Thermofluids (Determine surface temperature)

AI Thread Summary
The discussion revolves around calculating the heat flux and duct surface temperature for air flowing through a thin pipe. Given the mass flow rate, inlet and outlet temperatures, and heat transfer coefficient, the initial calculation yields a heat transfer of 1313 W. Participants question whether the heat flux can be assumed constant and if the problem is solvable without specific surface conditions. Additionally, there is a request for guidance on determining the heat transfer coefficient for internal flow. The conversation emphasizes the importance of understanding boundary conditions in heat transfer analysis.
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Homework Statement


Air flows at a mass flow rate(m) of 0.05kg/s in a thin pipe with a diameter of 0.15m. The air enters the pipe at (Ti)103 deg celc and cools to(To) 77 deg celc after traveling 5 m in the pipe. The heat transfer coefficient between the duct outer surface and the ambient air at Tamb = 0 deg celc is ho = 6W/m2K.

Determine the heat flux(W/m2 and the duct surface temperature at x = 5m. The duct wall is thin and conduction effect can be neglected.

Homework Equations


q''[W/m2] ...Might need this equation ??

The Attempt at a Solution



q [W] = mcp(Ti-To) = 1313 W where cp = 1010 J/KgK for air flowing through pipe.

If I'm not told that the surface heat flux is constant can I still apply the equation above? Also, without knowing surface conditions such as constant surface heat flux or constant surface temperature is this problem solvable?
 
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Have you learned how to determine the heat transfer coefficient for the internal flow? If so, please tell us how you would proceed.

Chet
 
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