MCQOPTIONS
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MCQOPTIONS
This section includes 17 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. |
A Pinch point may occur at intersection of feed line and |
| A. | Stream line |
| B. | Stripping line |
| C. | Rectifying line |
| D. | Equilibrium line |
| Answer» E. | |
| 2. |
If xD=0.95, xW= 0.04 and α=2.5. Find total trays? |
| A. | 7 |
| B. | 6.7 |
| C. | 7.7 |
| D. | 6 |
| Answer» C. 7.7 | |
| 3. |
Slope of rectifying line is given by |
| A. | R/XD |
| B. | R/(R+1) |
| C. | F/ (D+W) |
| D. | R/(R+1) |
| Answer» C. F/ (D+W) | |
| 4. |
Calculate minimum reflux? If intercept is 0.56 and XD= 0.96 |
| A. | 0.174 |
| B. | 0.125 |
| C. | 0.21 |
| D. | 0.28 |
| Answer» B. 0.125 | |
| 5. |
If ZF=0.6 and also feed contains 72% mole of the liquid, then intercept of x axis is |
| A. | 0.744 |
| B. | 0.899 |
| C. | 0.833 |
| D. | 1.2 |
| Answer» D. 1.2 | |
| 6. |
If ZF¬=0.58 and also feed contains 35% mole of the liquid, then intercept of y axis is |
| A. | 0.892 |
| B. | 0.205 |
| C. | 0.707 |
| D. | Can’t be calculated |
| Answer» B. 0.205 | |
| 7. |
If F= 200 kmol/h and ZF=0.4, XD=0.95, XW=0.04 and R=2.0, Then D is |
| A. | 88.1 |
| B. | 22.6 |
| C. | 79.1 |
| D. | 158.2 |
| Answer» D. 158.2 | |
| 8. |
IF_XD=0.95,_XW=_0.04_AND_‚ÂÀ√≠¬¨¬±=2.5._FIND_TOTAL_TRAYS??$# |
| A. | 7 |
| B. | 6.7 |
| C. | 7.7 |
| D. | 6 |
| Answer» C. 7.7 | |
| 9. |
A_Pinch_point_may_occur_at_intersection_of_feed_line_and$ |
| A. | Stream line |
| B. | Stripping line |
| C. | Rectifying line |
| D. | Equilibrium line |
| Answer» E. | |
| 10. |
Slope of rectifying line is given b? |
| A. | R/X<sub>D</sub> |
| B. | R/(R+1) |
| C. | F/ (D+W) |
| D. | R/(R+1) |
| Answer» C. F/ (D+W) | |
| 11. |
Calculate minimum reflux? If intercept is 0.56 and XD= 0.96 |
| A. | 0.174 |
| B. | 0.125 |
| C. | 0.21 |
| D. | 0.28 |
| Answer» B. 0.125 | |
| 12. |
If ZF=0.6 and also feed contains 72% mole of the liquid, then intercept of x axis is |
| A. | 0.744 |
| B. | 0.899 |
| C. | 0.833 |
| D. | 1.2 |
| Answer» D. 1.2 | |
| 13. |
If ZF¬=0.58 and also feed contains 35% mole of the liquid, then intercept of y axis is$ |
| A. | 0.892 |
| B. | 0.205 |
| C. | 0.707 |
| D. | Can’t be calculated |
| Answer» B. 0.205 | |
| 14. |
Calculate Boil up? If vapor flow and bottom withdrawal are 237.3 and 120.9 respectively |
| A. | 1.5 |
| B. | 2.9 |
| C. | 2.111 |
| D. | 1.963 |
| Answer» E. | |
| 15. |
The very First step of McCabe method is? |
| A. | Plot the equilibrium curve |
| B. | Plot diagonal curve |
| C. | Plot Operating line |
| D. | Plot stripping line |
| Answer» B. Plot diagonal curve | |
| 16. |
If F= 200 kmol/h and ZF=0.4, XD=0.95, XW=0.04 and R=2.0, Then D is |
| A. | 88.1 |
| B. | 22.6 |
| C. | 79.1 |
| D. | 158.2 |
| Answer» D. 158.2 | |
| 17. |
The component balance of the component A is given as |
| A. | Fz<sub>F</sub>= Dx<sub>D</sub> + Wx<sub>w</sub> |
| B. | Fz<sub>F</sub>= Dx<sub>D</sub> – Wx<sub>w</sub> |
| C. | Fz<sub>F</sub>= Dx<sub>D</sub>/Wx<sub>w</sub> |
| D. | Fz<sub>F</sub>= Dx<sub>D</sub> *Wx<sub>w</sub> |
| Answer» B. Fz<sub>F</sub>= Dx<sub>D</sub> ‚Äö√Ñ√∂‚àö√ë‚àö¬® Wx<sub>w</sub> | |