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Process Equipment and Plant Design

Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the minimum shell thickness for carbon steel (inclusive of corrosion allowance) depends on shell diameter and is in the range of __________ mm.

43895
44058
44183
43962

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Process Equipment and Plant Design
Maximum plate efficiency is achieved in case of __________ flow.

Cascade
Split
Reverse
Cross

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Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

All of these
Back trapping
Maldistribution of gas
Gas blowing beneath cap skit

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the 'tube pitch' is defined as the

O.D. of the tube for square pitch
None of these
Shortest distance between two adj acent tube holes
Shortest centre to centre distance between adjacent tubes

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Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the effect of L/D on inside film heat transfer co-efficient (hi) vanishes after a Reynold number of

3000
5000
1000
10000

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Process Equipment and Plant Design
Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.

5 to 10
2.5 to 5
1.5 to 2
10 to 15

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