使用相变纳米材料的斜阶式太阳能海水淡化的功能和财务分析

Ahmed Mahal, Maysoon Al-Haideri, Anas Alkhouri, A. Obaidullah, Meitao Duan
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摘要

近几十年来,由于水资源短缺,科学家们开始关注太阳能海水淡化技术。本研究在考虑各种相变材料 (PCM) 的同时,还研究了具有倾斜步骤的太阳能海水淡化系统。研究结果表明,PCM 的加入普遍提高了太阳能海水淡化系统的生产率。此外,还将纳米颗粒与 PCM 结合使用,这是目前用来提高这些系统效率的一种流行技术。目前的研究涉及利用能量守恒方程对太阳能海水淡化系统进行瞬态建模。这些方程使用 ODE23s 阶的 Runge-Kutta 技术求解。计算了盐水、玻璃罩吸水板和 PCM 在每个时间段的温度。在不使用换相器的情况下,淡水的生产率约为 5.15 kg/m2-h。石蜡、正 PCM I、正 PCM III、正 PCM II 和硬脂酸的相应质量流量分别为 22.9、28.9、5.9、11.9 和 73 kg/m2-h。除硬脂酸外,其他 PCM 在环境温度达到 29° 左右时都表现出相似的能效。然而,在温度超过 29° 时,正 PCM II 的性能优于其他 PCM。
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Functional and financial analysis of an inclined step solar desalination using phase change nanomaterials
Recent decades have seen a shortage of water, which has led scientists to concentrate on solar desalination technologies. The present study examines the solar water desalination system with inclined steps, while considering various phase change materials (PCMs). The findings suggest that the incorporation of PCM generally enhances the productivity of the solar desalination system. Additionally, the combination of nanoparticles has been used to PCM, which is a popular technique utilized nowadays to improve the efficiency of these systems. The current investigation involves the transient modeling of a solar water desalination system, utilizing energy conservation equations. The equations were solved using the Runge–Kutta technique of the ODE23s order. The temperatures of the salt water, the absorbent plate of the glass cover, and the PCM were calculated at each time. Without a phase changer, the rate at which fresh water is produced is around 5.15 kg/m2·h. The corresponding mass flow rates of paraffin, n-PCM I, n-PCM III, n-PCM II, and stearic acid are 22.9, 28.9, 5.9, 11.9, and 73 kg/m2·h. PCMs, with the exception of stearic acid, exhibit similar energy efficiency up to an ambient temperature of around 29°. However, at temperatures over 29°, n-PCM II outperforms other PCM.
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