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Process Equipment and Plant Design

Process Equipment and Plant Design
The ratio of down take area to cross-sectional area of the tube, for calendria type evaporator ranges from

0.5 to 1
1 to 1.5
2 to 2.5
1.5 to 2

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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
Making the joint leak proof
Preventing the local overstressing of the shell around the opening
Reduction of discontinuity in shape at the junction

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

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Process Equipment and Plant Design
Le/D for 90° elbow (medium radius) and 90°square elbow would be respectively around

250 and 600
100 and 250
3 and 5
25 and 60

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Process Equipment and Plant Design
For turbine agitator, the impeller diameter is about

0.3 to 0.5 d
0.1 to 0.2 d
0.65 to 0.85 d
0.95 d

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Process Equipment and Plant Design
Normally, the length to diameter ratio of rotary dryers varies form 4 to 10 and for its economic operation, the number of transfer units (NTU) for such dryers varies from

7.5-10.0
44119
3.5-5.5
1.5-2.5

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