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Process Equipment and Plant Design

Process Equipment and Plant Design
Brass valves are usually made for pipe sizes __________ inches.

>2.5
?1
?2
>3.5

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Process Equipment and Plant Design
Le/D for a Tee (used as elbow, entering run) would be around

60
5
350
200

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Process Equipment and Plant Design
In the downcomer of a distillation column, the minimum recommended residence time is about __________ seconds.

12.5
5
17.5
2.5

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Process Equipment and Plant Design
Which of the following is not a graphical method (but is an analytical method) for the calculation of theoretical number of stages in case of continuous binary distillation?

McCabe-Thiele's method
Ponchon-Savarit method
None of these
Sorel-Lewis method

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

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Process Equipment and Plant Design
Theoretically calculated diameter of the stripping section of the continuous rectification column is __________ that of the enriching section.

More than
Less than
Either more or less (depending upon relative volatility)
Same as

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