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Process Equipment and Plant Design - Section 1 (4)

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  • Process Equipment and Plant Design - Section 1
Directions to Solve

Process Equipment and Plant Design - Section 1

There are many MCQs available for this field and
you will find them in this section. You can solve them easily without any problem.

25. 

In a multipass shell and tube heat exchanger, the shell side cross flow area does not depend upon

A. baffle spacing
B. clearance
C. pitch
D. none of these

Answer: Option D

Explanation:

No answer description available for this question. Let us discuss.

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26. 

Bracket supports are the most suitable for supporting __________ vessels.

A. thick walled vertical
B. horizontal
C. thin shperical (e.g. Horton sphere)
D. none of these

Answer: Option A

Explanation:

No answer description available for this question. Let us discuss.

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27. 

Triangular pitch tube layout as compared to square pitch in a shell and tube heat exchanger

A. permits the use of less tubes in a given shell diameter.
B. facilitates comparatively easier external cleaning because of large clearance.
C. permits the use of more tubes in a given shell diameter.
D. both (b) and (c).

Answer: Option C

Explanation:

No answer description available for this question. Let us discuss.

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28. 

A rivetted joint does not fail by __________ of rivets.

A. tearing
B. shearing
C. tearing of the plate across a row
D. none of these

Answer: Option D

Explanation:

No answer description available for this question. Let us discuss.

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29. 

It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

A. 0.99
B. 0.95
C. 0.80
D. 0.55

Answer: Option C

Explanation:

No answer description available for this question. Let us discuss.

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30. 

Where does the maximum tensile strength occur in a thick cylindrical vessel subjected to internal pressure ?

A. At the inner surface.
B. At the mid thickness of the cylindrical wall.
C. At the outer surface.
D. None of these.

Answer: Option A

Explanation:

No answer description available for this question. Let us discuss.

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31. 

In a heat exchanger, shell side fluid velocity can be changed by changing the tube

A. layout
B. pitch
C. both (a) & (b)
D. neither (a) nor (b)

Answer: Option C

Explanation:

No answer description available for this question. Let us discuss.

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32. 

To keep the power input constant for a stirred vessel operating under fully developed turbulent flow conditions (constant power number), if the impeller diameter is increased by 20%, the impeller speed should be decreased by a factor of

A. (1.2)3/2
B. (1.2)3/5
C. (1.2)2/3
D. (1.2)5/3

Answer: Option D

Explanation:

No answer description available for this question. Let us discuss.

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