Power required for agitation depends upon the

Process Equipment and Plant Design
Power required for agitation depends upon the

Size of agitator & the tank

Agitator type & speed of agitation

Height & properties of the liquid

All of these

Size of agitator & the tank

Agitator type & speed of agitation

Height & properties of the liquid

All of these

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Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.55

0.95

0.8

0.99

0.55

0.95

0.8

0.99

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Process Equipment and Plant Design
In case of design of a shell and tube heat exchanger,

Minimum cleaning lane of 6.5 mm is provided, when tubes are on a square pitch

Minimum tube sheet thickness (in which tubes are fixed) is equal to the O.D. of the tube upto 15 mm tube diameter; and for > 15 mm tube diameter, tube sheet thickness is smaller than tube diameter

All of these

O.D. of the tube is 6 to 40 mm while the tube lengths used are 0.5, 2.5, 3.0, 4.0, 5.0, 6 metres

Minimum cleaning lane of 6.5 mm is provided, when tubes are on a square pitch

Minimum tube sheet thickness (in which tubes are fixed) is equal to the O.D. of the tube upto 15 mm tube diameter; and for > 15 mm tube diameter, tube sheet thickness is smaller than tube diameter

All of these

O.D. of the tube is 6 to 40 mm while the tube lengths used are 0.5, 2.5, 3.0, 4.0, 5.0, 6 metres

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Process Equipment and Plant Design
Column support for the roof of cylindrical storage tank must be provided for

Small diameter tall tanks

Small diameter tanks

All of these

Large diameter tanks

Small diameter tall tanks

Small diameter tanks

All of these

Large diameter tanks

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Process Equipment and Plant Design
In common bubble cap distillation column design practice, riser area is approximately equal to (where, Aa = Annular passage area, and Sa = Slot area)

1.2 Aa = 1.2 Sa

Sa = 1.5 Aa

Aa = Sa

Aa = 1.5 Sa

1.2 Aa = 1.2 Sa

Sa = 1.5 Aa

Aa = Sa

Aa = 1.5 Sa

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Process Equipment and Plant Design
Of the pressure vessels, with same thickness but different diameters, which one withstands higher pressure?

Larger dia long vessel

Strength of the vessel is same irrespective of the diameter

Larger dia vessel

Smaller dia vessel

Larger dia long vessel

Strength of the vessel is same irrespective of the diameter

Larger dia vessel

Smaller dia vessel

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Process Equipment and Plant Design

Process Equipment and Plant Design Power required for agitation depends upon the

Process Equipment and Plant Design It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

Process Equipment and Plant Design In case of design of a shell and tube heat exchanger,

Process Equipment and Plant Design Column support for the roof of cylindrical storage tank must be provided for

Process Equipment and Plant Design In common bubble cap distillation column design practice, riser area is approximately equal to (where, Aa = Annular passage area, and Sa = Slot area)

Process Equipment and Plant Design Of the pressure vessels, with same thickness but different diameters, which one withstands higher pressure?

Process Equipment and Plant Design
Power required for agitation depends upon the

Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

Process Equipment and Plant Design
In case of design of a shell and tube heat exchanger,

Process Equipment and Plant Design
Column support for the roof of cylindrical storage tank must be provided for

Process Equipment and Plant Design
In common bubble cap distillation column design practice, riser area is approximately equal to (where, Aa = Annular passage area, and Sa = Slot area)

Process Equipment and Plant Design
Of the pressure vessels, with same thickness but different diameters, which one withstands higher pressure?