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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

Sieve plate
Bubble cap plate
Packed
None of these

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Process Equipment and Plant Design
Which of the following efficiencies can be greater than 100%?

None of these
Overall plate efficiency
Murphree plate efficiency
Point efficiency

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Process Equipment and Plant Design
Large process vessels operating under extreme temperature and pressure conditions are normally clad/ lined with materials like stainless steel, aluminium, nickel & its alloys, copper & its alloys and titanium. The cladding thickness is generally about __________ percent of the total thickness.

10 to 20
30 to 40
40 to 50
1 to 5

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Process Equipment and Plant Design
Value of Peclet number = 0, is the representative of

Plug flow
Complete back mixing
Laminar flow
Eddy diffusivity = 0

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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)

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

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Process Equipment and Plant Design
Spherical shaped pressure vessel is considered to be the most ideal, because it can

Be supported very easily
Withstand higher pressure for a given metallic shell thickness
Be designed without wind load considerations
Be fabricated very easily

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