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Process Equipment and Plant Design

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

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

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Process Equipment and Plant Design
In actual operation of a bubble cap distillation tower, the __________ at the bottom of the tower is more than that at the top of the tower.

Molal flow rate of vapour
All of these
Vapour molecular weight
Pressure and temperature

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Process Equipment and Plant Design
Filtration rate is affected by the

Area of filtering surface & the viscosity of filtrate
Cake & filter medium resistance
All of these
Pressure drop across the cake & filter medium

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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)

Πd/4P²
4P²/πd
(P² - πd²/4)/πd
4(P² - πd²/4)/πd

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

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

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

All of these
Height & properties of the liquid
Agitator type & speed of agitation
Size of agitator & the tank

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