首页> 外文会议>NATO Advanced Research Workshop on Solar Desalination for the 21st Century; 20060223-25; Hammamet(TN) >OPTIMIZING COUPLING SMALL DESALINATION UNITS TO SOLAR COLLECTORS: A CASE STUDY
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OPTIMIZING COUPLING SMALL DESALINATION UNITS TO SOLAR COLLECTORS: A CASE STUDY

机译:优化小型除盐装置与太阳能集热器的耦合:案例研究

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The south Mediterranean area is suffering from lack of drinking water. However, brackish water is abundant in these regions. Desalination of such water can be a solution to provide the needs of the local populations (less than 10 m~3/day). Different solutions for brackish water desalination have been developed and many prototypes have been built and tested. Bourouni et al. (1999) developed a water desalination plant based on Aero-Evapo-Condensation Process (AECP). A prototype was built and tested in the region of Kebili in the south of Tunisia. A geothermal brackish water source was used to feed the unit. Promising results were found, since the cost of water was reduced to 1.2 USD per cubic meter of fresh water (Bourouni et al, 1999). The present study shows that the geothermal source can be replaced by solar preheated water. The efficiency of the whole system can be improved by using air flat-plate solar collectors to preheat the air entering the evaporator of the AEC system. Warm air has a higher evaporative capacity than ambient air, and thus, the evaporation of brackish water will be faster and more efficient. In this paper we present a methodology to obtain the best configuration of coupling solar energy to the desalination unit and to optimize the surface collectors used to preheat water and air. TRNSYS simulations are held to predict the performances of the new design of the system. A life cycle cost analysis of the new system design is held to evaluate the cost of a cubic meter of fresh water produced by this innovative process. Different configurations of the plant are studied by detailed simulations. For a small unit producing 3 m~3 of fresh water per day, the cost obtained is as low as 1.58 USD per cubic meter of fresh water produced.
机译:地中海南部地区缺乏饮用水。但是,这些地区咸水丰富。对此类水进行脱盐处理可以满足当地居民的需求(每天少于10 m〜3)。已经开发了用于咸水淡化的不同解决方案,并且已经建造和测试了许多原型。 Bourouni等。 (1999年)开发了一种基于航空蒸发凝结工艺(AECP)的海水淡化厂。在突尼斯南部的基比利地区建造并测试了一个原型。用地热微咸水源给该单元供料。由于水的成本降低到每立方米淡水1.2美元(Bourouni等,1999),因此发现了有希望的结果。本研究表明,地热源可以用太阳能预热水代替。通过使用空气平板太阳能集热器预热进入AEC系统蒸发器的空气,可以提高整个系统的效率。温暖的空气具有比周围空气更高的蒸发能力,因此,微咸水的蒸发将更快,更有效。在本文中,我们提出一种方法,以获取将太阳能耦合至脱盐装置的最佳配置,并优化用于预热水和空气的表面收集器。进行TRNSYS仿真可以预测系统新设计的性能。进行了新系统设计的生命周期成本分析,以评估此创新过程产生的立方米淡水成本。通过详细的模拟研究了工厂的不同配置。对于每天生产3m〜3淡水的小机组,所获得的成本低至每立方米淡水1.58美元。

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