A method to assess the cost effectiveness of large solar desalination
systems is presented. This method was used to investigate the effect o
f site, technological and economical parameters. The comparative cost
of full and partial solar desalting systems was also evaluated by a mo
re detailed case study of 20,000 m(3)/d and 200,000 m(3)/d systems. Tw
o solar technologies were considered: salt gradient solar ponds and du
al-purpose solar electric power stations supplying low pressure steam
to thermal desalting systems. The solar field could use any concentrat
ing collector technology such as parabolic troughs, dishes or helelios
tats. At the present state of heat storage technology, back-up of exte
rnal fuel will have to be used for continuous operation. Two desalting
technologies were considered: multi-effect distillation(MED) and hybr
id MED/SWRO systems. The first uses thermal process heat from the sola
r field and a relatively small supply of commercial electricity for pu
mping purposes. The second uses solar energy only for the MED portion
of the hybrid system while the SWRO portion uses commercial electricit
y. The hybrid concept represents therefore a partial rather than a ful
l solar system. Solar pond powered desalting systems were found to hav
e a considerable potential to be cost effective if favorable site cond
itions exist. Only for very low specific solar field cost and/or high
commercial electricity prices would the fully solar options be more co
st competitive than the partial solar options.