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Process Equipment and Plant Design

Process Equipment and Plant Design
In case of saddle packing (e.g., berl and intralox saddles), the maximum size of the packing should not exceed __________ of the column diameter.

l/30th
l/15th
l/50th
l/5th

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Process Equipment and Plant Design
Rotary driers are most economically designed for the number of heat transfer units (HTU) from

10 to 20
5 to 10
1.5 to 2.5
0.01 to 1

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Process Equipment and Plant Design
A pipe is generally made of circular cross-section, because a circular cross-section has the

Higher structural strength
Both A & B
Lowest surface area requirement for a given volume
None of these

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Process Equipment and Plant Design
Spherical shaped pressure vessel is considered to be the most ideal, because it can

Be fabricated very easily
Be designed without wind load considerations
Be supported very easily
Withstand higher pressure for a given metallic shell thickness

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Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Tall but empty
Thick walled tall
Large horizontal cylindrical
Small

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Process Equipment and Plant Design
Log mean temperature difference in case of multi-pass shell and tube heat exchanger is always

Less than arithmetic mean value
More than geometric mean value
Both B & C
More than arithmetic mean value

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