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Process Equipment and Plant Design

Process Equipment and Plant Design
The circumferential (hoop) stress in a thin walled cylinderical vessel under internal pressure is

pd/4t
pd/3t
pd/2t
pd/t

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Process Equipment and Plant Design
Lug support is

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

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Process Equipment and Plant Design
For storing hazardous chemicals in large storage tanks, the minimum safe distance between the two tanks should range between __________ times the tank diameter.

1 to 1.5
4 to 5
2.5 to 3.5
6 to 8

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Process Equipment and Plant Design
Corrosion allowance in the design of pressure vessel/chemical equipment is not necessary, if

Material of construction is high alloy steel
Plain carbon steel and cast iron parts are used
Both B & C
Wall thickness is > 30 mm

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Process Equipment and Plant Design
The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per metre height of packing.

20-40
100-150
43835
1000-1500

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

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

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