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This section includes 640 Mcqs, each offering curated multiple-choice questions to sharpen your Chemical Engineering knowledge and support exam preparation. Choose a topic below to get started.
201. |
A concentric double pipe heat exchanger as compared to the shell and tube heat exchanger for the same heat load requires |
A. | less heating surface. |
B. | more space. |
C. | lower maintenance cost. |
D. | none of these. |
Answer» C. lower maintenance cost. | |
202. |
Radiation heat transfer rates does not depend upon the |
A. | type of absorbing surface. |
B. | distance between the heat source and the object receiving the heat. |
C. | surface area and temperature of the heat source. |
D. | none of these. |
Answer» E. | |
203. |
Which has the lowest Prandtl number ? |
A. | Liquid metal |
B. | Aqueous solution |
C. | Water |
D. | Lube oil |
Answer» B. Aqueous solution | |
204. |
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 | |
205. |
Evaporator tubes are generally |
A. | horizontal |
B. | vertical |
C. | inclined |
D. | random |
Answer» C. inclined | |
206. |
A composite wall consists of two plates A and B placed in series normal to the flow of heat. The thermal conductivities are kA and kB and the specific heat capacities are CPA and CPB for plates A and B respectively. Plate B has twice the thickness of plate A. At steady state, the temperature difference across plate A is greater than that across plate B, when |
A. | CPA > CPB |
B. | CPA < CPB |
C. | kA < 0.5kB |
D. | kA>2 kB |
Answer» D. kA>2 kB | |
207. |
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. | |
208. |
__________ heat exchanger is the most suitable, when the temperature of shell side fluid is much higher than that of tube side. |
A. | Single pass, fixed tube sheet |
B. | U-tube |
C. | Three pass, fixed tube sheet |
D. | none of these |
Answer» C. Three pass, fixed tube sheet | |
209. |
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 | |
210. |
Heat flux, as defined in heat flow is analogous to __________ in electricity flow. |
A. | current |
B. | voltage |
C. | resistance |
D. | none of these |
Answer» B. voltage | |
211. |
In the free convection regime of pool boiling, the heat flux is proportional to |
A. | Δt1/2 |
B. | Δt2 |
C. | Δt5/4 |
D. | Δt |
Answer» D. Œît | |
212. |
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 | |
213. |
For a given ambient air temperature with increase in the thickness of insulation of a hot cylinderical pipe, the rate of heat loss from the surface would |
A. | decrease |
B. | increase |
C. | first decrease and then increase |
D. | first increase and then decrease |
Answer» E. | |
214. |
In a parallel flow heat exchanger, if the outlet temperature of hot and cold fluids are the same, then the log mean temperature difference (LMTD) is |
A. | minimum |
B. | maximum |
C. | zero |
D. | infinity |
Answer» D. infinity | |
215. |
Evaporation by thermocompression results in the |
A. | saving of steam. |
B. | realisation of multiple effect economy in a single effect. |
C. | both (a) and (b). |
D. | none of these. |
Answer» D. none of these. | |
216. |
Heat sensitive materials can be concentrated in an evaporator employing |
A. | vacuum |
B. | high pressure |
C. | high residence time |
D. | none of these |
Answer» B. high pressure | |
217. |
200 kg of solids (on dry basis) is subjected to a drying process for a period of 5000 seconds. The drying occurs in the constant rate period with the drying rate as, Nc = 0.5 x 10-3 kg/m2.s. The initial moisture content of the solid is 0.2 kg moisture/kg dry solid. The interfacial area available for drying is 4 m2/1000 kg of dry solid. The moisture content at the end of the drying period is (in kg moisture/kg dry solid) |
A. | 0.5 |
B. | 0.05 |
C. | 0.1 |
D. | 0.15 |
Answer» D. 0.15 | |
218. |
With increase in temperature, the thermal conductivity of a gas |
A. | increases. |
B. | decreases. |
C. | remains same. |
D. | may increase or decrease depending on the type of gas. |
Answer» B. decreases. | |
219. |
The film co-efficient is decreased due to the presence of non-condensing gases in the vapors. The film co-efficient of superheated vapor as compared to that of saturated vapor is |
A. | more |
B. | less |
C. | some |
D. | either more or less ; depends on the nature of vapor |
Answer» D. either more or less ; depends on the nature of vapor | |
220. |
In sub-cooled boiling, |
A. | temperature of the heating surface is less than the boiling point of the liquid. |
B. | temperature of the heating surface is more than the boiling point of the liquid. |
C. | bubbles from heating surface are absorbed by the mass of the liquid. |
D. | very large vapour space is necessary. |
Answer» C. bubbles from heating surface are absorbed by the mass of the liquid. | |
221. |
A metal wire of 0.01 m dia and thermal conductivity 200 W/m.K is exposed to a fluid stream with a convective heat transfer coefficient of 100 W/m2.K. The Biot number is |
A. | 5.6 |
B. | 0.025 |
C. | 3.5 |
D. | 0.0035 |
Answer» C. 3.5 | |
222. |
Natural convection is characterised by |
A. | Grashhoff number |
B. | Peclet number |
C. | Reynolds number |
D. | Prandtl number |
Answer» B. Peclet number | |
223. |
Thermal conductivity of a gas at low density, __________ with increase in temperature. |
A. | decreases |
B. | increases |
C. | remains unchanged |
D. | may increase or decrease; depends on the gas |
Answer» C. remains unchanged | |
224. |
For turbulent flow in a tube, the heat transfer co-efficient is obtained from the Dittus-Boelter correlation. If the tube diameter is halved and the flow rate is doubled, then the heat transfer co-efficient will change by a factor of |
A. | 1 |
B. | 1.74 |
C. | 6.1 |
D. | 37 |
Answer» D. 37 | |
225. |
When warm and cold liquids are mixed, the heat transfer is mainly by |
A. | conduction |
B. | convection |
C. | radiation |
D. | both(a) & (c) |
Answer» C. radiation | |
226. |
Sensible heat absorbed by 1 lb of water when it is heated from 32 to 212°F may be around __________ BTU.$ |
A. | 180 |
B. | 970 |
C. | 3.97 |
D. | data insufficient, can't be predicted |
Answer» B. 970 | |
227. |
For a perfectly transparent surface (like gases), the |
A. | absorptivity = 0 |
B. | transmissivity = 1 |
C. | reflectivity = 0 |
D. | all (a), (b) & (c) |
Answer» C. reflectivity = 0 | |
228. |
To reduce the tube side pressure drop for the same flow rate, the heat exchanger recomended is |
A. | 1-2 heat exchanger |
B. | 1-1 heat exchanger |
C. | 3-2 heat exchanger |
D. | 2-4 heat exchanger |
Answer» C. 3-2 heat exchanger | |
229. |
1000 Kg of liquid at 30°C in a well stirred vessel has to be heated to 120°C, using immersed coils carrying condensing steam at 150°C. The area of the steam coils is 1.2 m2 and the overall heat transfer co-efficient to the liquid is 1500 W/m2.°C. Assuming negligible heat loss to the surrounding and specific heat capacity of the liquid to be 4 kJ/kg.°C, the time taken for the liquid to reach desired temperature will be$ |
A. | 15 min |
B. | 22 min |
C. | 44 min |
D. | 51 min |
Answer» E. | |
230. |
In case of a vertical tube evaporator, with increase in the liquor level, the |
A. | capacity of the evaporator is decreased. |
B. | capacity of the evaporator is increased. |
C. | true temperature drop increases. |
D. | both (b) and (c). |
Answer» B. capacity of the evaporator is increased. | |
231. |
In a co-current double pipe heat exchanger used for condensing saturated steam over the inner tube, if the entrance and exit conditions of the coolant are interchanged, then the rate of condensation will |
A. | increase |
B. | decrease |
C. | remain unchanged |
D. | either increase or decrease; depends on the coolant flow rate |
Answer» D. either increase or decrease; depends on the coolant flow rate | |
232. |
If heat transfer rate varies with the time, it is termed as |
A. | forced convection |
B. | steady state conduction |
C. | monochromatic radiation |
D. | none of these |
Answer» E. | |
233. |
Steam economy in case of a triple effect evaporator will be |
A. | 1 |
B. | < 1 |
C. | > 1 |
D. | between 0 and 1 |
Answer» D. between 0 and 1 | |
234. |
Rate of heat transfer by vaporisation from pools of water is affected by the |
A. | nature of heating surface and distribution of bubbles. |
B. | surface tension of water. |
C. | viscosity of water. |
D. | all (a), (b) and (c). |
Answer» E. | |
235. |
Open pan evaporators are preferred to be used, when the solution to be concentrated is |
A. | scaling |
B. | highly viscous |
C. | corrosive |
D. | salty |
Answer» C. corrosive | |
236. |
Sensible heat of hot industrial flue gases can not be recovered by a/an |
A. | economiser |
B. | regenerator |
C. | ceramic recuperator |
D. | none of these |
Answer» E. | |
237. |
Tube pitch is the __________ of tube diameters and the clearances. |
A. | sum |
B. | difference |
C. | ratio |
D. | none of these |
Answer» B. difference | |
238. |
In a single evaporator system, the steam economy __________ by creating vacuum in the evaporator. |
A. | increases |
B. | decreases |
C. | remains constant |
D. | may increase or decrease, depends on the vacuum |
Answer» B. decreases | |
239. |
At what value of Prandtl number, the hydrodynamic and thermal boundary layers of a fluid flowing over a heated plate will be identical ? |
A. | 1 |
B. | < 1 |
C. | > 1 |
D. | none of these |
Answer» B. < 1 | |
240. |
For a laminar flow of fluid in a circular tube, 'h1' is the convective heat transfer co-efficient at velocity 'V1'. 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 h1 |
B. | 0.794 h1 |
C. | 0.574 h1 |
D. | 1.741 h1 |
Answer» C. 0.574 h1 | |
241. |
Dietus-Boelter equation cannot be used for molten metals mainly due to its very low |
A. | Prandtl number |
B. | Grashoff number |
C. | thermal conductivity |
D. | viscosity |
Answer» B. Grashoff number | |
242. |
For the same heat transfer area and the terminal conditions, the ratio of the capacities of a single effect evaporator to a triple effect evaporator is |
A. | 3 |
B. | 0.33 |
C. | 1 |
D. | 1.33 |
Answer» D. 1.33 | |
243. |
In evaporators, lowering the feed temperature |
A. | increases the heating area required. |
B. | reduces the economy. |
C. | both (a) and (b). |
D. | decreases the heating area required. |
Answer» D. decreases the heating area required. | |
244. |
Which of the following has the lowest Prandtl number ? |
A. | Molten sodium (a coolant used in fast breeder reactor) |
B. | Water |
C. | Transformer oil |
D. | Dilute H2SO4 |
Answer» B. Water | |
245. |
In an interphase heat transfer process, the equilibrium state corresponds to equality of temperature in the two phases, while the condition for equilibrium in an interphase mass transfer process is equality of |
A. | concentrations |
B. | chemical potentials |
C. | activity co-efficients |
D. | mass transfer co-efficients |
Answer» B. chemical potentials | |
246. |
The equation, Nst = f/2, is the __________ analogy. |
A. | Colburn |
B. | Reynolds |
C. | Prandtl |
D. | none of these |
Answer» C. Prandtl | |
247. |
In a shell and tube type heat exchanger, the floating tube bundle heat arrangement is used |
A. | in low range of temperature differences. |
B. | in high range of temperature differences. |
C. | because of its low cost. |
D. | to prevent corrosion of the tube bundles. |
Answer» C. because of its low cost. | |
248. |
Three material A, B and C of equal thick-nes and of thermal conductivity of 20, 40 & 60 kcal/hr. m. °C respectively are joined together. The temperature outside of A and C are 30°C and 100°C respectively. The interface between B and C will be at a temperature of __________ °C.$ |
A. | 40 |
B. | 95 |
C. | 70 |
D. | 50 |
Answer» D. 50 | |
249. |
Boiling point elevation of a solution of NaOH |
A. | increases rapidly with temperature rise. |
B. | is almost independent of temperature. |
C. | is almost independent of pressure. |
D. | both (b) and (c). |
Answer» E. | |
250. |
With increase in temperature, the thermal conductivity of fresh lubricating oil |
A. | increases |
B. | decreases |
C. | remains unchanged |
D. | may increase or decrease; depends on its composition |
Answer» C. remains unchanged | |