The raio, (properller agitator dia/tank dia) is normally taken as

Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

0.15-030

0.60-0.90

0.5-0.65

0.75-0.85

0.15-030

0.60-0.90

0.5-0.65

0.75-0.85

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design
The equivalent diameter for fluid flow through a channel of constant non-circular cross section of area 'A' is given by (where, P = perimeter of the channel in contact with the fluid)

4 P/A

A/P

4 A/P

√A

4 P/A

A/P

4 A/P

√A

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Independent of the type of

Orifice

Disk and ring

Segmental

Independent of the type of

Orifice

Disk and ring

Segmental

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Increases very rapidly

Increases linearly

Remains constant

Decreases very rapidly

Increases very rapidly

Increases linearly

Remains constant

Decreases very rapidly

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design
In a multiple effect evaporator system having 'n' effects, the amount of water evaporated per unit surface area in approximately equal to __________ times that in a single effect.

(1/n)th

1.5 nth

0.5 nth

nth

(1/n)th

1.5 nth

0.5 nth

nth

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design
Liquid gradient over a tray can be minimised by

Decreasing the number of rows of caps through which the liquid flows or by decreasing the velocity of liquid flow past the caps or by reducing the distance along the tray through which the liquid must

Using split flow, radial flow or cascade flow for column diameter large than 4 ft

All of these

Providing a higher skirt clearance or a higher weir

Decreasing the number of rows of caps through which the liquid flows or by decreasing the velocity of liquid flow past the caps or by reducing the distance along the tray through which the liquid must

Using split flow, radial flow or cascade flow for column diameter large than 4 ft

All of these

Providing a higher skirt clearance or a higher weir

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design

Process Equipment and Plant Design The raio, (properller agitator dia/tank dia) is normally taken as

Process Equipment and Plant Design The equivalent diameter for fluid flow through a channel of constant non-circular cross section of area 'A' is given by (where, P = perimeter of the channel in contact with the fluid)

Process Equipment and Plant Design The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Process Equipment and Plant Design With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Process Equipment and Plant Design In a multiple effect evaporator system having 'n' effects, the amount of water evaporated per unit surface area in approximately equal to __________ times that in a single effect.

Process Equipment and Plant Design Liquid gradient over a tray can be minimised by

Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

Process Equipment and Plant Design
The equivalent diameter for fluid flow through a channel of constant non-circular cross section of area 'A' is given by (where, P = perimeter of the channel in contact with the fluid)

Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Process Equipment and Plant Design
In a multiple effect evaporator system having 'n' effects, the amount of water evaporated per unit surface area in approximately equal to __________ times that in a single effect.

Process Equipment and Plant Design
Liquid gradient over a tray can be minimised by