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Process Equipment and Plant Design

Process Equipment and Plant Design
Friction factor for turbulent flow in a new pipe is given by

f = 0.22 NRe0.05
f = 25/NRe
f = 0.04/NRe0.16
f = 16/NRe

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Process Equipment and Plant Design
Any shell opening greater than 5 cms for a storage tank must be reinforced for reason of

None of these
Preventing the local overstressing of the shell around the opening
Making the joint leak proof
Reduction of discontinuity in shape at the junction

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Process Equipment and Plant Design
Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.

10 to 15
1.5 to 2
5 to 10
2.5 to 5

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

43833
0.07 - 0.12
0.5 - 1.0
0.01 - 0.5

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Process Equipment and Plant Design
Most of the storage vessels/tanks are made cylindrical, because of the fact that a cylinder

Is easy to fabricate
Both A & B
Has greater structural strength
Neither A nor B

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

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

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