 
			 
			MCQOPTIONS
 Saved Bookmarks
				This section includes 12 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 the previous question if the floor has micro pores and water penetrates the floor at a constant rate of 0.1kg/m2h, what will be the time required for the water layer to disappear? | 
| A. | 3.64h | 
| B. | 4.73h | 
| C. | 5.94h | 
| D. | 2.36h | 
| Answer» B. 4.73h | |
| 2. | In an accident a container containing ethanol(s.g 0.789) falls down in a room of dimension 1*1*2(all in m). Ethanol forms a layer of 2mm. Ethanol vaporizes and diffuses through a stagnant film of air of thickness 2.5mm. What will be the time required for the water layer to disappear completely. The diffusivity of ethanol in air is 2.567*10-5 m2/s. the total pressure is 1.013 bar and the pressure of ethanol in bulk air is 0.02244 bar and at the ethanol-air interface is 0.02718bar. The temperature is 25.2°C. | 
| A. | 4.73h | 
| B. | 14.6h | 
| C. | 5.87h | 
| D. | 16.2h | 
| Answer» B. 14.6h | |
| 3. | In order to prepare Lithium nitride, air is passed gently over a reactor. Suppose that Nitrogen diffuse to a length 5cm before getting reacted with Lithium. Nitrogen reacts with lithium quickly so that partial pressure of Nitrogen at that point is 0. Reactor is a cylinder of length 10cm and diameter 2cm. Assume air to be a mixture of Nitrogen and Oxygen only. The temperature is 298K and total pressure 1atm. Diffusivity of N2 in O2 is 2*10-5m2/s. Calculate the Molar flux (mol/m2.s) of N2 at a distance of 2.5cm from the top with respect to an observer moving with twice the mass average velocity a direction towards the liquid surface. (R=8.205*10-5m3atmK-1mol-1). Assume z=0 at the top of the reactor. | 
| A. | 4.242*10-4 | 
| B. | 4.242*10-5 | 
| C. | 4.242*10-3 | 
| D. | 4.242*10-2 | 
| Answer» B. 4.242*10-5 | |
| 4. | Oxygen diffuses through a stagnant layer of air, 1mm thick, ambient temperature 28°C and 1atm total pressure. The partial pressure of oxygen on two sides of layer is P1=0.9atm and P2=0.1atm respectively. Calculate the value of Molar flux (in mol/m2.s) with respect to an observer moving with molar average velocity. Calculate this value at the end of the path where P2=0.1atm. Use R=8.205*10-5m3atmK-1mol-1. | 
| A. | 2.713 | 
| B. | 1.713 | 
| C. | 0.1713 | 
| D. | 0.01713 | 
| Answer» C. 0.1713 | |
| 5. | For a gas mixture (A+B) equimolar counterdiffusion takes place. Which among the following statements are correct for molar flux? | 
| A. | If temperature is doubled, the flux will get halved | 
| B. | If diffusion length is halved, the flux will get halved | 
| C. | If temperature is halved, the flux will get halved | 
| D. | If temperature is doubled and length is halved, the flux will become four times | 
| Answer» B. If diffusion length is halved, the flux will get halved | |
| 6. | A cylinder of sulfur is kept in a large volume of stagnant air for sublimation. How much time will be required for its complete sublimation? | 
| A. | One fourth the time required by sphere of same mass | 
| B. | Half the time required by a cube of same mass | 
| C. | One fourth the time required by a cube of same mass | 
| D. | Infinite | 
| Answer» E. | |
| 7. | The molar average velocity of the components in a binary mixture in which they are in equimolar counter diffusion is | 
| A. | Equal to mass average velocity | 
| B. | Zero | 
| C. | Always negative | 
| D. | Always positive | 
| Answer» C. Always negative | |
| 8. | In the previous question if the floor has micro pores and water penetrates the floor at a constant rate of 0.1kg/m2h, what will be the time required for the water layer to disappear? | 
| A. | 3.64h | 
| B. | 4.73h | 
| C. | 5.94h | 
| D. | 2.36h | 
| Answer» B. 4.73h | |
| 9. | In an accident a container containing ethanol(s.g 0.789) falls down in a room of dimension 1*1*2(all in m). Ethanol forms a layer of 2mm. Ethanol vaporizes and diffuses through a stagnant film of air of thickness 2.5mm. What will be the time required for the water layer to disappear completely. The diffusivity of ethanol in air is 2.567*10-5 m2/s. the total pressure is 1.013 bar and the pressure of ethanol in bulk air is 0.02244 bar and at the ethanol-air interface is 0.02718bar. The temperature is 25.2°C.$ | 
| A. | 4.73h | 
| B. | 14.6h | 
| C. | 5.87h | 
| D. | 16.2h | 
| Answer» B. 14.6h | |
| 10. | A binary liquid mixture is separated by distillation process. The more volatile A vaporizes while less volatile B gets transported in opposite direction. Latent heat of vaporization of A and B is 0.5unit and 1unit respectively. What will be the relation between molar flux of A and B | 
| A. | N<sub>A</sub>=2N<sub>B</sub> | 
| B. | 2N<sub>A</sub>=N<sub>B</sub> | 
| C. | N<sub>A</sub>=4N<sub>B</sub> | 
| D. | 4N<sub>A</sub>=N<sub>B</sub> | 
| Answer» B. 2N<sub>A</sub>=N<sub>B</sub> | |
| 11. | In order to prepare Lithium nitride, air is passed gently over a reactor. Suppose that Nitrogen diffuse to a length 5cm before getting reacted with Lithium. Nitrogen reacts with lithium quickly so that partial pressure of Nitrogen at that point is 0. Reactor is a cylinder of length 10cm and diameter 2cm. Assume air to be a mixture of Nitrogen and Oxygen only. The temperature is 298K and total pressure 1atm. Diffusivity of N2 in O2 is 2*10-5m2/s. Calculate the Molar flux (mol/m2.s) of N2 at a distance of 2.5cm from the top with respect to an observer moving with twice the mass average velocity a direction towards the liquid surface. (R=8.205*10-5m3atmK-1mol-1). Assume z=0 at the top of the reactor. | 
| A. | 4.242*10<sup>-4</sup> | 
| B. | 4.242*10<sup>-5</sup> | 
| C. | 4.242*10<sup>-3</sup> | 
| D. | 4.242*10<sup>-2</sup> | 
| Answer» B. 4.242*10<sup>-5</sup> | |
| 12. | Oxygen diffuses through a stagnant layer of air, 1mm thick, ambient temperature 28°C and 1atm total pressure. The partial pressure of oxygen on two sides of layer is P1=0.9atm and P2=0.1atm respectively. Calculate the value of Molar flux (in mol/m2.s) with respect to an observer moving with molar average velocity. Calculate this value at the end of the path where P2=0.1atm. Use R=8.205*10-5m3atmK-1mol-1. | 
| A. | 2.713 | 
| B. | 1.713 | 
| C. | 0.1713 | 
| D. | 0.01713 | 
| Answer» C. 0.1713 | |