Continuous heat extraction is important for the process of freeze concentration of aqueous solutions, in which water is removed as solid ice. Three typical unsteady heat transportation patterns were distinguished at the subcooled surface of a scraped-surface heat exchanger (SSHE) in this study. They were found in different stages of freeze concentration. Experimental measurement of the heat-transfer coefficient in an SSHE showed that the overall heat-transfer coefficient of stage III, which was characterized by ice formation on the cooler surface, was about 1.5 times higher than stage I, where no ice formed. Although the ice layer (also known as ice fouling) on a heat exchanger surface may be considered disadvantageous for heat transfer, the initial ice formation actually boosted up the heat transportation in an SSHE. The mechanism analysis and mathematical modeling of this phenomenon, however, have not been found in the literature. A mathematical model is developed and a unified expression of the heat-transfer coefficient in an SSHE with/without phase change is presented. The model predicts a step increase of heat transfer occurs at the onset of ice formation and the maximum heat-transfer coefficient exists in a narrow range right after reaching the freezing point. These are consistent with the experimental results of this study.
[1]
Neville H Fletcher,et al.
The Chemical Physics of Ice
,
1970
.
[2]
Signe Kjelstrup Ratkje,et al.
Modelling the Freeze Concentration Process by Irreversible Thermodynamics
,
1995
.
[3]
J. Gros,et al.
Estimation of physical properties of foamed foods using energy dissipation in scraped-surface heat exchangers
,
1995
.
[4]
C. J. King,et al.
Kinetics of ice crystallization in sugar solutions and fruit juices
,
1974
.
[5]
Kevin W. Free,et al.
A note on the two models of ice growth velocity in aqueous solutions derived from an irreversible thermodynamics analysis and the conventional heat and mass transfer theory
,
1997
.
[6]
M. Cheryan,et al.
Performance of a Scraped-Surface Heat Exchanger Under Ultra High Temperature Conditions: A Dimensional Analysis
,
1982
.
[7]
D. I. Chandarana,et al.
Residence time distribution of particulate foods at aseptic processing temperatures
,
1996
.
[8]
N. H. Fletcher,et al.
The Chemical Physics of Ice: Liquid water and freezing
,
1970
.
[9]
M. Abid,et al.
Numerical analysis of three-dimensional flow and thermal behaviour in a scraped-surface heat exchanger
,
1997
.