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Process Equipment and Plant Design

Process Equipment and Plant Design
The ratio of volumes of the mixed reactor to the plug flow reactor (for identical feed composition, flow rate, conversion, and for all positive reaction orders) is always

>1
< 1
1
Equal to the order of reaction

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Process Equipment and Plant Design
Stage efficiency for packed tower varies with the

Operating pressure and column diameter
Type & size of packing
Fluid rates and fluid properties
All of these

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Process Equipment and Plant Design
Smaller sized packings are generally dumped to the packed columns, and the large ones of size greater than __________ mm are stacked individually, which provides better control over bed porosity and offers lower gas pressure drop.

150
25
75
50

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Process Equipment and Plant Design
The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per metre height of packing.

43835
20-40
1000-1500
100-150

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

Viscosity of the fluid
Density of the fluid
Total cost considerations (pumping cost plus fixed cost of the pipe)
None of these

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

All of these
All multipass
1-1 cocurrent
Double pipe

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