Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

Process Equipment and Plant Design
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

4

1/2

2

8

4

1/2

2

8

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Process Equipment and Plant Design
In the agitators, the power required will be changed with the increase of diameter of agitator (D) as

D²

D

D⁹

D⁵

D²

D

D⁹

D⁵

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Process Equipment and Plant Design
Saddle supports are used for supporting __________ vessels.

Thick walled vertical

Thick spherical

Tall vertical

Horizontal cylinderical

Thick walled vertical

Thick spherical

Tall vertical

Horizontal cylinderical

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Process Equipment and Plant Design
Wind load consideration in the design of a support can be neglected, when the vessel is

Tall (say 30 metres), but is full of liquid

Short (< 2 m) and housed indoor

None of these

Tall but empty

Tall (say 30 metres), but is full of liquid

Short (< 2 m) and housed indoor

None of these

Tall but empty

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Process Equipment and Plant Design
Power required for agitation depends upon the

Size of agitator & the tank

Agitator type & speed of agitation

Height & properties of the liquid

All of these

Size of agitator & the tank

Agitator type & speed of agitation

Height & properties of the liquid

All of these

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

Viscosity of the fluid

None of these

Total cost considerations (pumping cost plus fixed cost of the pipe)

Density of the fluid

Viscosity of the fluid

None of these

Total cost considerations (pumping cost plus fixed cost of the pipe)

Density of the fluid

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Process Equipment and Plant Design

Process Equipment and Plant Design Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

Process Equipment and Plant Design In the agitators, the power required will be changed with the increase of diameter of agitator (D) as

Process Equipment and Plant Design Saddle supports are used for supporting __________ vessels.

Process Equipment and Plant Design Wind load consideration in the design of a support can be neglected, when the vessel is

Process Equipment and Plant Design Power required for agitation depends upon the

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

Process Equipment and Plant Design
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

Process Equipment and Plant Design
In the agitators, the power required will be changed with the increase of diameter of agitator (D) as

Process Equipment and Plant Design
Saddle supports are used for supporting __________ vessels.

Process Equipment and Plant Design
Wind load consideration in the design of a support can be neglected, when the vessel is

Process Equipment and Plant Design
Power required for agitation depends upon the

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