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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ dished head is the strongest of all.

Torispherical
Hemispherical
Elliptical
None of these

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Process Equipment and Plant Design
The ratio of linear stress to linear strain is termed as the

None of these
Modulus of elasticity
Modulus of rigidity
Bulk modulus

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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
1000
5000
10000

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Process Equipment and Plant Design
The equivalent diameter for fluid flow through a channel of constant non-circular cross section of area 'A' is given by (where, P = perimeter of the channel in contact with the fluid)

√A
4 A/P
A/P
4 P/A

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Process Equipment and Plant Design
Smaller sized packings are generally dumped to the packed columns, and the large ones of size greater than __________ mm are stacked individually, which provides better control over bed porosity and offers lower gas pressure drop.

75
50
150
25

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Process Equipment and Plant Design
Any shell opening greater than 5 cms for a storage tank must be reinforced for reason of

Reduction of discontinuity in shape at the junction
Making the joint leak proof
Preventing the local overstressing of the shell around the opening
None of these

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