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Laminar mixing and heat transfer for constant heat flux boundary condition

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Abstract

In a recent paper we have investigated mixing and heat transfer enhancement in a mixer composed of two circular rods maintained vertically in a cylindrical tank. The rods and tank can rotate around their revolution axes while their surfaces were maintained at a constant temperature. In the present study we investigate the differences in the thermal mixing process arising from the utilization of a constant heat flux as a boundary condition. The study concerns a highly viscous fluid with a high Prandtl number for which this chaotic mixer is suitable. By solving numerically the flow and energy equations, and using different statistical tools we characterize the evolution of the fluid temperature and its homogenization. Fundamental differences are reported between these two modes of heating or cooling: while the mixing with an imposed temperature results in a homogeneous temperature field, with a fixed heat flux we observe a constant difference between the maximal and minimal temperatures that establish in the fluid; the extent of this difference is governed by the efficiency of the mixing protocol.

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Abbreviations

A :

Area (m2)

C p :

Heat capacity (J/kg K)

k :

Thermal conductivity (W/m K)

L :

Wall characteristic length (m)

p :

Pressure (Pa)

\(\dot q\) :

Surface heat flux (W/m2)

R 3 :

Tank radius (m)

R 1, R 2 :

Rod radii (m)

t :

Time (s)

T :

Temperature (K)

U :

Maximum tangential velocity of the walls (m/s)

\({\bf U}\) :

Velocity field (m/s)

Nu :

Nusselt number

Pe :

Péclet number

Pr :

Prandtl number

Re :

Reynolds number

X :

Rescaled dimensionless temperature

\(\varepsilon\) :

Eccentricity (m)

ρ:

Fluid density (kg/m3)

σ:

Standard deviation

τ:

Period of modulation (s)

\(\overset{=}{\tau}\) :

Viscous stress tensor (Pa)

\(\Upomega\) :

Angular velocity (rad/s)

c :

Cell

m :

Mean

f :

Face of a cell

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Correspondence to Kamal El Omari.

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El Omari, K., Le Guer, Y. Laminar mixing and heat transfer for constant heat flux boundary condition. Heat Mass Transfer 48, 1285–1296 (2012). https://doi.org/10.1007/s00231-012-0976-z

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