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Process Equipment and Plant Design

Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

0.60-0.90
0.5-0.65
0.75-0.85
0.15-030

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

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

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

0.5 - 1.0
43833
0.01 - 0.5
0.07 - 0.12

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Process Equipment and Plant Design
Value of Peclet number = ∞, is the representative of

Laminar flow
Plug flow
Complete back mixing
Eddy diffusivity = 0

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Process Equipment and Plant Design
__________ dished head is the strongest of all.

Elliptical
Torispherical
Hemispherical
None of these

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Process Equipment and Plant Design
For identical operating conditions, the pressure drop over __________ tray is the highest out of the following.

Counterflow
Bubble cap
Valve
Sieve

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