij</sub>) |
B. | D<sub>1m</sub>=(Y<sub>1</sub>‚àëN<sub>j</sub>)/(‚àë(Y<sub>j</sub>N<sub>1</sub>-Y<sub>1</sub>N<sub>j</sub>)/D<sub>ij</sub>) |
C. | D<sub>1m</sub>=N<sub>1</sub>/(‚àë[(Y<sub>j</sub>N<sub>1</sub>-Y<sub>1</sub>N<sub>j</sub>)/D<sub>ij</sub>]) |
D. | D<sub>1m</sub>=(1-Y<sub>1</sub>)/(‚àë[Y<sub>j</sub>/D<sub>ij</sub>]) |
Answer» E. | |
11. |
A mixture undergoing multicomponent diffusion is analyzed through the Maxwell-Stefan approach. With regard to this approach which among the following statements are incorrect? The difference in the partial pressure of the Component A over a small distance ∆z (AB)is proportional to |
A. | The molar concentration at the two points |
B. | Length of the diffusion path |
C. | Velocity at the point A |
D. | Difference in the velocities at point A and B |
Answer» D. Difference in the velocities at point A and B | |