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Process Equipment and Plant Design

Process Equipment and Plant Design
Movement of pipeline caused by thermal expansion is taken care by providing

All of these
Change in the shape of pipeline
Changes in its direction
Expansion joint

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Process Equipment and Plant Design
The approximate liquid depth in an agitation tank is equal to (where, d = tank diameter)

0.5 d
0.75 d
D
2 d

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

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Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.95
0.75
0.85
0.55

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Process Equipment and Plant Design
Needle valves are generally not used for

Smaller sizes of pipe
Very large diameter pipes
Very accurate flow control
High pressure throttling service

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Process Equipment and Plant Design
A perforated plate has holes of diameter dh arranged in a pitch ph. Each hole has a tube of I.D. dt passing through it. The ligament efficiency is given by

(ph - dh . dt/2)/ph
(ph - dh)/dh
(ph - dh)/ph
(ph - dt)/ph

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