High pressure fluid in a shell and tube heat exchanger should preferably be routed through the
Options
A. tubes to avoid the expansion of high pressure shell construction.
B. shell side for smaller total pressure drop.
C. shell side, if the flow is counter-current and tube side if the flow is co-current.
D. shell side for large overall heat transfer co-efficient.
Correct Answer
tubes to avoid the expansion of high pressure shell construction.
Process Equipment and Plant Design problems
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1. Low pressure steam (with saturation temperature between 105 to 120°C) is usually used in the vacuum evaporators, which normally employ a vacuum of about __________ mm Hg (referred to a 760 mm mercury barometer).
4. 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.
Correct Answer: not less than one-fourth of the tube diameter or 3/16".
9. For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is
10. In a shell and tube heat exchanger, the overall heat transfer co-efficient is proportional to the tube side (volumetric flow rate)0.8. This is valid, only when the ratio of the tube side film resistance to the total resistance is almost equal to