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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.
551. |
Heat produced when a steady state current, I passes through an electrical conductor having resistance, 'R' is |
A. | IR |
B. | I2R |
C. | IR2 |
D. | I2R2 |
Answer» C. IR2 | |
552. |
Three solid objects of the same material and of equal mass-a sphere, a cylinder (length = diameter) and a cube are at 500°C initially. These are dropped in a quenching bath containing a large volume of cooling oil each attaining the bath temperature eventually. The time required for 90% change in temperature is the smallest for |
A. | cube |
B. | cylinder |
C. | sphere |
D. | equal for all the three |
Answer» B. cylinder | |
553. |
'Fouling factor' used in the design of a multipass shell and tube heat exchanger is a |
A. | non-dimensional factor. |
B. | factor of safety. |
C. | conversion factor for individual film heat transfer co-efficient to overall heat transfer co-efficient. |
D. | none of these. |
Answer» C. conversion factor for individual film heat transfer co-efficient to overall heat transfer co-efficient. | |
554. |
jH factor for heat transfer is not a function of the __________ number. |
A. | Reynolds |
B. | Nusselt |
C. | Grashoff |
D. | both (b) & (c) |
Answer» E. | |
555. |
A backward feed multiple effect evaporator is better than forward feed for concentrating cold feed, because it provides |
A. | higher economy |
B. | lower capacity |
C. | both (a) & (b) |
D. | lower economy |
Answer» B. lower capacity | |
556. |
For large heat transfer area requirement, shell and tube heat exchanger is preferred, because it |
A. | occupies smaller space. |
B. | is more economical. |
C. | is easy to operate and maintain. |
D. | all (a), (b) and (c). |
Answer» E. | |
557. |
In the equation Q = UAΔt; Δt is |
A. | geometric mean temperature difference. |
B. | arithmetic mean temperature difference. |
C. | logarithmic mean temperature difference. |
D. | the difference of average bulk temperatures of hot and cold fluids. |
Answer» D. the difference of average bulk temperatures of hot and cold fluids. | |
558. |
Nucleate boiling is promoted |
A. | on polished surfaces |
B. | on rough surfaces |
C. | in the absence of agitation |
D. | none of these |
Answer» C. in the absence of agitation | |
559. |
Water is normally used as a coolant in the heat exchange equipments mainly because ofits |
A. | abundance & high heat capacity |
B. | low density |
C. | low viscosity |
D. | high fluidity |
Answer» B. low density | |
560. |
Controlling heat transfer film co-efficient is the one, which offers __________ resistance to heat transfer. |
A. | no |
B. | the least |
C. | the largest |
D. | lower |
Answer» D. lower | |
561. |
If the thermal conductivity of a wall material is independent of temperature, the steady state temperature distribution in the very large thin plane wall having steady, uniform surface temperature follows __________ law. |
A. | hyperbolic |
B. | parabolic |
C. | linear |
D. | logarithmic |
Answer» D. logarithmic | |
562. |
Multiple effect evaporators ar used to |
A. | increase the steam economy & decrease the capacity. |
B. | increase the steam economy & the capacity. |
C. | decrease the steam economy & the capacity. |
D. | decrease the steam economy & increase the capacity. |
Answer» C. decrease the steam economy & the capacity. | |
563. |
Kg of liquid evaporated per hour in an evaporator is defined as its |
A. | capacity |
B. | economy |
C. | steam load |
D. | none of these |
Answer» B. economy | |
564. |
The Graetz number is concerned with the |
A. | mass transfer between a gas and a liquid. |
B. | absorption with chemical reaction. |
C. | heat transfer in turbulent flow. |
D. | heat transfer in laminar flow. |
Answer» E. | |
565. |
A 2-4 heat exchanger involves |
A. | only counter-flow of fluids. |
B. | only parallel-flow of fluids. |
C. | both counter and parallel-flow of the fluids. |
D. | smaller pressure drop compared to 1-2 exchanger. |
Answer» D. smaller pressure drop compared to 1-2 exchanger. | |
566. |
Presence of a non-condensing gas in a condensing vapour |
A. | increases the rate of condensation. |
B. | decreases thermal resistance. |
C. | is desirable to increase the film co-efficient. |
D. | none of these. |
Answer» E. | |
567. |
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¬∞C | |
568. |
In SI units, fouling factor is expressed in |
A. | m2°K/W |
B. | W/m2°K |
C. | m2°K |
D. | m°K/W |
Answer» B. W/m2¬∞K | |
569. |
Boiling of milk in an open vessel is an example of __________ boiling. |
A. | film |
B. | sub-cooled |
C. | saturated nucleate |
D. | none of these |
Answer» B. sub-cooled | |
570. |
For an ideal black body |
A. | absorptivity = 1 |
B. | reflectivity = 1 |
C. | emissivity = 0 |
D. | transmissivity = 1 |
Answer» B. reflectivity = 1 | |
571. |
Heat transfer co-efficient (h) for a fluid flowing inside a clean pipe is given by This is valid for the value of NRe equal to |
A. | < 2100 |
B. | 2100-4000 |
C. | > 4000 |
D. | > 10000 |
Answer» E. | |
572. |
The dimensionless group in mass transfer that is equivalent to Prandtl number in heat transfer is |
A. | Nusselt number. |
B. | Sherwood number. |
C. | Schmidt number. |
D. | Stanton number. |
Answer» D. Stanton number. | |
573. |
Nusselt number is the ratio of the temperature gradient at the wall to |
A. | temperature difference |
B. | heat flux |
C. | that across the entire pipe |
D. | none of these |
Answer» D. none of these | |
574. |
In case of a multipass shell and tube heat exchanger, providing a baffle on the shell side __________ the heat transfer rate. |
A. | increases |
B. | decreases |
C. | does not affect |
D. | may increase or decrease, depends on the type of baffle |
Answer» B. decreases | |
575. |
The absorptivity of a grey body at a given temperature __________ with increasing wavelength of radiation. |
A. | increases |
B. | decreases |
C. | remains constant |
D. | may increase or decrease ; depends on the material |
Answer» E. | |
576. |
If average heat transfer co-efficient is ha and the local coefficient at the end of the plate is hl then in case of heat transfer to a fluid flowing over a flat plate, heated over its entire length |
A. | ha = hl |
B. | ha = 2hl |
C. | ha = 0.5 hl |
D. | ha = 0.75 hl |
Answer» C. ha = 0.5 hl | |
577. |
For concentrating an aqueous solution of a material like anhydrous Na2SO4, whose solubility decreases with rise in temperature, the most suitable evaporator is a __________ evaporator. |
A. | high pressure |
B. | vacuum |
C. | backward feed |
D. | none of these |
Answer» C. backward feed | |
578. |
The thermal efficiency of a reversible heat engine operating between two given thermal reservoirs is 0.4. The device is used either as a refrigerator or as a heat pump between the same reservoirs. Then the coefficient of performance as a refrigerator (COP)R and the co-efficient of performance as a heat pump (COP)HP are |
A. | (COP)R = (COP)HP = 0.6 |
B. | (COP)R = 2.5; (COP)HP = 1.5 |
C. | (COP)R = 1.5; (COP)HP = 2.5 |
D. | (COP)R = (COP)HP = 2.5 |
Answer» D. (COP)R = (COP)HP = 2.5 | |
579. |
For a fluid flowing in an annulus space, the wetted perimeter for heat transfer and pressure drop are |
A. | same |
B. | different |
C. | never different |
D. | linearly related |
Answer» C. never different | |
580. |
The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe whose surface temperature remains constant is |
A. | 1.66 |
B. | 88.66 |
C. | 3.66 |
D. | dependent on NRe only |
Answer» D. dependent on NRe only | |
581. |
With the increase of temperature, the Col-burn jH factor |
A. | increases. |
B. | decreases. |
C. | remains unchanged. |
D. | may increase or decrease ; depending on temperature. |
Answer» B. decreases. | |
582. |
Film boiling is usually not desired in commercial equipments, because |
A. | the heat transfer rate is low in view of the large temperature drop. |
B. | it is difficult to maintain. |
C. | it is not economic. |
D. | none of these. |
Answer» B. it is difficult to maintain. | |
583. |
A tank painted with which of the following coloured paints, would heat up maximum by radiation from sun ? |
A. | Yellow paint |
B. | White paint |
C. | Black paint |
D. | Grey paint |
Answer» D. Grey paint | |
584. |
The advantage of backward feed multiple effect evaporators over forward feed units is that |
A. | heat sensitive material can be handled. |
B. | there is no additional cost of pumping. |
C. | most concentrated liquid is at highest temperature. |
D. | equal heat transfer co-efficients exist in various effects. |
Answer» D. equal heat transfer co-efficients exist in various effects. | |
585. |
The purpose of providing expansion bellows in the shell of tubular exchanger is to |
A. | increase the heating load. |
B. | impart structural strength. |
C. | account for the uneven expansion of shell and tube bundles. |
D. | facilitate increase of shell length, if needed. |
Answer» D. facilitate increase of shell length, if needed. | |
586. |
In a heat exchanger, floating head is provided to |
A. | facilitate cleaning of the exchanger. |
B. | increase the heat transfer area. |
C. | relieve stresses caused by thermal expansion. |
D. | increase log mean temperature gradient. |
Answer» D. increase log mean temperature gradient. | |
587. |
In case of __________ boiling, the bubbles formed on a submerged hot surface get absorbed in the mass of the liquid. |
A. | nucleate |
B. | pool |
C. | low pressure |
D. | none of these |
Answer» C. low pressure | |
588. |
In a forward feed multiple effect evaporator unit |
A. | viscosity of liquid is highest in first effect. |
B. | transfer from effect to effect is done by pumps. |
C. | no pump is required to withdraw the product from the last effect. |
D. | none of these. |
Answer» E. | |
589. |
Film boiling occurs at __________ pressure. |
A. | atmospheric |
B. | sub-atmospheric |
C. | negative |
D. | very high |
Answer» E. | |
590. |
Reynold's analogy states that |
A. | Nst α f |
B. | Nst α NRe |
C. | NNu α f |
D. | NRe α f |
Answer» B. Nst Œ± NRe | |
591. |
Which one gives the monochromatic emissive power for black body radiation ? |
A. | Planck's law |
B. | Kirchhoffs law |
C. | Wien's law |
D. | Stefan-Boltzman law |
Answer» B. Kirchhoffs law | |
592. |
Bulk of the convective heat transfer resistance from a hot tube surface to the fluid flowing in it, is |
A. | in the central core of the fluid. |
B. | uniformly distributed throughout the fluid. |
C. | mainly confined to a thin film of fluid near the surface. |
D. | none of these. |
Answer» D. none of these. | |
593. |
Which is the most suitable for cold viscous feed? |
A. | Forward feed |
B. | Backward feed |
C. | Mixed feed |
D. | Parallel feed |
Answer» C. Mixed feed | |
594. |
The heat transfer co-efficient in film type condensation is __________ that for dropwise condensation. |
A. | greater than |
B. | lower than |
C. | is same as |
D. | half |
Answer» C. is same as | |
595. |
Baffles in the shell side of a shell and tube heat exchanger |
A. | increase the cross-section of the shell side liquid. |
B. | force the liquid to flow parallel to the bank. |
C. | increase the shell side heat transfer co-efficient. |
D. | decrease the shell side heat transfer co-efficient. |
Answer» D. decrease the shell side heat transfer co-efficient. | |
596. |
Grashoff number, which is defined as g . β(Ts - T∞) ρ2. L3/μ2, is proportional to the ratio of buoyancy force to __________ force. |
A. | viscous |
B. | elastic |
C. | inertial |
D. | none of these |
Answer» B. elastic | |
597. |
According to Reynolds analogy, Stanton number is equal to (where, f = Fanning friction factor) |
A. | 2f |
B. | f |
C. | f/2 |
D. | f/4 |
Answer» D. f/4 | |
598. |
Which of the following parameters of the fluid is not very important, while deciding its route in a shell and tube heat exchanger? |
A. | Corrosiveness & fouling characteristics |
B. | pressure |
C. | viscosity |
D. | density |
Answer» E. | |
599. |
For flow over a flat plate, the ratio of thermal boundary layer thickness, 'xt' and hydrodynamic boundary layer thickness 'x' is equal to (where, NPr = Prandtl number) |
A. | NPr |
B. | NPr1/3 |
C. | NPr-1 |
D. | NPr-1/3 |
Answer» C. NPr-1 | |
600. |
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 | |