in heat transfer at a boundary (surface) within a fluid, the nusselt number (nu) is the ratio of convective to conductive heat transfer across (normal to) the boundary. in this context, convection includes both advection and diffusion. named after wilhelm nusselt, it is a dimensionless number. the conductive component is measured under the same conditions as the heat convection but with a (hypothetically) stagnant (or motionless) fluid. a nusselt number close to one, namely convection and conduction of similar magnitude, is characteristic of "slug flow" or laminar flow. a larger nusselt number corresponds to more active convection, with turbulent flow typically in the 100â1000 range. the convection and conduction heat flows are parallel to each other and to the surface normal of the boundary surface, and are all perpendicular to the mean fluid flow in the simple case. :\mathrm{nu}_l = \frac{\mbox{convective heat transfer }}{\mbox{conductive heat transfer }} = \frac{hl}{k} where l is the characteristic length, k is the thermal conductivity of the fluid, h is the convective heat transfer coefficient of the fluid. * selection of the characteristic length should be in the direction of growth (or thickness) of the boundary layer; some examples of characteristic length are: the outer diameter of a cylinder in (external) cross flow (perpendicular to the cylinder axis), the length of a vertical plate undergoing natural convection, or the diameter of a sphere. for complex shapes, the length may be defined as the volume of the fluid body divided by the surface area. * the thermal conductivity of the fluid is typically (but not always) evaluated at the film temperature, which for engineering purposes may be calculated as the mean-average of the bulk fluid temperature and wall surface temperature. in contrast to the definition given above, known as average nusselt number, local nusselt number is defined by taking the length to be the distance from the surface boundary to the local point of interest. :nu_x = \frac{h_x x}{k} the mean, or average, number is obtained by integrating the expression over the range of interest, such as: :\overline{nu}=\frac{1}{h} \int_{0}^{h} {nu(y) \cdot dy} the mass transfer analog of the nusselt number is the sherwood number. ==introduction== an understanding of convection boundary layers is necessary
Convection Dimensionless_numbers_of_fluid_mechanics Dimensionless_numbers_of_thermodynamics Fluid_dynamics Heat_transfer