Welded joint efficiency in the design of chemical process equipment is taken as

Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.95

0.55

0.75

0.85

0.95

0.55

0.75

0.85

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Process Equipment and Plant Design
__________ liquor is best handled in a long tube vertical evaporator.

Salting

Foamy

Viscous

Scaling

Salting

Foamy

Viscous

Scaling

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

O.D. of the tube for square pitch

Shortest distance between two adj acent tube holes

None of these

Shortest centre to centre distance between adjacent tubes

O.D. of the tube for square pitch

Shortest distance between two adj acent tube holes

None of these

Shortest centre to centre distance between adjacent tubes

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Process Equipment and Plant Design
In the design of a shell and tube heat exchanger, the corrosion allowance

For carbon steel and cast iron pressure parts is 1.5 mm (except for tubes) and for severe conditions it is 3 mm

Need not be provided for non-pressure parts like tie rods, spacers, baffles, supports etc

All of these

For internal cover and tube sheet is provided on both the sides

For carbon steel and cast iron pressure parts is 1.5 mm (except for tubes) and for severe conditions it is 3 mm

Need not be provided for non-pressure parts like tie rods, spacers, baffles, supports etc

All of these

For internal cover and tube sheet is provided on both the sides

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Process Equipment and Plant Design
Cooling water fouling factors vary in the range of 0.001 to 0.003

(BTU/hr.ft² . °F)⁻¹

(kcal/hr. m. °C)⁻¹

(W/m².°K)⁻¹

(kcal/hr.m² .°C)⁻¹

(BTU/hr.ft² . °F)⁻¹

(kcal/hr. m. °C)⁻¹

(W/m².°K)⁻¹

(kcal/hr.m² .°C)⁻¹

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Process Equipment and Plant Design
In a shell and tube heat exchanger having square pitch, the shell side equivalent diameter is given by (where, P = pitch, d = outside diameter of the tube)

4P²/πd

4(P² - πd²/4)/πd

(P² - πd²/4)/πd

Πd/4P²

4P²/πd

4(P² - πd²/4)/πd

(P² - πd²/4)/πd

Πd/4P²

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Process Equipment and Plant Design

Process Equipment and Plant Design Welded joint efficiency in the design of chemical process equipment is taken as

Process Equipment and Plant Design __________ liquor is best handled in a long tube vertical evaporator.

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

Process Equipment and Plant Design In the design of a shell and tube heat exchanger, the corrosion allowance

Process Equipment and Plant Design Cooling water fouling factors vary in the range of 0.001 to 0.003

Process Equipment and Plant Design In a shell and tube heat exchanger having square pitch, the shell side equivalent diameter is given by (where, P = pitch, d = outside diameter of the tube)

Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

Process Equipment and Plant Design
__________ liquor is best handled in a long tube vertical evaporator.

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

Process Equipment and Plant Design
In the design of a shell and tube heat exchanger, the corrosion allowance

Process Equipment and Plant Design
Cooling water fouling factors vary in the range of 0.001 to 0.003

Process Equipment and Plant Design
In a shell and tube heat exchanger having square pitch, the shell side equivalent diameter is given by (where, P = pitch, d = outside diameter of the tube)