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Process Equipment and Plant Design

Process Equipment and Plant Design
The thermal stress in a metallic bar does not depend upon the

Changes in temperature
Both A & B
Cross-sectional area
Neither A nor B

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Process Equipment and Plant Design
A shell may by termed as thin if its thickness to diameter ratio is less than 0.1. The factor which can be neglected in the calculation of membrane stresses is

Elongation
Bending
Deformation
Shear

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Process Equipment and Plant Design
Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is

More or less depending upon the pressure & temperature inside the vessel and the nature of the fluid contained therein
More
Less
Same

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Process Equipment and Plant Design
The dust collection efficiency of a cyclone separator

None of these
Is directly proportional to the radius of the dust particle path
Decreases with increase in gas flow rate
Is inversely proportional to the mass of the dust particle

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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

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

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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
O.D. of the tube for square pitch
Shortest centre to centre distance between adjacent tubes
Shortest distance between two adj acent tube holes

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