2014
DOI: 10.1016/j.desal.2013.11.037
|View full text |Cite
|
Sign up to set email alerts
|

Study on a new air-gap membrane distillation module for desalination

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

1
24
0

Year Published

2015
2015
2019
2019

Publication Types

Select...
4
3
1

Relationship

0
8

Authors

Journals

citations
Cited by 71 publications
(25 citation statements)
references
References 21 publications
1
24
0
Order By: Relevance
“…Among the proposed technologies, the non-isothermal process membrane distillation (MD) has emerged as an important process for desalination of high saline aqueous solutions and treatment of brines [8][9][10][11][12][13][14][15]. One of the main advantages of MD over other membrane processes in the field of desalination is its capability to operate under high salt concentrations (i.e.…”
Section: Introductionmentioning
confidence: 99%
“…Among the proposed technologies, the non-isothermal process membrane distillation (MD) has emerged as an important process for desalination of high saline aqueous solutions and treatment of brines [8][9][10][11][12][13][14][15]. One of the main advantages of MD over other membrane processes in the field of desalination is its capability to operate under high salt concentrations (i.e.…”
Section: Introductionmentioning
confidence: 99%
“…and T c,in (17,20,25 • C). For the numerical model predictions, an effective gap conductivity of k gap = 0.6 W/m-K and effective gap thickness of 1 mm were used.…”
Section: Validationmentioning
confidence: 99%
“…shown to be capable of achieving higher GORs [5,15,16,17]. Permeate Gap MD is also referred to as Water Gap and Liquid Gap MD.…”
Section: Energy Efficiencymentioning
confidence: 99%
“…For both MD modes very high rejection factors ranging from 99 to 100% could be obtained but the AGMD production is higher than that of DCMD, using the same membrane [8]. Experiments on seawater desalination by AGMD were conducted by Kubota et al [9] temperature drop and local water vapor permeate flux distribution have considered by Pingli Li et al [46] using a porous Polytetrafluoroethylene (PTFE) membrane. The obtained AGMD permeate fluxes of the PTFE membrane were as high as a maximum flux of 10 kg·h.…”
Section: Introductionmentioning
confidence: 97%
“…The obtained AGMD permeate fluxes of the PTFE membrane were as high as a maximum flux of 10 kg·h. Temperature drop and local water vapor permeate flux distribution have been considered by Li et al [46] which showed that the local flux drop and temperature drop of water vapor permeate were much larger at the upper part than those at the lower part of the membrane module in the hot feed side.…”
Section: Introductionmentioning
confidence: 98%