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Process Equipment and Plant Design

Process Equipment and Plant Design
Height of the flights in the rotary drier is in the range of

0.2 to 0.5 d
0.5 to 0.6 d
0.08 to 0.12 d
0.02 to 0.05 d

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Process Equipment and Plant Design
Which of the following factors determine the amount of entrainment in a distillation column?

All of these
Plate spacing
Vapour velocity in the volume between the plates
Depth of liquid above the bubble cap slots

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Process Equipment and Plant Design
Length to diameter ratio of most rotary driers is in the range of

1 to 2
20 to 30
10 to 20
4 to 10

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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?

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

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Process Equipment and Plant Design
Minimum baffle spacing recommended in a shell and tube heat exchanger is equal to

40% of the I.D. of the shell
I.D. of the shell
25 cms
5 cms

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Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

None of these
Bubble cap plate
Sieve plate
Packed

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