Flow over an isothermal plate is shown in the right. Assuming steady state, incompressible, laminar flow, constant fluid
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Flow over an isothermal plate is shown in the right. Assuming steady state, incompressible, laminar flow, constant fluid
Flow over an isothermal plate is shown in the right. Assuming steady state, incompressible, laminar flow, constant fluid properties, negligible viscous dissipation and dp/dx = 0, the boundary layer equations are reduced to: T, 8(x) L ди Ov ди du 22u + = 0 - (1), u +v =V ax ay ax ay ду? at ar 02T (2), and u + v Ξα ax ду ду? (3) After introducing the stream function, y, and defining new dependent and independent variables, f (n) and n, such that: f(n) , n = y/uc/ux. Uvx/uce Pr dt* d27* (a) Please derive the energy equation (3) to + f = 0, where T*=[(T-Ts)/(Too-Ts)] dn2 dn (b) Applying the boundary conditions, T*(0) = 0 and T*(60) = 1, numerical integration shows: = 0.332Pr1/3 for Pr20.6. Please derive Nux = 0.332Re 2 Pr1/3 dn = dT* 1/2 'n=0
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