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

8

2

1/2

4

8

2

1/2

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

Approximate

None of these

Inner

Outer

Approximate

None of these

Inner

Outer

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Process Equipment and Plant Design
Lug support is

All of these

Provided usually for vessels of much smaller height than skirt supported vessels

The most suitable for thick vertical vessel

Same as bracket support

All of these

Provided usually for vessels of much smaller height than skirt supported vessels

The most suitable for thick vertical vessel

Same as bracket support

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Process Equipment and Plant Design
In a shell and tube heat exchanger, tube side __________ of the mass velocity.

Pressure drop is proportional to the square

Heat transfer co-efficient is proportional to 0.8th power

Both A & B

Neither A nor B

Pressure drop is proportional to the square

Heat transfer co-efficient is proportional to 0.8th power

Both A & B

Neither A nor B

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Process Equipment and Plant Design
Le/D for a Tee (used as elbow, entering run) would be around

60

5

200

350

60

5

200

350

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Process Equipment and Plant Design
Two iron pipes of the same nominal diameter but different schedule numbers will have the same

Inside diameter

Wall thickness

Outside diameter

None of these

Inside diameter

Wall thickness

Outside diameter

None of these

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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 Nominal size of a pipe is an indication of its __________ diameter.

Process Equipment and Plant Design Lug support is

Process Equipment and Plant Design In a shell and tube heat exchanger, tube side __________ of the mass velocity.

Process Equipment and Plant Design Le/D for a Tee (used as elbow, entering run) would be around

Process Equipment and Plant Design Two iron pipes of the same nominal diameter but different schedule numbers will have the same

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
Nominal size of a pipe is an indication of its __________ diameter.

Process Equipment and Plant Design
Lug support is

Process Equipment and Plant Design
In a shell and tube heat exchanger, tube side __________ of the mass velocity.

Process Equipment and Plant Design
Le/D for a Tee (used as elbow, entering run) would be around

Process Equipment and Plant Design
Two iron pipes of the same nominal diameter but different schedule numbers will have the same