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Process Equipment and Plant Design

Process Equipment and Plant Design
Rivets are generally specified by the

Shank diameter
None of these
Overall length
Head diameter

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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

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

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Disk and ring
Independent of the type of
Orifice
Segmental

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Process Equipment and Plant Design
In a __________ rivetted joint, the rivets in the various rows are opposite to each other.

None of these
Zig-zag
Chain
Diamond

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the shortest centre to centre distance between the adjacent tubes is

None of these
Called tube pitch
Called tube clearance
Always less than the diameter of the tube

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Process Equipment and Plant Design
Maximum acceptable total liquid gradient over a tray is about __________ mm.

30.5
12.5
45.5
5.5

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