Transport Phenomena

assumed boundary conditions boundary-layer Btu hr-1 C₁ calculated Chapter circular tube components constant coordinates correlations cylinder density derivation diameter differential equation dimensional analysis dimensionless discussed energy balance equation of continuity equation of motion equations of change Example expression flow system fluid force Fourier's law free convection friction factor function gases given gives gradient heat conduction heat flux heat transfer heat-transfer coefficient Hence incompressible integration kinetic laminar flow liquid mass molecular molecules momentum balance momentum flux Newtonian fluid non-Newtonian Nusselt obtained pipe quantities radiation radius rate of flow result Reynolds number shown in Fig solid solution solved sphere steady-state surface T₁ Table tank temperature profiles thermal conductivity thermal energy time-smoothed transport turbulent flow v₂ velocity distribution velocity profile viscosity wall zero δυ θυ μο әт др ду дх