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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.
301. |
In a forward feed multiple effect, the pressure build up will be |
A. | least at the inlet of the first effect. |
B. | least at the outlet of the last effect. |
C. | highest at the inlet of the last effect. |
D. | highest at the outlet of the last effect. |
Answer» C. highest at the inlet of the last effect. | |
302. |
__________ equation relates the thermal conductivity of a solid to its temperature. |
A. | Antonie |
B. | Kopp's |
C. | Lee's |
D. | Kistyakowski |
Answer» D. Kistyakowski | |
303. |
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. | |
304. |
In a forward feed multiple effect evaporator, the pressure is |
A. | highest in last effect |
B. | lowest in last effect |
C. | same in all effects |
D. | dependent on the number of effects |
Answer» C. same in all effects | |
305. |
When the ratio of the Grashoff number and to the square of Reynolds number is one, the dominant mechanism of heat transfer is |
A. | free convection |
B. | entry length problem in laminar forced conduction (developing thermal boundary layer) |
C. | mixed convection (both free and forced) |
D. | forced convection |
Answer» D. forced convection | |
306. |
Analogy between mass and heat transfer is not applicable in case of |
A. | same velocity profile or equal eddy diffusivities. |
B. | thermal or pressure mass diffusion. |
C. | viscous heating or chemical reaction. |
D. | both (b) and (c). |
Answer» E. | |
307. |
In a 1-1 cocurrent heat exchanger, if the tube side fluid outlet temperature is equal to the shell side fluid outlet temperature, then the LMTD is |
A. | ‚àû |
B. | 0 |
C. | equal to the difference between hot and cold fluids inlet temperature. |
D. | equal to the difference between hot fluid inlet temperature and cold fluid outlet temperature. |
Answer» C. equal to the difference between hot and cold fluids inlet temperature. | |
308. |
A hot body will radiate heat most rapidly, if its surface is |
A. | white & rough |
B. | black & rough |
C. | white & polished |
D. | black & polished |
Answer» C. white & polished | |
309. |
In a heat exchanger, one transfer unit means |
A. | a section of the exchanger in which change in temperature of one stream equals the average driving force in the section. |
B. | the size of the exchanger in which heat transfer rate is 1 kcal/hr. |
C. | both (a) and (b) |
D. | none of these |
Answer» B. the size of the exchanger in which heat transfer rate is 1 kcal/hr. | |
310. |
Fouling factor for a heat exchanger is given by (where, U1 = heat transfer co-efficient of dirty surface U2 = heat transfer co-efficient of clean surface) |
A. | U1 - U2 |
B. | |
Answer» C. | |
311. |
Radiant energy received by a body is proportional to (where, d = the distance between the object emitting radiation and that receiving it.) |
A. | d |
B. | d |
C. | d2 |
D. | d1.5 |
Answer» D. d1.5 | |
312. |
Conductance is given by(where, x = thickness, A = heat flow area, K = thermal conductivity.) |
A. | x/KA |
B. | KA/x |
C. | K/Ax |
D. | A/Kx |
Answer» C. K/Ax | |
313. |
Agitated film evaporator is suitable for concentrating __________ liquids. |
A. | foaming |
B. | viscous |
C. | very thin |
D. | corrosive |
Answer» C. very thin | |
314. |
Baffle spacing |
A. | is not the same as baffle pitch. |
B. | should be less than one fifth the diameter of the shell. |
C. | should be less than the inside diameter of the shell. |
D. | none of these. |
Answer» D. none of these. | |
315. |
Maximum heat transfer rate is achieved in __________ flow. |
A. | co-current |
B. | counter-current |
C. | turbulent |
D. | laminar |
Answer» D. laminar | |
316. |
The Dietus-Boelter equation for convective leat transfercannot be used for |
A. | low Reynold's number |
B. | very low Grashoff number |
C. | molten metals |
D. | all (a), (b) and (c) |
Answer» E. | |
317. |
Dropwise condensation is promoted on a/an __________ surface. |
A. | glazed |
B. | oily |
C. | coated |
D. | smooth |
Answer» C. coated | |
318. |
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 | |
319. |
Nusselt number is a function of Prandtl number and __________ number of fluid in natural convection heat transfer. |
A. | Grashoff |
B. | Biot |
C. | Stantan |
D. | Reynolds |
Answer» B. Biot | |
320. |
A multiple effect evaporator as compared to a single effect evaporator of the same capacity has |
A. | lower heat transfer area. |
B. | lower steam economy. |
C. | higher steam economy. |
D. | higher solute concentration in the product. |
Answer» D. higher solute concentration in the product. | |
321. |
The capacity of double-effect evaporator is less than half of the capacity of two single effects, each of which is operating over same terminal temperature difference, when the |
A. | solution has an elevation of boiling point. |
B. | evaporators operate under vacuum. |
C. | evaporators opreate at atmospheric pressure. |
D. | none of these. |
Answer» B. evaporators operate under vacuum. | |
322. |
The ratio of momentum diffusivity to thermal diffusivity is the __________ number. |
A. | Prandtl |
B. | Nusselt |
C. | Stanton |
D. | Grashoff |
Answer» B. Nusselt | |
323. |
A __________ surface has the maximum thermal emissivity out of the following. |
A. | black & smooth |
B. | black & rough |
C. | white & smooth |
D. | white & rough |
Answer» C. white & smooth | |
324. |
The thickness of condensate layer in filmwise condensation depends on the |
A. | condensation rate |
B. | surface configuration |
C. | liquid flow rate from the surface |
D. | all (a), (b) and (c) |
Answer» E. | |
325. |
If air (a non-condensing gas) is present in a condensing vapor stream, it will __________ the condensation rate of vapor. |
A. | increase |
B. | decrease |
C. | not affect |
D. | increase the condensing film co-efficient as well as |
Answer» C. not affect | |
326. |
LMTD for counterflow and prallel flow heat exchanger will be the same, when the |
A. | cold fluid is heated to a certain temperature by condensing steam (isothermal fluid). |
B. | outlent temperature of both the hot and cold fluid are same. |
C. | outlet temperature of hot fluid is less than the outlet temperature of the cold fluid. |
D. | none of these. |
Answer» B. outlent temperature of both the hot and cold fluid are same. | |
327. |
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. | |
328. |
In pipe flow, heat is transferred from hot wall to the liquid by |
A. | conduction only. |
B. | forced convection only. |
C. | forced convection and conduction. |
D. | free and forced convection. |
Answer» D. free and forced convection. | |
329. |
Which is the most suitable for the concentration of foamy & frothy liquors ? |
A. | Agitated film evaporator |
B. | Long tube vertical evaporator |
C. | Open pan evaporator |
D. | None of these |
Answer» C. Open pan evaporator | |
330. |
Forced circulation evaporators are useful for the concentration of viscous, salting and scale forming liquors. Which of the following is a forced circulation evaporator? |
A. | Long vertical evaporator |
B. | Horizontal tube evaporator |
C. | Agitated film evaporator |
D. | Calenderia vertical tube evaporator |
Answer» D. Calenderia vertical tube evaporator | |
331. |
In a shell and tube heat exchanger, the height of 25 percent cut baffles is equal to (where, D = inside diameter of shell) |
A. | 0.25 D |
B. | 0.75 D |
C. | 0.50 D |
D. | none of these |
Answer» C. 0.50 D | |
332. |
Multipass heat exchangers are used |
A. | because of simplicity of fabrication. |
B. | for low heat load. |
C. | to obtain higher heat transfer co-efficient and shorter tube. |
D. | to reduce the pressure drop. |
Answer» D. to reduce the pressure drop. | |
333. |
is termed as the __________ number. |
A. | Grashoff |
B. | Nusselt |
C. | Prandtl |
D. | Stanton |
Answer» D. Stanton | |
334. |
The local surface conductance for laminar film condensation on vertical surface is (where, t = film thickness) |
A. | ‚àù t |
B. | ‚àù 1/t |
C. | ‚àù t |
D. | independent of 't' |
Answer» C. ‚àù t | |
335. |
A black body does not __________ radiation. |
A. | absorb or emit |
B. | refract |
C. | reflect |
D. | both(b) & (c) |
Answer» E. | |
336. |
Which of the following situations can be approximated to a steady state heat transfer system ? |
A. | A red hot steel slab (having outside surface temperature as 1300°C) exposed to the atmosheric air at 35°C. |
B. | 10 kg of dry saturated steam at 8 kgf/cm2 flowing through a short length of stainless steel pipe exposed to atmospheric air at 35°C. |
C. | Boiling brine kept in open vessel when the bottom surface temperature of the vessel is maintained constant at 180°C. |
D. | A sub-cooled refrigerant liquid at 8°C flowing at the rate of 6 Kg/minute through a copper pipe exposed to atmospheric air at 35°C. |
Answer» C. Boiling brine kept in open vessel when the bottom surface temperature of the vessel is maintained constant at 180¬∞C. | |
337. |
A cube, sphere & a thin circular plate (all having same mass and made of same material) are all heated to 300°C and allowed to cool in natural air. Which one will cool the slowest ?$ |
A. | Cube |
B. | Plate |
C. | Sphere |
D. | All will cool at the same rate |
Answer» D. All will cool at the same rate | |
338. |
The range of electromagnetic spectrum important in heat transfer by radiation is __________ microns. |
A. | 0.38-0.78 |
B. | 0.5-50 |
C. | 100-1000 |
D. | 18384 |
Answer» C. 100-1000 | |
339. |
During crystallisation, formation of crystal can occur in __________ solution only. |
A. | saturated |
B. | supersaturated |
C. | undersaturated |
D. | all (a), (b) and (c) |
Answer» C. undersaturated | |
340. |
The main function of baffles provided in a shell and tube heat exchanger is to |
A. | facilitate the cleaning of outer tube surface. |
B. | enhance turbulence. |
C. | hold the tubes in position. |
D. | all 'a', 'b' & 'c'. |
Answer» C. hold the tubes in position. | |
341. |
Corrosiveness of steam condensate is due to the presence of |
A. | CO2 |
B. | dissolved O2 |
C. | both (a) & (b) |
D. | neither (a) nor (b) |
Answer» D. neither (a) nor (b) | |
342. |
Prandtl number is the ratio of |
A. | momentum diffusivity to mass diffusivity. |
B. | momentum diffusivity to thermal diffusivity. |
C. | thermal diffusivity to mass diffusivity. |
D. | thermal diffusivity to momentum diffusivity. |
Answer» C. thermal diffusivity to mass diffusivity. | |
343. |
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 | |
344. |
Asymptotic conditions is reached, when for a fluid flowing in laminar flow through a long tube |
A. | exit-fluid temperature > wall temperature. |
B. | exit fluid temperature < wall temperature. |
C. | exit fluid temperature = wall temperature. |
D. | Graetz number > 100. |
Answer» D. Graetz number > 100. | |
345. |
Heat transfer rate described by Fourier's law will decrease, if the __________ increases. |
A. | thermal conductivity |
B. | thickness |
C. | temperature difference |
D. | heat transfer area |
Answer» C. temperature difference | |
346. |
The overall resistance for heat transfer through a series of flat resistance, is the __________ of the resistances. |
A. | average |
B. | geometric mean |
C. | product |
D. | sum |
Answer» E. | |
347. |
What is the geometric mean of two heat transfer areas A1 and A2 ? |
A. | A1 . A2 |
B. | A1 + A2 |
C. | A1 . A2 |
D. | 2 A1 . A2 |
Answer» B. A1 + A2 | |
348. |
Reynold's analogy states that (where, St = Stanton number f = friction factor) |
A. | |
B. | |
Answer» B. | |
349. |
The actual temperature drop across the heating surface of an evaporator depends on the |
A. | liquid depth over the heating surface. |
B. | solution being evaporated. |
C. | pressure difference between the steam chest and the vapor space above the boiling liquid. |
D. | all (a), (b) and (c) |
Answer» E. | |
350. |
LMTD correction factor which is to be applied for a cross-flow heat exchanger increases with increase in the number of shell passes. Its value for a single pass cross flow heat exchanger is |
A. | 0 |
B. | 1 |
C. | >1 |
D. | <1 |
Answer» E. | |