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This section includes 482 Mcqs, each offering curated multiple-choice questions to sharpen your Chemical Engineering knowledge and support exam preparation. Choose a topic below to get started.
151. |
*/*_What is the thermal conductivity of a perfect heat insulator?? |
A. | Zero |
B. | One |
C. | ‚Äö√ √ª |
D. | Between 0 and ‚Äö√ √ª |
Answer» B. One | |
152. |
*/*_In a multipass shell and tube heat exchanger, tube side return pressure loss is equal to __________ the velocity head.? |
A. | Twice |
B. | Four times |
C. | Square root of |
D. | Square of |
Answer» C. Square root of | |
153. |
*/*_'Duhring's plot' is of use in? |
A. | Extractive distillation |
B. | Evaporation |
C. | Leaching |
D. | Absorption |
Answer» C. Leaching | |
154. |
*/*_A black body does not __________ radiation.? |
A. | Absorb or emit |
B. | Refract |
C. | Reflect |
D. | Both B & C |
Answer» E. | |
155. |
*/*_In case of heat transfer by conduction in a hollow cylinder, __________ mean area is used to calculate the heat transfer rate.? |
A. | Geometric |
B. | Arithmetic |
C. | Logarithmic |
D. | Either A, B or C |
Answer» D. Either A, B or C | |
156. |
*/*_Natural convection is characterised by? |
A. | Grashhoff number |
B. | Peclet number |
C. | Reynolds number |
D. | Prandtl number |
Answer» B. Peclet number | |
157. |
*/*_Choose the correct equation.? |
A. | Nu = (Re) (Pr) (Gz) |
B. | Nu = (Re) (Pr) (St) |
C. | Nu = (Re)(Pr) |
D. | Nu = (Pr)(St) |
Answer» C. Nu = (Re)(Pr) | |
158. |
*/*_Mode of heat transfer in which the fluid moves under the influence of changes in fluid pressure produced by external work is called? |
A. | Radiation |
B. | Natural convection |
C. | Forced convection |
D. | Conduction |
Answer» D. Conduction | |
159. |
*/*_Heat transfer co-efficient (h1) for liquids increases with? |
A. | Increasing temperature |
B. | Decreasing temperature |
C. | Decreasing Reynolds number |
D. | None of these |
Answer» B. Decreasing temperature | |
160. |
*/*_Wavelength corresponding to the maximum energy is inversely proportional to the absolute temperature. This is __________ law.? |
A. | Stefan's |
B. | Dalton's |
C. | Wien's |
D. | Kirchoffs |
Answer» D. Kirchoffs | |
161. |
*/*_For what value of Prandtl number, St = f/2?? |
A. | 1.5 |
B. | 1 |
C. | > 1 |
D. | < 1 |
Answer» C. > 1 | |
162. |
*/*_Baffles are provided in heat exchangers to increase the? |
A. | Fouling factor |
B. | Heat transfer area |
C. | Heat transfer co-efficient |
D. | Heat transfer rate |
Answer» D. Heat transfer rate | |
163. |
*/*_Film condensation is promoted on a/an __________ surface.? |
A. | Oily |
B. | Coated |
C. | Clean & smooth |
D. | Dirty |
Answer» D. Dirty | |
164. |
*/*_Boiling point elevation of an ideal solution? |
A. | Increases rapidly with temperature rise |
B. | Decreases rapidly with temperature rise |
C. | In independent of pressure |
D. | Both B and C |
Answer» B. Decreases rapidly with temperature rise | |
165. |
*/*_A fluid is flowing inside the inner tube of a double pipe heat exchanger with diameter 'd'. For a fixed mass flow rate, the tube side heat transfer co-efficient for turbulent flow conditions is proportional to? |
A. | D0.8 |
B. | D-0.2 |
C. | D-1 |
D. | D-1.8 |
Answer» C. D-1 | |
166. |
*/*_Tube pitch is the __________ of tube diameters and the clearances.? |
A. | Sum |
B. | Difference |
C. | Ratio |
D. | None of these |
Answer» B. Difference | |
167. |
*/*_For a laminar flow of fluid in a circular tube, 'h‚ÇÅ' is the convective heat transfer co-efficient at velocity 'V‚ÇÅ'. If the velocity is reduced by half and assuming the fluid properties are constant, the new convective heat transfer co-efficient is? |
A. | 1.26 h‚ÇÅ |
B. | 0.794 h‚ÇÅ |
C. | 0.574 h‚ÇÅ |
D. | 1.741 h‚ÇÅ |
Answer» C. 0.574 h‚Äö√á√Ö | |
168. |
*/*_When vaporisation takes place directly at the heating surface, it is called? |
A. | Film boiling |
B. | Nucleate boiling |
C. | Vapour binding |
D. | None of these |
Answer» C. Vapour binding | |
169. |
*/*_A single pass air heater is connected to a two pass unit. For the air flow rate and other conditions remaining the same, the film heat transfer co-efficient for air will vary in the ratio of? |
A. | 2 |
B. | 20.8 |
C. | 20.2 |
D. | 20.5 |
Answer» C. 20.2 | |
170. |
*/*_In a multiple effect evaporator, the effect of boiling point elevation is to? |
A. | Reduce the capacity |
B. | Reduce the economy |
C. | Increase the economy |
D. | None of these |
Answer» B. Reduce the economy | |
171. |
*/*_In case of a shell and tube heat exchanger, the minimum and maximum baffle spacing is respectively (where, D = inside diameter of the shell)? |
A. | D/5 and D |
B. | D/2 and 2 D |
C. | D/4 and 2 D |
D. | D and 2 D |
Answer» B. D/2 and 2 D | |
172. |
*/*_LMTD for evaporators & condensers for a given terminal parameters & set of conditions for counterflow is equal to that for parallel flow. In such heat exchangers, with one of the fluids condensing or evaporating, the surface area required is the least in the __________ flow.? |
A. | Parallel |
B. | Mixed |
C. | Counterflow |
D. | Same in either A, B or C |
Answer» E. | |
173. |
%_Log mean temperature difference (LMTD) cannot be used, if_% |
A. | Heat transfer co-efficient over the entire heat exchanger is not constant |
B. | There exists an unsteady state |
C. | The heat capacity is not constant and there is a phase change |
D. | None of these |
Answer» E. | |
174. |
%_Walls of a cubical oven are of thickness l, and they are made of material of thermal conductivity k. The temperature inside the oven is 100°C and the inside heat transfer co-efficient is 3k/l. If the wall temperature on the outside is held at 25°C, what is the inside wall temperature in degree centigrade?_% |
A. | 35.5 |
B. | 43.75 |
C. | 81.25 |
D. | 48.25 |
Answer» D. 48.25 | |
175. |
%_Evaporator tubes are generally_% |
A. | Horizontal |
B. | Vertical |
C. | Inclined |
D. | Random |
Answer» C. Inclined | |
176. |
%_Steam condensate is recovered by steam traps and recycled for use as boiler feed water, because of its low_% |
A. | Hardness |
B. | Dissolved soilds content |
C. | Suspended solids content |
D. | All of the above |
Answer» E. | |
177. |
%_The rate of heat transfer is a product of overall heat transfer co-efficient, the difference in temperature and the_% |
A. | Heating volume |
B. | Heat transfer area |
C. | Nusselt number |
D. | None of these |
Answer» C. Nusselt number | |
178. |
%_The sum of reflectivity and absorptivity for an opaque body is equal to_% |
A. | 0.5 |
B. | 1 |
C. | 0 |
D. | 2 |
Answer» C. 0 | |
179. |
%_Fouling factor_% |
A. | Is a dimensionless quantity |
B. | Does not provide a safety factor for design |
C. | Accounts for additional resistances to heat flow |
D. | None of these |
Answer» D. None of these | |
180. |
%_Heat transfer in the laminar sublayer in case of a liquid flowing through a pipe, is mostly by_% |
A. | Eddies current |
B. | Conduction |
C. | Convection |
D. | None of these |
Answer» C. Convection | |
181. |
%_Heat transfer co-efficient (h1) for liquids increases with_% |
A. | Increasing temperature |
B. | Decreasing temperature |
C. | Decreasing Reynolds number |
D. | None of these |
Answer» B. Decreasing temperature | |
182. |
%_Wavelength corresponding to the maximum energy is inversely proportional to the absolute temperature. This is __________ law._% |
A. | Stefan's |
B. | Dalton's |
C. | Wien's |
D. | Kirchoffs |
Answer» D. Kirchoffs | |
183. |
%_Choose the correct equation._% |
A. | Nu = (Re) (Pr) (Gz) |
B. | Nu = (Re) (Pr) (St) |
C. | Nu = (Re)(Pr) |
D. | Nu = (Pr)(St) |
Answer» C. Nu = (Re)(Pr) | |
184. |
%_Mode of heat transfer in which the fluid moves under the influence of changes in fluid pressure produced by external work is called_% |
A. | Radiation |
B. | Natural convection |
C. | Forced convection |
D. | Conduction |
Answer» D. Conduction | |
185. |
%_In case of heat transfer by conduction in a hollow cylinder, __________ mean area is used to calculate the heat transfer rate._% |
A. | Geometric |
B. | Arithmetic |
C. | Logarithmic |
D. | Either A, B or C |
Answer» D. Either A, B or C | |
186. |
%_Natural convection is characterised by_% |
A. | Grashhoff number |
B. | Peclet number |
C. | Reynolds number |
D. | Prandtl number |
Answer» B. Peclet number | |
187. |
%_'Duhring's plot' is of use in_% |
A. | Extractive distillation |
B. | Evaporation |
C. | Leaching |
D. | Absorption |
Answer» C. Leaching | |
188. |
%_A black body does not __________ radiation._% |
A. | Absorb or emit |
B. | Refract |
C. | Reflect |
D. | Both B & C |
Answer» E. | |
189. |
%_Extended heat transfer surface like fins are used to increase the heat transfer rate. Fin efficiency is defined as the ratio of heat transferred across the fin surface to the theoretical heat transfer across an equal area held at the_% |
A. | Surrounding temperature |
B. | Average temperature of the fin |
C. | Temperature of the fin end |
D. | Constant temperature equal to that of the base |
Answer» E. | |
190. |
%_What is the unit of thermal conductivity ?_% |
A. | Kcal/hr. m² °C |
B. | Kcal/hr.m.°C |
C. | Kcal/hr.m |
D. | Kcal/hr. °C |
Answer» C. Kcal/hr.m | |
191. |
%_The heat flux in the nucleate boiling regimes is proportional to (where, ΔT = excess temperature)_% |
A. | (ΔT)² |
B. | (ΔT)⁴ |
C. | (ΔT)³ |
D. | ‚Äö√ √∂(≈í√ÆT) |
Answer» D. ‚Äö√ √∂(≈í√ÆT) | |
192. |
%_Which of the following accessories is provided in the vapor line of an evaporator for removing the entrained liquid?_% |
A. | Bleed point |
B. | Vent |
C. | Catchall |
D. | Baffle |
Answer» D. Baffle | |
193. |
%_In a shell and tube heat exchanger, the shell side fluid velocity can not be changed by changing the_% |
A. | Tube layout |
B. | Tube diameter |
C. | Tube pitch |
D. | No. of baffles |
Answer» C. Tube pitch | |
194. |
%_It is not recommended to use a 1-2 shell and tube heat exchanger for a particular heat duty, whenever the LMTD correction factor is_% |
A. | > 0.75 |
B. | < 0.75 |
C. | < 0.50 |
D. | < 0.25 |
Answer» C. < 0.50 | |
195. |
%_Heat transfer by conduction results due to the transfer of free electrons, kinetic energy & vibrational energy from one molecule to another. Conduction heat transfer can not take place_% |
A. | Between two bodies in physical contact with each other |
B. | Between two bodies not in physical contact with each other |
C. | From one part of a body to the another part of the same body |
D. | Both B & C |
Answer» C. From one part of a body to the another part of the same body | |
196. |
%_What is the steam economy in case of a single effect evaporator system?_% |
A. | 1 |
B. | >1 |
C. | < 1 |
D. | 0.1 |
Answer» D. 0.1 | |
197. |
%_An evaporator while concentrating an aqueous solution from 10 to 40% solids evaporates 30000 kg of water. The amount of solids handled by the system in kg is_% |
A. | 4000 |
B. | 9000 |
C. | 4600 |
D. | 3000 |
Answer» B. 9000 | |
198. |
%_The purpose of floating head in a heat exchanger is to_% |
A. | Avoid buckling of tubes |
B. | Provide support for tubes |
C. | Decrease the pressure drop |
D. | Facilitate its lengthening, if needed |
Answer» B. Provide support for tubes | |
199. |
%_The driving potential for the crystal growth during crystallisation is the __________ of the solution._% |
A. | Concentration |
B. | Viscosity |
C. | Super-saturation |
D. | Density |
Answer» D. Density | |
200. |
%_The heat flux (from outside to inside) across an insulating wall with thermal conductivity, K= 0.04 W/m.°K and thickness 0.16m is 10 W/m². The temperature of the inside wall is - 5°C. The outside wall temperature is_% |
A. | 25°C |
B. | 30°C |
C. | 35°C |
D. | 40°C |
Answer» D. 40¬¨‚àûC | |