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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
Optimum economic pipe diameter for fluid flow is determined by the

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

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Process Equipment and Plant Design
With increase in the number of shell passes, the value of FT

Remains same, only if the number of tube passes does not change
Remains same
Decreases
Increases

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Process Equipment and Plant Design
The slope of the feed line in distillation opeartion is given by (where, q = fraction of the feed stream that is liquid.)

-q/(1-q)
-q
-q/(q-1)
None of these

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Process Equipment and Plant Design
Poisson's ratio of a material is the ratio of unit lateral strain to the unit axial elongation within its elastic limit. The value of Poisson's ratio for structural and pressure vessel steel may be taken as

0.75
0.01
0.95
0.3

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Process Equipment and Plant Design
The necessary wall thickness for a metallic storage vessel is a function of the

Ultimate tensile strength (or yield point) of the material and operating temperature
All of these
Operating pressure and welding/joint efficiency
Diameter of the vessel

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