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Process Equipment and Plant Design

Process Equipment and Plant Design
The difficulty of liquid distribution in packed towers is accentuated, when the ratio of tower diameter to packing diameter is

> 20 < 50
< 30
> 7 < 15
< 7

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Process Equipment and Plant Design
Any shell opening greater than 5 cms for a storage tank must be reinforced for reason of

Making the joint leak proof
None of these
Preventing the local overstressing of the shell around the opening
Reduction of discontinuity in shape at the junction

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Process Equipment and Plant Design
The ratio of down take area to cross-sectional area of the tube, for calendria type evaporator ranges from

1.5 to 2
2 to 2.5
1 to 1.5
0.5 to 1

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Process Equipment and Plant Design
Corrosion allowance in the design of pressure vessel/chemical equipment is not necessary, if

Both B & C
Wall thickness is > 30 mm
Material of construction is high alloy steel
Plain carbon steel and cast iron parts are used

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Process Equipment and Plant Design
Which tube arrangement in a heat exchanger would facilitate highest heat transfer rate?

Triangular pitch
Diagonal square pitch
Square pitch
Heat transfer rate is independent of tube arrangement

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Process Equipment and Plant Design
Rivets are generally specified by the

Shank diameter
Overall length
Head diameter
None of these

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