chemical engineering heat transfer chemical engineering MCQs – Page 18

Practise multiple-choice questions from chemical engineering heat transfer chemical engineering for competitive examinations and subject revision. Review each marked answer and report any item that may be outdated or unclear.

chemical engineering heat transfer chemical engineering Mcqs
341. If h1 = inner film co-efficient and /h2 = outer film co-efficient, then the overall heat transfer co-efficient is________________?
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A. Always higher than h2

B. Always between h1 and h2

C. Always less than h1

D. Dependent on metal resistance

343. Low thermal conductivity of heat insulating materials is due to its_________________?
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A. High specific heat

B. Dense structure

C. High proportion of air space

D. None of these

344. Steady state one dimensional heat flow by conduction as given by Fouriers low does not assume that_______________?
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A. Constant temperature gradient exists

B. Boundary surfaces are isothermal

C. There is no internal heat generation

D. Material is anisotropic
346. Heat exchangers operating, when the asymptotic range is reached, ?
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A. None of these

B. Results in making part of the heating surface inactive

C. Provide very large heat transfer co-efficient

D. Results in abruptly increased velocity

349. Which of the following is concerned with both heat and mass transfer ?
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A. Froude number

B. Kutateladze number

C. Nusselt number

D. Lewis relationship
351. A body is called grey if the monochromatic emissivity of the body is___________________?
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A. Unity

B. Different for all wavelengths

C. Zero

D. Same for all wavelengths
354. Prandtl number is the ratio of________________?
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A. Thermal diffusivity to mass diffusivity

B. Momentum diffusivity to thermal diffusivity

C. Mass diffusivity to thermal diffusivity

D. Thermal diffusivity to momentum diffusivity

355. Which of the following is not concerned with the heat transfer ?
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A. Peclet number

B. Stanton number

C. Brinkman number

D. Schmidt number
356. In case of a multipass shell and tube heat exchanger, providing a baffle on the shell side ______________ the heat transfer rate?
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A. Decreases

B. Does not affect

C. Increases

D. May increase or decrease, depends on the type of baffle

357. Heat transfer efficiency leading of energy conservation in a heat exchanger can be achieved by____________________?
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A. Enhancing the fluid pumping rate

B. Keeping the heat transfer surface clean

C. Increasing the tube length

D. None of these

358. In a multiple effect evaporator, the effect of boiling point elevation is to______________________?
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A. Increase the economy

B. Reduce the economy

C. Reduce the capacity

D. None of these

360. Fouling factor used in the design of a multipass shell and tube heat exchanger is a_____________________?
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A. None of these

B. Conversion factor for individual film heat transfer co-efficient to overall heat transfer coefficient

C. Factor of safety

D. Non-dimensional factor