Non-Newtonian Pseudoplastic Fluid Flow and Heat Transfer inside a Horizontal Duct: New Correlations

In this chapter, we have studied the problem of forced convection in a simple horizontal cylindrical pipe. Two boundary conditions are considered, uniform constant heat flux and uniform temperature. The fluid to be heated is pseudoplastic, modeled by the Ostwald law (n ≤ 1.0). A fully developed velocity profile is assumed at the pipe entrance. The energy equation is solved numerically with a simple implicit finite difference scheme. Results focus on the effects of the rheological behavior (index n), the type of heating, and the Pe number on the heat transfer coefficient (Nu) and the thermal entry length. They show an improvement in heat transfer with a decrease in the fluid-structure index (n). An increasing thermal length when Pe and/or n increase is also recorded. This may lead to a huge increase in the tube’s length when a thermal establishment is targeted. New, simple, precise, and physically indicative correlations with wide ranges of variation of the main parameters are proposed here. Their mathematical forms are chosen mainly to guide manufacturers for heat exchangers dimensioning. Scientists have also shown an interest in them as tools for validation and physical interpretation.