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Annual Report 2006 - Plataforma Solar de Almería

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PLATAFORMA SOLAR DE ALMERÍA<br />

Motivation: Desalination is an intensive energy consumer; in reverse osmosis<br />

seawater <strong>de</strong>salination systems, this consumption is around 3.5 kWh/m 3 . Taking<br />

into account that 2 10 6 m 3 /day are distilled in Spain, the need for <strong>de</strong>veloping<br />

sustainable and economically feasible <strong>de</strong>salination technologies is unquestionable.<br />

The solar reverse osmosis plants in operation to date are based<br />

on photovoltaic technology. The use of solar thermal energy for this process<br />

would enable better use to be ma<strong>de</strong> of the solar resource and less environmental<br />

impact once the problems of waste involved in the use of batteries<br />

required for photovoltaics is eliminated.<br />

Purposes: The main goal of the OSMOSOL project is the <strong>de</strong>velopment of an<br />

innovative technology based on solar thermal energy applied to the reverse<br />

osmosis <strong>de</strong>salination process which complies at the same time with the principles<br />

of environmental sustainability and economic feasibility. To do this it is<br />

inten<strong>de</strong>d to use thermal energy collected and concentrated in a solar <strong>de</strong>vice to<br />

feed a thermodynamic cycle based on a fluid that evaporates at a relatively<br />

low temperature and which, hooked up to a turbo-compressor system, allows<br />

direct transformation of the thermal energy into mechanical energy required<br />

by the osmosis process.<br />

Figure 4.16 Generic reverse osmosis system hooked up to a solar driver<br />

Objectives met in <strong>2006</strong>: During the first year of the project, low and mediumtemperature<br />

solar thermal collectors were thoroughly reviewed from the point<br />

of view of their application to <strong>de</strong>salination processes.<br />

Once certain solar organic Rankine cycles had been selected, we procee<strong>de</strong>d<br />

to choose from among the solar collectors compiled in the previous activity,<br />

those which best adapted to the conditions <strong>de</strong>limited by the thermodynamic<br />

cycle mentioned above. Four stationary solar collectors and two parabolictrough<br />

collectors meeting the technical and functional specifications were preselected<br />

for analysis of the solar power cycle, which was done employing up<br />

to 22 different working fluids.<br />

92

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