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Process Equipment and Plant Design

Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.99
0.55
0.8
0.95

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Process Equipment and Plant Design
Two iron pipes of the same nominal diameter but different schedule numbers will have the same

Outside diameter
None of these
Wall thickness
Inside diameter

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Process Equipment and Plant Design
Cylinderical shell thickness of rotary drier is generally __________ mm.

43864
44180
43990
18-22

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Process Equipment and Plant Design
The main purpose of providing stepping on the trays is to

Facilitate handling of large flow rate of liquid
Decrease the pressure drop
Increase the residence time
Improve the flow condition

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Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

All of these
Back trapping
Gas blowing beneath cap skit
Maldistribution of gas

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Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Large horizontal
Small horizontal
Tall vertical
Thick walled

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