An increase in the liquid resistance to interphase mass transfer and a resultant reduction in plate efficiency is caused by

Process Equipment and Plant Design
An increase in the liquid resistance to interphase mass transfer and a resultant reduction in plate efficiency is caused by

All of these

Decrease in gas solubility for absorbers

An increase in relatived volatility for rectification columns

An increase in liquid viscosity

All of these

Decrease in gas solubility for absorbers

An increase in relatived volatility for rectification columns

An increase in liquid viscosity

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Process Equipment and Plant Design
Oxygen carrying pipelines in chemical industries are coloured with __________ colour.

Red

Black

Yellow

Blue

Red

Black

Yellow

Blue

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Process Equipment and Plant Design
Baffle width is normally taken as __________ times the tank diameter.

0.2-0.45

0.45-0.6

0.1-0.12

0.4-0.5

0.2-0.45

0.45-0.6

0.1-0.12

0.4-0.5

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Process Equipment and Plant Design
A/an __________ is used for changing the direction of a pipeline.

Elbow

Union

Disc compensator

Flange

Elbow

Union

Disc compensator

Flange

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Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

0.2-0.5

0.1-0.2

1.2-1.5

0.4-0.9

0.2-0.5

0.1-0.2

1.2-1.5

0.4-0.9

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the 'tube pitch' is defined as the

None of these

O.D. of the tube for square pitch

Shortest distance between two adj acent tube holes

Shortest centre to centre distance between adjacent tubes

None of these

O.D. of the tube for square pitch

Shortest distance between two adj acent tube holes

Shortest centre to centre distance between adjacent tubes

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Process Equipment and Plant Design

Process Equipment and Plant Design An increase in the liquid resistance to interphase mass transfer and a resultant reduction in plate efficiency is caused by

Process Equipment and Plant Design Oxygen carrying pipelines in chemical industries are coloured with __________ colour.

Process Equipment and Plant Design Baffle width is normally taken as __________ times the tank diameter.

Process Equipment and Plant Design A/an __________ is used for changing the direction of a pipeline.

Process Equipment and Plant Design The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

Process Equipment and Plant Design In a shell and tube heat exchanger, the 'tube pitch' is defined as the

Process Equipment and Plant Design
An increase in the liquid resistance to interphase mass transfer and a resultant reduction in plate efficiency is caused by

Process Equipment and Plant Design
Oxygen carrying pipelines in chemical industries are coloured with __________ colour.

Process Equipment and Plant Design
Baffle width is normally taken as __________ times the tank diameter.

Process Equipment and Plant Design
A/an __________ is used for changing the direction of a pipeline.

Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

Process Equipment and Plant Design
In a shell and tube heat exchanger, the 'tube pitch' is defined as the