Heat and mass transfer in hollow-fiber modules for direct contact membrane distillation: Integral transforms solution and parametric analysis

被引:12
|
作者
Lisboa, Kleber Marques [1 ,2 ]
Brito de Souza, Jose Roberto [1 ,2 ]
Naveira-Cotta, Carolina Palma [1 ,2 ]
Cotta, Renato Machado [1 ,2 ,3 ,4 ]
机构
[1] Univ Fed Rio de Janeiro, LabMEMS Mech Engn Dept, Lab Nano & Microfluid & Microsyst, Rio De Janeiro, RJ, Brazil
[2] Univ Fed Rio de Janeiro, Nanoengn Dept, POLI & COPPE, Rio De Janeiro, RJ, Brazil
[3] Univ Fed Rio de Janeiro, Technol Ctr, NIDES CT, Interdisciplinary Nucleus Social Dev, Rio De Janeiro, RJ, Brazil
[4] Brazilian Navy, DGDNTM, Gen Directorate Nucl & Technol Dev, Rio De Janeiro, Brazil
关键词
Desalination; Direct contact membrane distillation; Waste heat recovery; Single domain formulation; Generalized integral transform technique; TRANSPORT; DESALINATION; MODEL; DCMD;
D O I
10.1016/j.icheatmasstransfer.2019.104373
中图分类号
O414.1 [热力学];
学科分类号
摘要
This work reports a heat and mass transfer analysis of direct contact membrane distillation (DCMD), aiming at predicting its performance in water desalination with hollow-fiber membrane modules. A single-fiber model is proposed to simulate the simultaneous heat and mass transfer in DCMD for a hollow-fibers bundle, and the efficiency of the desalination process is assessed. The problem for a single membrane is handled through the hybrid numerical-analytical approach known as the Generalized Integral Transform Technique (GITT). A comparison of the numerical results obtained with the proposed model and both theoretical and experimental results from the literature is carried out. A prediction of the performance of a hollow-fiber DCMD module is then presented and paths for further improvement are discussed.
引用
收藏
页数:7
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