chemical engineering process equipment and plant design MCQs – Page 13

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 Review each marked answer and report any item that may be outdated or unclear.

chemical engineering process equipment and plant design Mcqs
241. Shortest distance between two tubes is___________________?
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A. Called tube clearance

B. Called tube pitch

C. More in case of triangular pitch as compared to square pitch of tube layout

D. None of these

244. Rivets are generally specified by the____________________?
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A. Shank diameter

B. None of these

C. Overall length

D. Head diameter

245. Saddle supports are used for supporting _____________ vessels?
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A. Horizontal cylindrical

B. Tall vertical

C. Thick walled vertical

D. Thick spherical

247. Which of the following factors determine the amount of entrainment in a distillation column ?
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A. Plate spacing

B. Depth of liquid above the bubble cap slots

C. All A., B. and C.

D. Vapour velocity in the volume between the plates

250. A forced circulation long tube vertical evaporator as compared to the natural circulation evaporator__________________?
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A. Is economical in operation

B. Employs high velocity, high heat transfer rate and less heating surface requirement

C. Employs a centrifugal pump placed between external downtake from vapor drum and inlet to

D. e bundle

E. Both B. & C.
252. Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is____________?
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A. More

B. Same

C. More or less depending upon the pressure & temperature inside the vessel and the nature of

D. Less

E. fluid contained therein

254. In a vertical short tube evaporator (Calandria type), the ______________________?
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A. All A., B. & C.

B. mally used

C. Tube dia of 2.5-7.5 cms, tube length of 75-200 cms and cylindrical drum dia of 1-6 metres are

D. rounding tube

E. Liquor is inside the tube while the steam is outside the tube

F. Area of central downtake is equal to 40 to 100% of total cross-sectional area of the