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Process Equipment and Plant Design

Process Equipment and Plant Design
The difficulty of liquid distribution in packed towers is accentuated, when the ratio of tower diameter to packing diameter is

> 7 < 15
< 7
< 30
> 20 < 50

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Process Equipment and Plant Design
The absorption factor is defined as (where, S₁ = slope of the equilibrium curve, S₂ = slope of the operating line)

S₂/S₁
1/S₁.S₂
S₁.S₂
S₁/S₂

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Process Equipment and Plant Design
Accidents in chemical plants are mostly due to

Improper layout of the equipments
Failure of equipments
Inadequate equipment design
Faulty operating procedures

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Process Equipment and Plant Design
Elastic failure of a material occurs, when the tensile stress equals yield strength, yield point or the elastic limit. Also, the elastic failure occurs according to maximum strain theory, when the maximum tensile strain equals (where, σ = yield strength and E = modulus of elasticity)

E
Σ/E
E/σ
Σ

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Process Equipment and Plant Design
To keep the power input constant for a stirred vessel operating under fully developed turbulent flow conditions (constant power number), if the impeller diameter is increased by 20%, the impeller speed should be decreased by a factor of

(1.2)3/5
(1.2)2/3
(1.2)3/2
(1.2)5/3

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Process Equipment and Plant Design
The wall thickness for a large high pressure pipeline is determined by the consideration of the

Temperature stresses
Circumferential pipewall tension
Forces exerted by static and dynamic action at bends
Axial tensile stress in the pipe

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