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Heat transfer to newtonian and non‐newtonian liquids in a screw agitator and draft coil system
Author(s) -
Carreau P. J.,
Paris J.,
Guérin P.
Publication year - 1994
Publication title -
the canadian journal of chemical engineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.404
H-Index - 67
eISSN - 1939-019X
pISSN - 0008-4034
DOI - 10.1002/cjce.5450720605
Subject(s) - reynolds number , agitator , nusselt number , prandtl number , mechanics , non newtonian fluid , electromagnetic coil , heat transfer , newtonian fluid , materials science , thermodynamics , heat exchanger , heat transfer coefficient , physics , impeller , turbulence , quantum mechanics
Heat transfer has been investigated for several Newtonian and non‐Newtonian liquids mixed in a flat bottomed vessel equipped with a screw agitator and a coil acting simultaneously as draft tube and heat exchanger. Heat transfer rates from coil to liquid were determined for different coil designs, rheological properties and operating conditions in the heating and cooling modes. A circulation Reynolds number is defined, the characteristic length being the effective height of the heat exchanger (the coil) and the characteristic velocity being the circulation velocity of the fluid which was determined experimentally. Using this Reynolds number, it was possible to establish a single correlation for the Nusselt number as a function of Reynolds and Prandtl numbers. Geometric ratios do not appear in this correlation which could adequately represent more than 200 experimental data. A similar single correlation could not be obtained when using the conventional mixing Reynolds number. This novel system is shown to be very efficient for handling rheologically complex fluids.