Figure.2 shows the heat transfer rate per unit width (normal to the page) from a longitudinal section, x2-x₁, can be expressed as 912 = h₁2(x2-x1)(Ts - T∞), where h₁₂ is the average coefficient for the section of length (x2-x1). Consider laminar flow over a flat plate with a uniform temperature Ts. The spatial variation of the local convection coefficient is of the form hx =Cx², where C is a const To loo x2 dx 912 TSK Fig.2. A heat transfer of a longitudinal plate (a) Beginning with the convection rate equation in the form dq' = hxdx(Ts - T∞), derive an expression for h₁₂ in terms of C, x₁, andx2. (b) Derive an expression for h₁₂ in terms of x1, x2, and the average coefficients and h₂, corresponding to lengths x₁, andx2., respectively.
Figure.2 shows the heat transfer rate per unit width (normal to the page) from a longitudinal section, x2-x₁, can be expressed as 912 = h₁2(x2-x1)(Ts - T∞), where h₁₂ is the average coefficient for the section of length (x2-x1). Consider laminar flow over a flat plate with a uniform temperature Ts. The spatial variation of the local convection coefficient is of the form hx =Cx², where C is a const To loo x2 dx 912 TSK Fig.2. A heat transfer of a longitudinal plate (a) Beginning with the convection rate equation in the form dq' = hxdx(Ts - T∞), derive an expression for h₁₂ in terms of C, x₁, andx2. (b) Derive an expression for h₁₂ in terms of x1, x2, and the average coefficients and h₂, corresponding to lengths x₁, andx2., respectively.
Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)
8th Edition
ISBN:9781305387102
Author:Kreith, Frank; Manglik, Raj M.
Publisher:Kreith, Frank; Manglik, Raj M.
Chapter8: Natural Convection
Section: Chapter Questions
Problem 8.54P
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