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

1/2

4

8

2

1/2

4

8

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design
__________ heat exchanger is also known as 'hair pin type' exchanger,

Plate type

Finned

Regenerative

Double pipe

Plate type

Finned

Regenerative

Double pipe

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design
Log mean temperature difference in case of multi-pass shell and tube heat exchanger is always

Less than arithmetic mean value

More than geometric mean value

Both B & C

More than arithmetic mean value

Less than arithmetic mean value

More than geometric mean value

Both B & C

More than arithmetic mean value

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets

Saddles

Columns

Skirts

Brackets

Saddles

Columns

Skirts

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design
In a rotary drier, the average retention time of solid is(where Z = length of the drier, metres ρ = apparent solid density, kg/m³ L = flow rate of dry solids, kg/see. m² drier cross-section H = hold up of solid.)

Z.H/L.ρ

Z.H.ρ/L

H.ρ/L

L/Z.H.ρ

Z.H/L.ρ

Z.H.ρ/L

H.ρ/L

L/Z.H.ρ

ANSWER DOWNLOAD EXAMIANS APP

Process Equipment and Plant Design
Which of the following types of reactors is the safest from operation point of view?

A vapor phase reactor

A liquid phase reactor

Pot type reactor

A liquid phase catalytic reactor

A vapor phase reactor

A liquid phase reactor

Pot type reactor

A liquid phase catalytic reactor

ANSWER DOWNLOAD EXAMIANS APP

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 __________ heat exchanger is also known as 'hair pin type' exchanger,

Process Equipment and Plant Design Log mean temperature difference in case of multi-pass shell and tube heat exchanger is always

Process Equipment and Plant Design Vertical vessels are not supported by

Process Equipment and Plant Design In a rotary drier, the average retention time of solid is(where Z = length of the drier, metres ρ = apparent solid density, kg/m³ L = flow rate of dry solids, kg/see. m² drier cross-section H = hold up of solid.)

Process Equipment and Plant Design Which of the following types of reactors is the safest from operation point of view?

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
__________ heat exchanger is also known as 'hair pin type' exchanger,

Process Equipment and Plant Design
Log mean temperature difference in case of multi-pass shell and tube heat exchanger is always

Process Equipment and Plant Design
Vertical vessels are not supported by

Process Equipment and Plant Design
In a rotary drier, the average retention time of solid is(where Z = length of the drier, metres ρ = apparent solid density, kg/m³ L = flow rate of dry solids, kg/see. m² drier cross-section H = hold up of solid.)

Process Equipment and Plant Design
Which of the following types of reactors is the safest from operation point of view?