Recent studies have examined the rate of salt deposition by natural convection on a cylinder heated above the solubility temperature corresponding to the concentration of salt in the surrounding solution at conditions typical of the Supercritical Water Oxidation (SCWO) process (Hodes et al. [1,2], Hodes [3]). The total deposition rate of salt on the cylinder is the sum of the rate of deposition at the salt layer-solution interface (SLSI) formed on the cylinder and that within the porous salt layer. The rate of deposition at the SLSI cannot be computed without determining whether or not salt nucleates homogeneously in the adjacent (natural convection) boundary layer. A methodology to determine whether or not homogeneous nucleation in the boundary layer is possible is presented here. Temperature and concentration profiles in the boundary layer are computed under the assumption that homogeneous nucleation does not occur. If, under this assumption, supersaturation does not occur, homogeneous nucleation is impossible. If supersaturation is present, homogeneous nucleation may or may not occur depending on the amount of metastability the solution can tolerate. It is shown that the Lewis number is the critical solution property in determining whether or not homogeneous nucleation is possible and a simple formula is developed to predict the Lewis number below which homogeneous nucleation is impossible for a given solubility boundary and set of operating conditions. Finally, the theory is shown to be consistent with experimental observations for which homogeneous nucleation is absent or present.

1.
Hodes, M., Smith, K. A., Hurst, W. S., Bowers, Jr., W., Griffith, P., and Sako, K., 2002, “Solubilities and Deposition Rates in Aqueous Sulfate Solutions at Elevated Temperatures and Pressure,” submitted to Int. J. Heat Mass Transfer.
2.
Hodes, M., Smith, K. A., and Griffith, P., 2002, “A Natural Convection Model for the Rate of Salt Deposition from Near-Supercritical, Aqueous, Salt Solutions,” submitted to J. Heat Transfer.
3.
Hodes, M., 1998, “Measurements and Modeling of Deposition Rates from Near-Supercritical, Aqueous, Sodium Sulfate and Potassium Sulfate Solutions to a Heated Cylinder,” Ph.D. thesis, Massachusetts Institute of Technology, Cambridge, MA.
4.
Tester
,
J. W.
,
Holgate
,
H. R.
,
Armellini
,
F. J.
,
Webley
,
P. A.
,
Killilea
,
W. R.
,
Hong
,
G. T.
, and
Barner
,
H. E.
,
1991
, “
Supercritical Water Oxidation Technology: A Review of Process Development and Fundamental Research
,”
ACS Symp. Ser.
,
518
.
5.
Gloyna, E. F., and Li, L., 1998, “Supercritical Water Oxidation for Wastewater and Sludge Remediation,” Encyclopedia of Environmental Analysis and Remediation, R. A. Meyers, ed., John Wiley and Sons, Inc., pp. 4780–4797.
6.
Shaw, R. W., and Dahmen, N., “Destruction of Toxic Organic Materials Using Super-Critical Water Oxidation: Current State of the Technology,” Supercritical Fluids: Fundamentals and Applications, E. Kiran, P. G. Debenedetti and C. J. Peters, eds., Kluwer Academic Publishers, Dordrecht, The Netherlands.
7.
Hurst
,
W. A.
,
Hodes
,
M. S.
,
Bowers
, Jr.,
W.
,
Bean
,
V. E.
,
Maslar
,
J. E.
,
Smith
,
K. A.
, and
Griffith
,
P.
,
2002
, “
Optical Flow Cell and Apparatus for Solubility, Salt Deposition and Raman Spectroscopic Studies in Aqueous Solutions near the Water Critical Point
,”
J. Supercrit. Fluids
,
22
(
2
), pp.
157
166
.
8.
Butenhoff
,
T. J.
,
Goemans
,
M.
, and
Buelow
,
S. J.
,
1996
, “
Mass Diffusion Coefficients and Thermal Diffusivity in Concentrated NaNO3 Solutions
,”
J. Phys. Chem.
,
100
, pp.
5982
5992
.
9.
Lamb
,
W. J.
,
Hoffman
,
G. A.
, and
Jonas
,
J.
,
1981
, “
Self-Diffusion in Compressed Super-Critical Water
,”
J. Chem. Phys.
,
74
(
12
), pp.
6875
6880
.
10.
Fogler, H. S., 1992, Elements of Chemical Reaction Engineering, Prentice Hall.
11.
Armellini
,
F. J.
,
Tester
,
J. W.
, and
Hong
,
G. T.
,
1994
, “
Precipitation of Sodium Chloride and Sodium Sulfate in Water from Sub- to Supercritical Conditions: 150 to 550°C, 100 to 300 bar
,”
J. Supercrit. Fluids
,
7
, pp.
147
158
.
12.
Harvey, A. H., Peskin, A. P., and Klein, S. A., 2000, “NIST/ASME Steam Properties: Version 2.2,” U.S. Department of Commerce.
13.
Gebhart
,
B.
, and
Pera
,
L.
,
1971
, “
The Nature of Vertical Natural Convection Flows Resulting from the Combined Buoyancy Effects of Thermal and Mass Diffusion
,”
Int. J. Heat Mass Transf.
,
14
, pp.
2025
2050
.
14.
Gebhart, B., Jaluria, Y., Mahajan, R., and Sammakia, B., 1988, Buoyancy-Induced Flows and Transport, Hemisphere Publishing Corporation.
15.
Abramowitz, M., and Stegun, I. A., 1965, Handbook of Mathematical Functions, Dover Publications.
16.
Ostrach, S., 1953, “An Analysis of Laminar Free-Convection Flow and Heat Transfer about a Flat Plate Parallel to the Direction of the Generating Body Force,” Technical Report 1111, NACA.
1.
Le`ve^que
,
J.
,
1928
,
Annales des Mines
,
12
(
13
), pp.
305
305
and
2.
12(13), pp. 381.
1.
Marshall
,
W. L.
,
Gill
,
J. S.
, and
Secoy
,
C. H.
,
1954
, “
Phase Equilibria of Uranium Trioxide and Aqueous Hydrofluoric Acid in Stochiometric Concentrations
,”
J. Am. Chem. Soc.
, p.
4279
4279
.
2.
Linke, W., 1958, Solubilities of Inorganic and Metal-Organic Compounds: A Compilation of Solubility Data from the Periodical Literature, D. Van Nostrand Company Inc.
3.
Stephen, H., and Stephen, T., 1963, Solubilities of Inorganic and Organic Compounds: Volume 1-Binary Systems, Macmillan.
4.
Friend
,
J. A. N.
,
1932
, “
The Selenates of Lanthanum and Their Solubilities in Water
,”
J. Chem. Soc.
, p.
1597
1597
.
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