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Process Equipment and Plant Design

Process Equipment and Plant Design
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m².°C.

15000
1250
2500
7500

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Process Equipment and Plant Design
Lug support is

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

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Process Equipment and Plant Design
Baffles are provided in a shell and tube heat exchanger to increase the turbulence and velocity of the shell side fluid. Which of the following shaped baffles does not fall in the category of transverse baffle?

Flat plate extending across the wall
Helical type baffle
Segmental baffle
Disk type baffle

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Process Equipment and Plant Design
A rivetted joint does not fail by __________ of rivets.

Shearing
Tearing
Tearing of the plate across a row
None of these

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Process Equipment and Plant Design
25 per cent cut segmental baffle means that the baffle

Height is 75% of the I.D. of the shell
Width is 25% of its height
Spacing is 75% of its height
Height is 25% of the I.D. of the shell

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Process Equipment and Plant Design
Poisson's ratio of a material is the ratio of unit lateral strain to the unit axial elongation within its elastic limit. The value of Poisson's ratio for structural and pressure vessel steel may be taken as

0.01
0.75
0.3
0.95

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