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Process Equipment and Plant Design

Process Equipment and Plant Design
In common bubble cap distillation column design practice, riser area is approximately equal to (where, Aa = Annular passage area, and Sa = Slot area)

Aa = 1.5 Sa
Sa = 1.5 Aa
1.2 Aa = 1.2 Sa
Aa = Sa

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Process Equipment and Plant Design
Column support for the roof of cylindrical storage tank must be provided for

Large diameter tanks
Small diameter tanks
Small diameter tall tanks
All of these

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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)

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

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Process Equipment and Plant Design
With increase in the reflux ratio for a fixed production from a continuous binary distillation column, the __________ decreases.

Vapour & liquid load both
Running cost of steam for reboiler
Fixed charges initially
Running cost of cooling water for condenser

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Process Equipment and Plant Design
For a given design of bubble cap, the number of bubble caps to be used per tray is set by the

Allowable gas velocity through the slots
Plate spacing
Diameter of the column
All of these

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Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

1/D⁵
1/D²
1/D
D²

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