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Process Equipment and Plant Design

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

200
350
5
60

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

Density of the fluid
Viscosity of the fluid
None of these
Total cost considerations (pumping cost plus fixed cost of the pipe)

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Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Thick walled tall
Tall but empty
Small
Large horizontal cylindrical

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Process Equipment and Plant Design
Corrosion allowance in the design of pressure vessel/chemical equipment is not necessary, if

Both B & C
Plain carbon steel and cast iron parts are used
Wall thickness is > 30 mm
Material of construction is high alloy steel

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Process Equipment and Plant Design
Equivalent diameter for heat transfer calculation for a duct of square cross-section having each side as 'd' will be

√(2d)
D
√d
√(2πd)

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Multipass shell and tube heat exchanger
Counter flow of hot and cold fluids
Double pipe heat exchanger
Fouling fluids

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