Chemical Engineering - Process Equipment and Plant Design
Exercise : Process Equipment and Plant Design - Section 5
- Process Equipment and Plant Design - Section 1
- Process Equipment and Plant Design - Section 2
- Process Equipment and Plant Design - Section 3
- Process Equipment and Plant Design - Section 4
- Process Equipment and Plant Design - Section 5
- Process Equipment and Plant Design - Section 6
- Process Equipment and Plant Design - Section 7
- Process Equipment and Plant Design - Section 8
11.
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.
12.
Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.
13.
Slope of countercurrent flow rotary drier is in the range of __________ meter/metre.
14.
In case of saddle packing (e.g., berl and intralox saddles), the maximum size of the packing should not exceed __________ of the column diameter.
15.
Seamless pipe is made
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