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.

2

8

4

1/2

2

8

4

1/2

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Process Equipment and Plant Design
Liquid gradient over the tray results due to the

Large plate spacing

Large reflux ratio

Resistance offered to flow of liquids by caps & risers and the flow of gas

Low gas velocity

Large plate spacing

Large reflux ratio

Resistance offered to flow of liquids by caps & risers and the flow of gas

Low gas velocity

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

Neither A nor B

Either A or B

U-bend

Floating head tube sheet

Neither A nor B

Either A or B

U-bend

Floating head tube sheet

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Process Equipment and Plant Design
Pressure differential maintained across a continuous rotary vacuum filter is in the range of __________ mm Hg column.

100 to 150

250 to 500

50 to 100

600 to 700

100 to 150

250 to 500

50 to 100

600 to 700

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Process Equipment and Plant Design
Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.

2.5 to 5

5 to 10

1.5 to 2

10 to 15

2.5 to 5

5 to 10

1.5 to 2

10 to 15

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Process Equipment and Plant Design
Normal screwed fittings are used for pipes upto a diameter of __________ inches.

3

1.5

7

5

3

1.5

7

5

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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 Liquid gradient over the tray results due to the

Process Equipment and Plant Design In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

Process Equipment and Plant Design Pressure differential maintained across a continuous rotary vacuum filter is in the range of __________ mm Hg column.

Process Equipment and Plant Design Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.

Process Equipment and Plant Design Normal screwed fittings are used for pipes upto a diameter of __________ inches.

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
Liquid gradient over the tray results due to the

Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

Process Equipment and Plant Design
Pressure differential maintained across a continuous rotary vacuum filter is in the range of __________ mm Hg column.

Process Equipment and Plant Design
Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.

Process Equipment and Plant Design
Normal screwed fittings are used for pipes upto a diameter of __________ inches.