scholarly journals Performance evaluation of the different nano-enhanced polysulfone membranes via membrane distillation for produced water desalination in Sert Basin-Libya

2020 ◽  
Vol 13 (4) ◽  
pp. 5118-5136
Author(s):  
Osamah M.A. Shahlol ◽  
Heba Isawi ◽  
Mohamed G. El-Malky ◽  
Abd El-Hameed M. Al-Aassar ◽  
Adel El zwai
Water ◽  
2020 ◽  
Vol 12 (12) ◽  
pp. 3560
Author(s):  
Jingbo Wang ◽  
Dian Tanuwidjaja ◽  
Subir Bhattacharjee ◽  
Arian Edalat ◽  
David Jassby ◽  
...  

Herein, we report on the performance of a hybrid organic-ceramic hydrophilic pervaporation membrane applied in a vacuum membrane distillation operating mode to desalinate laboratory prepared saline waters and a hypersaline water modeled after a real oil and gas produced water. The rational for performing “pervaporative distillation” is that highly contaminated waters like produced water, reverse osmosis concentrates and industrial have high potential to foul and scale membranes, and for traditional porous membrane distillation membranes they can suffer pore-wetting and complete salt passage. In most of these processes, the hard to treat feed water is commonly softened and filtered prior to a desalination process. This study evaluates pervaporative distillation performance treating: (1) NaCl solutions from 10 to 240 g/L at crossflow Reynolds numbers from 300 to 4800 and feed-temperatures from 60 to 85 °C and (2) a real produced water composition chemically softened to reduce its high-scale forming mineral content. The pervaporative distillation process proved highly-effective at desalting all feed streams, consistently delivering <10 mg/L of dissolved solids in product water under all operating condition tested with reasonably high permeate fluxes (up to 23 LMH) at optimized operating conditions.


2015 ◽  
Vol 57 (24) ◽  
pp. 10995-11007 ◽  
Author(s):  
Khaled Okiel ◽  
Abdel Hameed M. El-Aassar ◽  
Tarek Temraz ◽  
Salah El-Etriby ◽  
Hosam A. Shawky

2013 ◽  
Vol 781-784 ◽  
pp. 2084-2086
Author(s):  
Guo Fu Sun ◽  
Jing Li Xu ◽  
Chun Hua Sui ◽  
Hong Yan Si

An air sweep vacuum membrane distillation process was used to treat brackish water desalination. The only operating parameter of the apparatus is the sweeping air flow rate. The effect of sweeping air flow rate on desalination was observed. The produced/condensed water rate was about 2.5 g/h for the PP module. The conductivity of produced water was about 92 μs·cm-1, the salt rejection was above 95%.


2020 ◽  
Vol 135 ◽  
pp. 106729 ◽  
Author(s):  
Alanood A. Alsarayreh ◽  
M.A. Al-Obaidi ◽  
A.M. Al-Hroub ◽  
R. Patel ◽  
I.M. Mujtaba

Fibers ◽  
2018 ◽  
Vol 7 (1) ◽  
pp. 1 ◽  
Author(s):  
Marek Gryta

Only nonwetted porous membranes can be used in membrane distillation. The possibility of application in this process the capillary polypropylene membranes manufactured by thermally-induced phase separation was studied. The performance of a few types of membranes available commercially was presented. The resistance of the membranes to wetting was tested in the continuous process of water desalination. These studies were carried out for 1000 h without module cleaning. The presence of scaling layer on the membranes surface was confirmed by Scanning Electron Microscope observations. Both the permeate flux and distillate conductivity were almost not varied after the studied period of time, what indicates that the used membranes maintained their nonwettability, and the negative influence of scaling was limited. The role of surface porosity on the pore wetting and influence of membrane wettability on the quality of the distillate obtained were discussed.


Desalination ◽  
2015 ◽  
Vol 366 ◽  
pp. 121-129 ◽  
Author(s):  
Hung C. Duong ◽  
Allan R. Chivas ◽  
Bart Nelemans ◽  
Mikel Duke ◽  
Stephen Gray ◽  
...  

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