The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per metre height of packing.

Process Equipment and Plant Design
The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per metre height of packing.

100-150

1000-1500

20-40

43835

100-150

1000-1500

20-40

43835

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Multipass shell and tube heat exchanger

Fouling fluids

Counter flow of hot and cold fluids

Double pipe heat exchanger

Multipass shell and tube heat exchanger

Fouling fluids

Counter flow of hot and cold fluids

Double pipe heat exchanger

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Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

Gas blowing beneath cap skit

Back trapping

Maldistribution of gas

All of these

Gas blowing beneath cap skit

Back trapping

Maldistribution of gas

All of these

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Process Equipment and Plant Design
In the design of a bag filter, the gas temperature is an important consideration, as it affects the

All of these

Gas viscosity

Fibre selection

Gas density

All of these

Gas viscosity

Fibre selection

Gas density

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Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Tall vertical

Small horizontal

Large horizontal

Thick walled

Tall vertical

Small horizontal

Large horizontal

Thick walled

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Process Equipment and Plant Design
The thickness of heat transfer plates used in the plate type heat exchanger ranges from __________ mm, pressed in a single piece provided with grooves & corrugations.

1.25 to 3.125

44055

3.5 to 7.0

0.3 to 0.8

1.25 to 3.125

44055

3.5 to 7.0

0.3 to 0.8

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Process Equipment and Plant Design

Process Equipment and Plant Design The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per metre height of packing.

Process Equipment and Plant Design LMTD correction factor is used in heat exchanger design for

Process Equipment and Plant Design Excessive liquid gradient on a tray may result in the

Process Equipment and Plant Design In the design of a bag filter, the gas temperature is an important consideration, as it affects the

Process Equipment and Plant Design Skirt support is the most suitable for supporting __________ vessels.

Process Equipment and Plant Design The thickness of heat transfer plates used in the plate type heat exchanger ranges from __________ mm, pressed in a single piece provided with grooves & corrugations.

Process Equipment and Plant Design
The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per metre height of packing.

Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

Process Equipment and Plant Design
In the design of a bag filter, the gas temperature is an important consideration, as it affects the

Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Process Equipment and Plant Design
The thickness of heat transfer plates used in the plate type heat exchanger ranges from __________ mm, pressed in a single piece provided with grooves & corrugations.