A model for calculation and optimization of seawater desalination process is presented. In this process, temperature difference between the upper and the lower strata of the ocean is utilized in producing fresh water, by evaporating the warm surface seawater at a reduced pressure and then condensing the generated steam by using the colder seawater drawn from the depth of the ocean to produce distilled water. In order to make the optimization process realistic, the developed model takes into consideration the characteristics of the proposed location such as temperature and density variation with depth, seabed topography, and subsequently the actual lengths of the cold and the warm seawater intake pipes. This article gives details of the process and investigates on the influence of various parameters on its economics. As electricity is the sole source of energy used, the objective function was taken as the specific energy, i.e., the amount of electrical energy required for producing a unit mass of distilled water. Results indicate that distilled water can be produced at a value as low as 5.5 kWh per ton, which makes the process competitive with most of the existing desalination technologies.

References

1.
Gleick
,
P. H.
,
2002
, “
Dirty Water: Estimated Deaths from Water-Related Diseases 2000–2020
,” Pacific Institute for Studies in Development, Environment, and Security. Available at: http://www.pacinst.org/wp-content/uploads/sites/21/2013/02/water_related_deaths_report3.pdf
2.
World Health Organization (WHO
),
2000
, “
Global Water Supply and Sanitation Assessment 2000 Report
.” Available at: http://www.who.int/water_sanitation_health/monitoring/jmp2000.pdf
3.
Lisa
,
H.
, President of (IDA) in November 2009 Talk, “
The Current State of Desalination
,” International Desalination Association
5.
Vega
,
L. A.
,
2002
, “
Ocean Thermal Energy Conversion Primer
,”
Mar. Technol. Soc. J.
,
36
(
4
), pp.
25
35
.10.4031/002533202787908626
6.
Ikegami
,
Y.
,
Urata
,
K.
,
Bando
,
A.
,
Wajima
,
T.
,
Ohto
,
K.
,
Nakaoka
,
T.
,
Tabuchi
,
K.
, and
Kamano
,
T.
,
2005
, “
Oceanic Observation and Investigation for Utilization of Ocean Energy in the Fiji
,”
Proceedings of the 15th International Offshore and Polar Engineering Conference
, Seoul, Korea.
7.
Mutair
,
S.
, and
Ikegami
,
Y.
,
2010
, “
Experimental Investigation on the Characteristics of Flash Evaporation From Superheated Water Jets for Desalination
,”
Desalination
,
251
, pp.
103
111
.10.1016/j.desal.2009.09.136
8.
Mutair
,
S.
, and
Ikegami
,
Y.
,
2009
, “
Experimental Study on Flash Evaporation From Superheated Water Jets: Influencing Factors and Formulation of Correlation
,”
Int. J. Heat Mass Transfer
,
52
(
23–24
), pp.
5643
5651
.10.1016/j.ijheatmasstransfer.2009.05.009
9.
Stoughton
,
R. W.
, and
Lietzke
,
M. H.
,
1967
, “
Thermodynamic Properties of Sea Salt Solutions
,”
J. Chem. Eng. Data
,
12
(
1
), pp.
101
104
.10.1021/je60032a032
10.
Bharathan
,
D.
,
Parsons
,
B. K.
, and
Althof
,
J. A.
,
1988
, “
Direct-Contact Condensers for Open-Cycle OTEC Applications
,” National Renewable Energy Laboratory Report ERI/TP-252-3108 for DOE Contract No. DE-AC02-83CH10093.
11.
Taborek
,
J.
,
1988
,
Process Heat Exchangers
,
Hemisphere
,
Washington, D. C
.
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