Analysis of the heat and mass transfer processes in solar stills – The validation of a model

Abstract The outcome of the earlier systematic research work on the theoretical modeling of the complex transport phenomena occurring in solar stills was the development of the fundamental Dunkle’s model, already known almost four decades ago. Although it has been based on several simplified assumptions, this model has extensively been employed over the years as a convenient and sufficiently accurate predictive tool for solar stills working under ordinary operating conditions. However, it has occasionally been reported that it fails under unusual operating conditions, mainly corresponding to higher average temperatures, usually leading to higher distillate yields. The aim of the present investigation was to relax the initially established simplified assumptions of the fundamental Dunkle’s model and to evaluate the comparative accuracy of both, the refined and the earlier fundamental models against an extensive body of previously reported measurements from the literature, both field and laboratory. The comparative presentation of results indicates that although both models are impressively correct for ordinary low temperature operating conditions where the humid air thermophysical properties are close to those of dry air, the saturation vapor pressure at the brine and condensing plate temperatures are negligible compared to barometric pressure and the familiar Jakob’s dimensionless Nusselt–Rayleigh correlation for natural convection heat transfer appears to be valid, they both fail at higher operational temperatures. It appears that as far as Dunkle’s simplified model is concerned, this occurs not only owing to the first two counteracting effects but also to the effect of the dimensionless convective heat transfer correlation affecting also the accuracy of the refined model, which fails to predict precisely the natural convection conditions at higher Rayleigh numbers representing conditions of strong turbulence in the solar still cavity. Assuming a constant asymptotic value of the exponent n  = 1/3 which persists over a broad region of high Rayleigh numbers relevant to solar still operation, an improved value of the proportionality constant C around the value of 0.05 was estimated for the accurate prediction of measurements, at least as far as the available data from the literature is concerned.

[1]  G. Tiwari,et al.  Estimation of convective mass transfer in solar distillation systems , 1996 .

[2]  Vassilis Belessiotis,et al.  Transport phenomena and dynamic modeling in greenhouse-type solar stills , 2000 .

[3]  Jim A. Clark,et al.  The steady-state performance of a solar still , 1990 .

[4]  P. I. Cooper,et al.  Digital simulation of transient solar still processes , 1969 .

[5]  M. E. Khan,et al.  Simulation of convective mass transfer in a solar distillation process , 1997 .

[6]  Shruti Aggarwal,et al.  Convective mass transfer in a double-condensing chamber and a conventional solar still , 1998 .

[7]  Jürgen Rheinländer Numerical calculation of heat and mass transfer in solar stills , 1982 .

[8]  G. N. Tiwari,et al.  Computer modeling of passive/active solar stills by using inner glass temperature , 2003 .

[9]  G. N. Tiwari,et al.  Effect of the condensing cover's slope on internal heat and mass transfer in distillation: an indoor simulation , 2005 .

[10]  G. N. Tiwari,et al.  Effect of water depths on heat and mass transfer in a passive solar still: in summer climatic condition , 2006 .

[11]  D. Dropkin,et al.  Natural-Convection Heat Transfer in Liquids Confined by Two Horizontal Plates and Heated From Below , 1959 .

[12]  Rajendra Singh Adhikari,et al.  Estimation of mass‐transfer rates in solar stills , 1990 .

[13]  G. N. Tiwari,et al.  Effect of condensing cover material on yield of an active solar still: an experimental validation , 2008 .

[14]  P. I. Cooper,et al.  Some factors affecting the absorption of solar radiation in solar stills , 1972 .

[15]  G. N. Tiwari,et al.  Performance evaluation of a solar still by using the concept of solar fractionation , 2004 .

[16]  P. Tsilingiris Thermophysical and transport properties of humid air at temperature range between 0 and 100 °C , 2008 .

[17]  P. T. Tsilingiris,et al.  The influence of binary mixture thermophysical properties in the analysis of heat and mass transfer processes in solar distillation systems , 2007 .

[18]  M. Farid,et al.  New development in the theory of heat and mass transfer in solar stills , 1995 .

[19]  T. Unny,et al.  Free convective heat transfer across inclined air layers , 1976 .

[20]  G. N. Tiwari,et al.  Effect of water depth on internal heat and mass transfer for active solar distillation , 2005 .

[21]  Zhang Xiaoyan,et al.  A group of improved heat and mass transfer correlations in solar stills , 2002 .

[22]  G. N. Tiwari,et al.  New heat and mass transfer relations for a solar still , 1991 .

[23]  G. N. Tiwari,et al.  THERMAL MODELING OF PASSIVE AND ACTIVE SOLAR STILLS FOR DIFFERENT DEPTHS OF WATER BY USING THE CONCEPT OF SOLAR FRACTION , 2006 .

[24]  K.G.T. Hollands,et al.  Correlation equations for free convection heat transfer in horizontal layers of air and water , 1975 .