MCQOPTIONS
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This section includes 9 Mcqs, each offering curated multiple-choice questions to sharpen your Distillation Design knowledge and support exam preparation. Choose a topic below to get started.
| 1. |
If the feed is saturated liquid, then |
| A. | q = 1 |
| B. | q= 0.1 |
| C. | q = F |
| D. | q= 0 |
| Answer» B. q= 0.1 | |
| 2. |
If feed is saturated vapor, then |
| A. | q = 1 |
| B. | q= 0.5 |
| C. | q= 0 |
| D. | q= infinite |
| Answer» D. q= infinite | |
| 3. |
Sometime the reboiler is also considered as the |
| A. | Reflux item |
| B. | Extra equity |
| C. | Heat extractor |
| D. | Extra Stage |
| Answer» E. | |
| 4. |
In the Fenske s equation, xw and yw are |
| A. | Equilibrium liquid and vapor concentration |
| B. | Equilibrium distilled content |
| C. | Partial vapor concentrations of liquid and solid |
| D. | Total vapor and liquid rate |
| Answer» B. Equilibrium distilled content | |
| 5. |
If the D -> 0, then the condition is called as |
| A. | Total Boil up |
| B. | No distillation |
| C. | No Separation |
| D. | Total Reflux |
| Answer» E. | |
| 6. |
If the ideal trays are 7.7 and the efficiency of each one is 0.5, then real number of trays are |
| A. | 15.4 |
| B. | 14.1 |
| C. | 15.0 |
| D. | 18.5 |
| Answer» B. 14.1 | |
| 7. |
The real number of trays are obtained as ratio of |
| A. | Number of ideal trays and flow rate |
| B. | Number of ideal trays and efficiency |
| C. | Number of ideal trays and reflux ratio |
| D. | Number of ideal trays and stripping ratio |
| Answer» C. Number of ideal trays and reflux ratio | |
| 8. |
If R=1.5 and xd= 0.96, then intercept of enriching line is estimated as |
| A. | 0.384 |
| B. | 0.234 |
| C. | 0.5 |
| D. | 0.96 |
| Answer» B. 0.234 | |
| 9. |
The overall material balance of the tower is given by |
| A. | L= V+W |
| B. | F=D+W |
| C. | D= F+HD |
| D. | D= V+HD |
| Answer» C. D= F+HD | |