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Process Equipment and Plant Design

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

>3.5
>2.5
?2
?1

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design
Pressure drop per tray in the atmospheric distillation column is about __________ psi.

0.5 - 1.0
0.01 - 0.5
43833
0.07 - 0.12

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Process Equipment and Plant Design
The average velocity in the tubes of a 1-4 heat exchanger is __________ times that in 1-1 heat exchanger having the same size & number of tubes and operated at same liquid flow rate.

43834
2
4
43832

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Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

0.1-0.2
1.2-1.5
0.4-0.9
0.2-0.5

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Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

3.5
2.5
1.75
1.25

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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?

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

ANSWER DOWNLOAD EXAMIANS APP
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