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Process Equipment and Plant Design

Process Equipment and Plant Design
Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.

2.5-3.0
15-20
5-7.5
10-12.5

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Process Equipment and Plant Design
Steam is preferred to be used as a heating medium in heat exchangers, because of its

Low cost
Non-corrosive condensate
High film co-efficient
High latent heat

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Process Equipment and Plant Design
Which of the following lengths of heat exchanger tubes are normally not used in practice?

6 metres
0.5 metre
10 metres
2.5 metres

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Process Equipment and Plant Design
Minimum baffle spacing recommended in a shell and tube heat exchanger is equal to

I.D. of the shell
25 cms
40% of the I.D. of the shell
5 cms

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Process Equipment and Plant Design
Maximum allowable vapour velocity in a bubble cap tower is determined by the

None of these
Entrainment considerations
Vapour density
Diameter of the column

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Process Equipment and Plant Design
Lug support is

Same as bracket support
The most suitable for thick vertical vessel
Provided usually for vessels of much smaller height than skirt supported vessels
All of these

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