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Process Equipment and Plant Design

Process Equipment and Plant Design
To avoid the tearing off the plate of an edge, the margin (i.e., the minimum distance from the centre of the rivet hole to the nearest edge of the plate) should be equal to

2.5 d
0.5 d
1.5 d
D

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Process Equipment and Plant Design
In a shell and tube heat exchanger having triangular pitch, the shell side equivalent diameter is given by

4(0.86p² - πd²/4)/πd
(p² - πd²/4)/πd
4(0.86p² - πd²)/πd
(4p² - πd²/4)/πd

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

None of these
Density of the fluid
Viscosity of the fluid
Total cost considerations (pumping cost plus fixed cost of the pipe)

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Process Equipment and Plant Design
for couplings and unions would be

60
Negligible
200
350

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Process Equipment and Plant Design
In case of bubble cap distillation column of diameter greater than 1.2 metres, the cap diameter is roughly about __________ cms.

10
30
35
20

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Process Equipment and Plant Design
A high vapour velocity is required for high plate efficiency in a seive plate coloumn. The satisfactory value of operating vapor velocity for design purpose in seive plate column is about __________ percent of the flooding velocity.

45
95
80
60

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