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Process Equipment and Plant Design

Process Equipment and Plant Design
Normally, the length to diameter ratio of rotary dryers varies form 4 to 10 and for its economic operation, the number of transfer units (NTU) for such dryers varies from

1.5-2.5
44119
3.5-5.5
7.5-10.0

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Process Equipment and Plant Design
Baffles may be eliminated for

High viscosity liquids (> 600 poise)
None of these
Low viscosity liquids (< 200 poise)
Large diameter tanks

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Process Equipment and Plant Design
In a shell and tube heat exchanger having square pitch, the shell side equivalent diameter is given by (where, P = pitch, d = outside diameter of the tube)

(P² - πd²/4)/πd
Πd/4P²
4P²/πd
4(P² - πd²/4)/πd

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Process Equipment and Plant Design
In the allocated cap area, bubble caps are generally arranged on equilateral triangular pitch. Number of caps fixed on a plate is with a

Cap pitch of 1.3-2 times the cap diameter
Neither A nor B
Clearance of 25-75 mm
Either A or B

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Process Equipment and Plant Design
__________ dished head is the strongest of all.

None of these
Torispherical
Hemispherical
Elliptical

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Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

L to 3
3 to 12.5
12.5 to 18.5
4 to 8

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