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Process Equipment and Plant Design

Process Equipment and Plant Design
Speed of industrial paddle agitator ranges from __________ rpm.

500 to 750
1000 to 2000
20 to 100
1 to 5

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Process Equipment and Plant Design
In actual operation of a bubble cap distillation tower, the __________ at the bottom of the tower is more than that at the top of the tower.

Vapour molecular weight
All of these
Molal flow rate of vapour
Pressure and temperature

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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
McCabe-Thiele's method
Sorel-Lewis method

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Process Equipment and Plant Design
Saddle supports are used for supporting __________ vessels.

Tall vertical
Thick spherical
Horizontal cylinderical
Thick walled vertical

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Process Equipment and Plant Design
The LMTD correction factor (FT) is applied in __________ heat exchangers.

Double pipe
All multipass
1-1 cocurrent
All of these

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Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the effect of L/D on inside film heat transfer co-efficient (hi) vanishes after a Reynold number of

3000
10000
5000
1000

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