In the final stages of production, a pharmaceutical is sterilized by heating it from 25 to 75°C as it moves at 0.22 m/s through a straight thin-walled stainless steel tube of 12.7-mm diameter. A uniform heat flux is maintained by an electric resistance heater wrapped around the outer surface of the tube. If the tube is 10 m long, what is the required heat flux? If fluid enters the tube with a fully developed velocity profile and a uniform temperature profile, what is the surface temperature at the tube exit? Fluid properties may be approximated as p = 1000 kg/m³, cp 4000 J/kg-K, μ = 2 x 103 kg/s-m, k = 0.8 W/m-K, and Pr = 10. = Determine the required heat flux, W/m². q" = i W/m² Determine the surface temperature at the tube exit, in °C. Tsp = °C

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Chapter7: Forced Convection Inside Tubes And Ducts
Section: Chapter Questions
Problem 7.15P
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In the final stages of production, a pharmaceutical is sterilized by heating it from 25 to 75°C as it moves at 0.22 m/s through a
straight thin-walled stainless steel tube of 12.7-mm diameter. A uniform heat flux is maintained by an electric resistance heater
wrapped around the outer surface of the tube. If the tube is 10 m long, what is the required heat flux? If fluid enters the tube with a
fully developed velocity profile and a uniform temperature profile, what is the surface temperature at the tube exit? Fluid properties
may be approximated as p = 1000 kg/m³, cp = 4000 J/kg-K, μ = 2 × 10³ kg/s-m, k = 0.8 W/m-K, and Pr = 10.
Determine the required heat flux, W/m².
q'" =
W/m²
i
Determine the surface temperature at the tube exit, in °C.
Tso =
°C
Physical Properties Mathematical Functions
Transcribed Image Text:In the final stages of production, a pharmaceutical is sterilized by heating it from 25 to 75°C as it moves at 0.22 m/s through a straight thin-walled stainless steel tube of 12.7-mm diameter. A uniform heat flux is maintained by an electric resistance heater wrapped around the outer surface of the tube. If the tube is 10 m long, what is the required heat flux? If fluid enters the tube with a fully developed velocity profile and a uniform temperature profile, what is the surface temperature at the tube exit? Fluid properties may be approximated as p = 1000 kg/m³, cp = 4000 J/kg-K, μ = 2 × 10³ kg/s-m, k = 0.8 W/m-K, and Pr = 10. Determine the required heat flux, W/m². q'" = W/m² i Determine the surface temperature at the tube exit, in °C. Tso = °C Physical Properties Mathematical Functions
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