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Process Equipment and Plant Design

Process Equipment and Plant Design
Movement of pipeline caused by thermal expansion is taken care by providing

Expansion joint
Change in the shape of pipeline
Changes in its direction
All of these

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Process Equipment and Plant Design
In case of saddle packing (e.g., berl and intralox saddles), the maximum size of the packing should not exceed __________ of the column diameter.

l/15th
l/50th
l/5th
l/30th

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Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Small horizontal
Thick walled
Tall vertical
Large horizontal

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Process Equipment and Plant Design
Slope of countercurrent flow rotary drier is in the range of __________ meter/metre.

0 to 0.8
0 to 2.2
0 to 1.5
0 to 0.08

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Process Equipment and Plant Design
Tube wall thickness depends on the cor-rosiveness of the fluids and their operating pressure & temperature and is specified by Birmingham wire gauge (B.W.G)-a number which varies from 8 to 18 with the numbers 14 and 16 being more commonly used. Outside diameter of tubes varies from about 15 to 50 mm; however a tube of less than __________ mm outside diameter is generally not recommended for fouling fluids.

28
19
38
16

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Process Equipment and Plant Design
The LMTD correction factor (FT) is applied in __________ heat exchangers.

All of these
1-1 cocurrent
All multipass
Double pipe

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