太阳能/混合海水淡化系统的数值模拟

Y. Aldali, K. Morad, Nabil A. S. Elminshawy, F. Ahwide
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摘要

建立了预测太阳能/混合海水淡化系统性能的数学模型。本文研究的新型混合海水淡化系统由多级热蒸汽压缩(TVC)系统和螺旋缠绕气隙膜海水淡化(AGMD)装置组成。TVC系统各蒸发器级排出的热卤水作为AGM装置的热进料。将直接产汽的抛物槽集热器(ptc)场视为太阳能系统。在太阳能时,太阳能场产生一部分动力蒸汽需要运行TVC系统,而其余部分由锅炉产生。研究结果表明:TVC系统蒸馏水产出率为3415 L/h (20.56 L/h.m2), AGMD装置蒸馏水产出率为150 L/h (6.944 L/h.m2),利用ptc气田每年可节约天然气24吨。经济研究表明,利用ptc油田产生部分动力蒸汽的效益/成本比为2.1,AGMD装置生产1立方米蒸馏水的成本为0.9美元,而其他类型的海水淡化系统的生产成本为0.45-2.51美元。
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Numerical Simulation of the Integrated Solar/Hybrid Desalination System
A mathematical model is developed to predict the performance of the integrated solar/hybrid desalination system. The novel hybrid desalination system in this study consists of multi-stage thermal vapor compression (TVC) system and spiral wound air-gap membrane desalination (AGMD) units. The hot brine rejected from each evaporator stage of TVC system is used as the hot feed to the AGM unit. The parabolic trough collectors (PTCs) fild with direct steam generation was considered as solar system. At solar time, the solar fild generates a portion of motive steam required to operate the TVC system while the remaining part is generated by the boiler. Th results of this study show that the rate of distilled water from TVC system is 3415 L/h (20.56 L/h.m2) and from the AGMD units is 150 L/h (6.944 L/h.m2) and the annual saving of natural gas (NG) consumption by using PTCs fild is 24 tons. Th economic study has indicated that the benefi/cost ratio from of the use of PTCs fild to generate a portion of motive steam is 2.1 and the production cost of 1 m3 of distilled water from AGMD units is 0.9 $ in comparison with 0.45-2.51 $ from diffrent types of water desalination systems.
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