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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.
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页数:7
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