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Dimensionless Numbers in Heat Transfer

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Biot Number (Bi)

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Measures the ratio of internal thermal resistance within a body to the external thermal resistance across the boundary layer. Important in estimating temperature gradients in a solid object during heat transfer. Defined as Bi=hLkBi = \frac{hL}{k}, where hh is the heat transfer coefficient, LL is the characteristic length, and kk is the thermal conductivity of the solid.

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Schmidt Number (Sc)

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Represents the ratio of momentum diffusivity (kinematic viscosity) to mass diffusivity, it is more commonly used in mass transfer but can be relevant for coupled heat and mass transfer scenarios. Defined by Sc=νDSc = \frac{\nu}{D}, where ν\nu is the kinematic viscosity and DD is the mass diffusivity.

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Prandtl Number (Pr)

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Expresses the ratio of momentum diffusivity (kinematic viscosity) to thermal diffusivity and helps in analyzing forced and natural convection problems. Defined by Pr=ναPr = \frac{\nu}{\alpha} where ν\nu is the kinematic viscosity and α\alpha is the thermal diffusivity.

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Grashof Number (Gr)

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Quantifies the ratio of buoyancy to viscous forces in a fluid and is used in the context of natural (free) convection. Defined as Gr=gL3βΔTν2Gr = \frac{gL^3\beta\Delta T}{\nu^2}, where gg is the acceleration due to gravity, β\beta is the thermal expansion coefficient, ΔT\Delta T is the temperature difference, and ν\nu is the kinematic viscosity.

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Péclet Number (Pe)

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Represents the ratio of the rate of advection of a physical quantity by the flow to the rate of diffusion of the same quantity driven by an appropriate gradient. For heat transfer, it is given by Pe=Re×Pr=uLαPe = Re \times Pr = \frac{uL}{\alpha}, where uu is the flow velocity, and α\alpha is the thermal diffusivity.

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Rayleigh Number (Ra)

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A combination of Grashof and Prandtl numbers that represents the ratio of buoyancy and thermal diffusivity forces in natural convection. Defined as Ra=Gr×Pr=gβΔTL3ναRa = Gr \times Pr = \frac{g\beta\Delta TL^3}{\nu\alpha}, where gg is the gravitational acceleration, β\beta is the thermal expansion coefficient, ΔT\Delta T is the temperature difference, LL is the characteristic length, ν\nu is the kinematic viscosity, and α\alpha is the thermal diffusivity.

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Stanton Number (St)

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Indicates the ratio of heat transferred into a fluid to the heat capacity of the fluid flowing. It can be described by St=NuRe×PrSt = \frac{Nu}{Re \times Pr} or St=hρucpSt = \frac{h}{\rho u c_p}, where hh is the heat transfer coefficient, ρ\rho is the density, uu is the velocity, and cpc_p is the specific heat at constant pressure.

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Reynolds Number (Re)

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Represents the ratio of inertial forces to viscous forces and predicts the transition from laminar to turbulent flow which affects convective heat transfer rates. Defined by the equation Re=ρuLμRe = \frac{\rho u L}{\mu}, where ρ\rho is density, uu is velocity, LL is characteristic length, and μ\mu is dynamic viscosity.

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Nusselt Number (Nu)

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Describes the enhancement of heat transfer through a fluid layer as a result of convective motion of the fluid compared with conductive heat transfer across a stagnant fluid layer. Defined by Nu=hLkNu = \frac{hL}{k}, where hh is the convective heat transfer coefficient, LL is characteristic length, and kk is the thermal conductivity.

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Fourier Number (Fo)

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Expresses the ratio of conductive heat transfer to the energy stored in a material. Primarily used in transient heat conduction analysis. Defined by Fo=αtL2Fo = \frac{\alpha t}{L^2} where α\alpha is the thermal diffusivity, tt is time, and LL is the characteristic length.

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