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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffle spacing is generally __________ the I.D. of the shell.

More than
Not greater than
Both B and C
Not less than one fifth of

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Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

0.5-0.65
0.60-0.90
0.75-0.85
0.15-030

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Process Equipment and Plant Design
The ends of a cylinderical vessel can be closed by a head, which can be one of the four shapes. For the same thickness, choose the one which can withstand the highest pressure.

Torispherical
Flat plate
Hemispherical
Ellipsoidal

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Process Equipment and Plant Design
The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per metre height of packing.

1000-1500
100-150
43835
20-40

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Process Equipment and Plant Design
An underdesigned steam trap will

None of these
Destroy itself of acceleration wear due to rapid recycling
Back up condensate and cause water hammer in steam line
Waste steam

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Process Equipment and Plant Design
Floating head heat exchangers are used for the

Cases where temperature difference between the shell and the tubes is more (>50°C)
Co-current heat transfer systems
Counter-current heat transfer systems
Heat transfer between corrosive fluids

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