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Process Equipment and Plant Design

Process Equipment and Plant Design
Le/D for a Tee (used as elbow, entering run) would be around

5
350
200
60

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Process Equipment and Plant Design
Fouling factor must be included in the calculation of over all design heat transfer coefficient, when the liquid

Containing suspended solids flows at high velocity
Containing suspended solids flows at low velocity
Is of high specific gravity
Is highly viscous

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

(W/m².°K)⁻¹
(kcal/hr. m. °C)⁻¹
(BTU/hr.ft² . °F)⁻¹
(kcal/hr.m² .°C)⁻¹

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Process Equipment and Plant Design
Apex angle of conical heads used in the bottom heads of chemical process equipments is usually

45°
75°
30°
60°

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Process Equipment and Plant Design
The ratio of lateral strain to linear strain is termed as the

Shear modulus
Modulus of elasticity
Bulk modulus
Poisson's ratio

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Process Equipment and Plant Design
The buckling tendency of compression members is always in the direction of the

Perpendicular to the axis of the load
Axis of the load
Least radius of gyration
None of these

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