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Process Equipment and Plant Design

Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.99
0.55
0.8
0.95

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Process Equipment and Plant Design
For identical operating conditions, the pressure drop over __________ tray is the highest out of the following.

Valve
Sieve
Bubble cap
Counterflow

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Process Equipment and Plant Design
Wind load consideration in the design of a support can be neglected, when the vessel is

Tall (say 30 metres), but is full of liquid
Tall but empty
None of these
Short (< 2 m) and housed indoor

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Process Equipment and Plant Design
The stress developed in a material without any permanent set is called the

Breaking stress
Elastic limit
Ultimate stress
Yield stress

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Process Equipment and Plant Design
In a heat exchanger, shell side fluid velocity can be changed by changing the tube

Layout
Neither A nor B
Pitch
Both A & B

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Process Equipment and Plant Design
For a cylinderical vessel of moderate height, the weld joint efficiency for joints parallel to the cylinderical axis is given as 1.0, while for joints along the girth (circumference) it is given as 0.8. In calculating the shell wall thickness using code formula for an internally pressurised cylinderical vessel, what value of weld joint efficiency should be used?

1
0.9
0.8
(0.8)0.5

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