Vertical vessels are not supported by

Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets

Skirts

Columns

Saddles

Brackets

Skirts

Columns

Saddles

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Process Equipment and Plant Design
Le/D for fully open gate valves would be

Both B and C

Much more than that for fully open globe valves

Much less (say 2% than that for fully open globe valves)

Around 7

Both B and C

Much more than that for fully open globe valves

Much less (say 2% than that for fully open globe valves)

Around 7

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Process Equipment and Plant Design
In the design of a shell and tube heat exchanger, the corrosion allowance

For carbon steel and cast iron pressure parts is 1.5 mm (except for tubes) and for severe conditions it is 3 mm

All of these

For internal cover and tube sheet is provided on both the sides

Need not be provided for non-pressure parts like tie rods, spacers, baffles, supports etc

For carbon steel and cast iron pressure parts is 1.5 mm (except for tubes) and for severe conditions it is 3 mm

All of these

For internal cover and tube sheet is provided on both the sides

Need not be provided for non-pressure parts like tie rods, spacers, baffles, supports etc

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Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

1/D

D²

1/D²

1/D⁵

1/D

D²

1/D²

1/D⁵

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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

U-bend

Floating head tube sheet

Neither A nor B

Either A or B

U-bend

Floating head tube sheet

Neither A nor B

Either A or B

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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

1 to 1.5

2.5 to 3.5

6 to 8

4 to 5

1 to 1.5

2.5 to 3.5

6 to 8

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Process Equipment and Plant Design

Process Equipment and Plant Design Vertical vessels are not supported by

Process Equipment and Plant Design Le/D for fully open gate valves would be

Process Equipment and Plant Design In the design of a shell and tube heat exchanger, the corrosion allowance

Process Equipment and Plant Design For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

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

Process Equipment and Plant Design
Vertical vessels are not supported by

Process Equipment and Plant Design
Le/D for fully open gate valves would be

Process Equipment and Plant Design
In the design of a shell and tube heat exchanger, the corrosion allowance

Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

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