2002
DOI: 10.1046/j.1365-246x.1999.00795.x
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Parametrization of heat transport by non-Newtonian convection

Abstract: Summary We study the heat transport efficiency of the 2‐D steady convection in a box (aspect ratio=1) with a power‐law creep which may be important for mantle convection. Effects of pressure‐ (depth) and temperature‐dependent creep are also studied. To analyse the heat transport, we use the local Rayleigh (Ral) and Nusselt (Nul) numbers, which are defined by the values characterizing each thermal boundary layer except the length scale. The commonly used definition of the Rayleigh and Nusselt numbers is only us… Show more

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Cited by 6 publications
(3 citation statements)
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“…This thickness is less than the 310 km expected from equation (15) for nonlinear convection (n = 5 in equation (15)). This discrepancy occurs because the convection in the model is very time-dependent, like convection (without basal drag) cooled from above in a fluid with a nonlinear viscosity [Solomatov, 1995;Reese et al, 1998Reese et al, , 1999Kawada and Honda, 1999;Solomatov andMoresi, 1997, 2000]. That is, the thermal boundary layer is stagnant at most times.…”
Section: Parameterized Convection With Strong Basal Dragmentioning
confidence: 99%
“…This thickness is less than the 310 km expected from equation (15) for nonlinear convection (n = 5 in equation (15)). This discrepancy occurs because the convection in the model is very time-dependent, like convection (without basal drag) cooled from above in a fluid with a nonlinear viscosity [Solomatov, 1995;Reese et al, 1998Reese et al, , 1999Kawada and Honda, 1999;Solomatov andMoresi, 1997, 2000]. That is, the thermal boundary layer is stagnant at most times.…”
Section: Parameterized Convection With Strong Basal Dragmentioning
confidence: 99%
“…On the Earth it occurs as secondary convection beneath the plates and transfers moderate amounts of heat to the oceanic lithosphere [Davaille and Jaupart, 1994] where k is thermal conductivity, p is density, g is the acceleration of gravity, cz is the thermal expansion coefficient, r-=k/pC is thermal diffusivity, ri0 is the half-space viscosity, T n is the temperature to change viscosity by a factor of e, and pC is specific heat per volume. The temperature contrast across the boundary layer is 2 T n to 3 T n. Kawada and Honda, 1999]. Crudely, nonlinear fluid is nearly equivalent to a linear fluid with an apparent T n a factor of n larger than the actual T n. More precise parameterizations are complicated and are not repeated here.…”
Section: Modes Of Convectionmentioning
confidence: 99%
“…Eq. 27has also been used by Christensen (1984), who found l = 1 also to be a suitable choice, as we well as by Kawada & Honda (1999). Independent of the method used, we always exclude the stagnant lid upon averaging the viscosity.…”
Section: Nusselt-rayleigh Scalingmentioning
confidence: 99%