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Process Equipment and Plant Design

Process Equipment and Plant Design
Joint efficiency (J) for a seamless pipe is

1.2
1
< 0.5
0.85

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Process Equipment and Plant Design
Rotary driers are most economically designed for the number of heat transfer units (HTU) from

10 to 20
5 to 10
1.5 to 2.5
0.01 to 1

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Process Equipment and Plant Design
The safe height (h) to diameter (d) ratio (i.e., h/d) for liquid/petro fuel storage tank of capacity more than 45 kilolitres is less than

3.5
1
3
2

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Process Equipment and Plant Design
Wall thickness of schedule 40 pipe as compared to that of schedule 80 pipe is

Same
Less
More
Cither A or B; depends upon the I.D. of the pipe

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Process Equipment and Plant Design
The main purpose of providing stepping on the trays is to

Decrease the pressure drop
Increase the residence time
Facilitate handling of large flow rate of liquid
Improve the flow condition

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

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

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