Direct contact membrane distillation system for waste heat recovery: Modelling and multi-objective optimization

被引:57
|
作者
Long, Rui [1 ]
Lai, Xiaotian [1 ]
Liu, Zhichun [1 ]
Liu, Wei [1 ]
机构
[1] Huazhong Univ Sci & Technol, Sch Energy & Power Engn, 1037 Luoyu Rd, Wuhan 430074, Hubei, Peoples R China
基金
中国国家自然科学基金;
关键词
Direct contact membrane distillation; Modelling; Heat recovery; Multi-objective optimization; MASS-TRANSFER; NUMERICAL-SIMULATION; THERMAL-ENERGY; PERFORMANCE; DESALINATION; MODULES; FLUX; EFFICIENCY; CYCLE; FLOW;
D O I
10.1016/j.energy.2018.02.027
中图分类号
O414.1 [热力学];
学科分类号
摘要
Direct contact membrane distillation (DCMD) is an alternative technology to utilize the low temperature waste heat source for water supply. In this paper, we proposed a modified model characterizing the heat and mass transfer in the DCMD, which was validated by a great accordance with the experiment data. For evaluating the performance of a DCMD system with heat recovery, gain output ration (GOR) and mass recovery rate are two main criteria, however, they could not achieve their maximum values simultaneously. To achieve such a compromise, a multi-objective optimization considering both the water recovery rate and GOR was conducted. Besides, the GOR. mass recovery rate and thermal efficiency under single-objective optimization methods were calculated and compared. Compared to the results under the maximum GOR, the increase magnitude of water mass recovery rate under the multi-objective optimization override the decrease magnitude of GOR. Compared with the performance under the single-objective optimization for transmembrane water flux, the transmembrane water flux under the multi-objective optimization was reduced by only 6.7%, but the GOR is increased by 83.2%. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1060 / 1068
页数:9
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