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Annual Report 2006 - Plataforma Solar de Almería

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ENVIRONMENTAL APPLICATIONS OF SOLAR ENERGY<br />

Duration: March 2002 – February <strong>2006</strong><br />

Motivation: Seawater <strong>de</strong>salination is one of the possible solutions to the<br />

severe water shortage problem that our planet is going to un<strong>de</strong>rgo during the<br />

first half of this century, a problem which is not exclusively in <strong>de</strong>veloping<br />

countries, as the appearance of persistent seasonal droughts are more and<br />

more frequent in some regions of <strong>de</strong>veloped countries.<br />

In spite of all of the advances of the last few <strong>de</strong>ca<strong>de</strong>s, seawater <strong>de</strong>salination<br />

technologies continue being intensive fossil-fuel consumers. In the present<br />

world framework, with growing instability of oil market prices and environmental<br />

<strong>de</strong>mands <strong>de</strong>rived fro compliance with the Kyoto Protocol, sustainable<br />

<strong>de</strong>salination must unavoidably be arrived at through improved efficiency<br />

of the technologies involved as well as the use of renewable energy resources.<br />

The AQUASOL project faces both options by using solar thermal energy as the<br />

renewable energy resource and contributes to increasing the thermal efficiency<br />

of the multi-effect distillation process. The environmental impact of the<br />

<strong>de</strong>salination process has also been reduced by recovering the salt contained in<br />

the brine.<br />

Purposes: The main goal of the AQUASOL project is the <strong>de</strong>velopment of a hybrid<br />

solar/gas seawater <strong>de</strong>salination technology based on multi-effect distillation<br />

(MED) which also meets the principles of energy efficiency, low cost and<br />

zero discharge.<br />

Objectives met in <strong>2006</strong>: The implementation of the different subsystems was<br />

completed during this period and their testing un<strong>de</strong>r real weather conditions<br />

was begun at the PSA facilities (MED Plant, heat pump and solar field) and the<br />

Greek saltern Hellenic Saltworks on the Island of Lesbos (<strong>Solar</strong> Dryer).<br />

The AQUASOL system has three different operating mo<strong>de</strong>s <strong>de</strong>pending on<br />

the origin of the thermal energy:<br />

• <strong>Solar</strong>-only mo<strong>de</strong>: the thermal energy supply to the first effect of the<br />

distillation plant comes exclusively from the solar collector field.<br />

• Fossil-only mo<strong>de</strong>: the double-effect heat pump supplies all of the energy<br />

required by the distillation plant<br />

• Hybrid mo<strong>de</strong>: the energy supply comes from both the heat pump and<br />

the solar field. Two different operating philosophies are consi<strong>de</strong>red: in<br />

the first the heat pump works continuously 24 hours a day supplying<br />

the minimum 30%, while in the second it starts up and stops, <strong>de</strong>pending<br />

on the solar resource availability.<br />

The operating and maintenance experience with the AQUASOL system has<br />

been shown to be highly reliable, with no important problems being recor<strong>de</strong>d<br />

during testing. The solar collector field has <strong>de</strong>monstrated an average daily<br />

efficiency (ratio between the thermal power <strong>de</strong>livered to the storage tanks<br />

and the global solar radiation inci<strong>de</strong>nt on the tilted surface of the collectors)<br />

of 48%. The plant performance factor (kg distillate produced per 2316 kJ<br />

thermal energy supplied to the system) in solar-only mo<strong>de</strong> is over 10.<br />

As a result of evaluation of the new absorption heat puma after the first<br />

tests, it was <strong>de</strong>ci<strong>de</strong>d to change the initial configuration of parallel flow to series<br />

flow, to improve the controllability of the equipment, especially during<br />

transients. After this modification, the unit showed excellent behavior, increasing<br />

the plant performance factor from 10 to over 20, which is a 100%<br />

increase in thermal process efficiency. In hybrid mo<strong>de</strong>, it should be mentioned<br />

that the absorption pump showed strong thermal inertia, mainly due to the<br />

fact that the maximum power <strong>de</strong>livered by the steam boiler is much more<br />

than required by the pump un<strong>de</strong>r stationary conditions. The best results were<br />

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