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Process Equipment and Plant Design

Process Equipment and Plant Design
For storing hazardous chemicals in large storage tanks, the minimum safe distance between the two tanks should range between __________ times the tank diameter.

4 to 5
6 to 8
2.5 to 3.5
1 to 1.5

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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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Process Equipment and Plant Design
If 'D' is the inside diameter of the shell of a shell and tube heat exchanger, then the baffle spacing is usually in the range of

D/5 or minimum 2" to D
None of these
D/2 or minimum 2" to 5D
D/5 or minimum 2" to 5D

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Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

None of these
Bubble cap plate
Packed
Sieve plate

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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.

Valve
Bubble cap
Sieve
Counterflow

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Process Equipment and Plant Design
Which of the following is used to set the diameter of the distillation column?

Number of theorectical plates
Allowable vapour velocity
Static submergence
Length of straight rectangular weir on cross-flow tray

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