At the following point for a given packing and set of fluids, the pressure drop per metre of packed height, with variation in fluid rates and operating pressure

Process Equipment and Plant Design
At the following point for a given packing and set of fluids, the pressure drop per metre of packed height, with variation in fluid rates and operating pressure

Decreases

Increases

May increase or decrease depending upon the solubility of the gas in the liquid

Remains same

Decreases

Increases

May increase or decrease depending upon the solubility of the gas in the liquid

Remains same

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Process Equipment and Plant Design
The approximate liquid depth in an agitation tank is equal to (where, d = tank diameter)

D

0.5 d

0.75 d

2 d

D

0.5 d

0.75 d

2 d

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Process Equipment and Plant Design
Nominal size of a pipe is an indication of its __________ diameter.

Inner

Approximate

None of these

Outer

Inner

Approximate

None of these

Outer

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Process Equipment and Plant Design
Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.

15-20

10-12.5

5-7.5

2.5-3.0

15-20

10-12.5

5-7.5

2.5-3.0

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Process Equipment and Plant Design
Optimum reflux ratio in a continuous distillation column is determined by the

None of these

Flooding limit of the column

Total cost consideration (fixed cost of the column plus the cooling water & steam cost)

Maximum permissible vapour velocity

None of these

Flooding limit of the column

Total cost consideration (fixed cost of the column plus the cooling water & steam cost)

Maximum permissible vapour velocity

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Process Equipment and Plant Design
High pressure fluid in a shell and tube heat exchanger should preferably be routed through the

Shell side for smaller total pressure drop

Tubes to avoid the expansion of high pressure shell construction

Shell side, if the flow is counter-current and tube side if the flow is co-current

Shell side for large overall heat transfer co-efficient

Shell side for smaller total pressure drop

Tubes to avoid the expansion of high pressure shell construction

Shell side, if the flow is counter-current and tube side if the flow is co-current

Shell side for large overall heat transfer co-efficient

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Process Equipment and Plant Design

Process Equipment and Plant Design At the following point for a given packing and set of fluids, the pressure drop per metre of packed height, with variation in fluid rates and operating pressure

Process Equipment and Plant Design The approximate liquid depth in an agitation tank is equal to (where, d = tank diameter)

Process Equipment and Plant Design Nominal size of a pipe is an indication of its __________ diameter.

Process Equipment and Plant Design Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.

Process Equipment and Plant Design Optimum reflux ratio in a continuous distillation column is determined by the

Process Equipment and Plant Design High pressure fluid in a shell and tube heat exchanger should preferably be routed through the

Process Equipment and Plant Design
At the following point for a given packing and set of fluids, the pressure drop per metre of packed height, with variation in fluid rates and operating pressure

Process Equipment and Plant Design
The approximate liquid depth in an agitation tank is equal to (where, d = tank diameter)

Process Equipment and Plant Design
Nominal size of a pipe is an indication of its __________ diameter.

Process Equipment and Plant Design
Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.

Process Equipment and Plant Design
Optimum reflux ratio in a continuous distillation column is determined by the

Process Equipment and Plant Design
High pressure fluid in a shell and tube heat exchanger should preferably be routed through the