Towards sustainable circular brine reclamation using seawater reverse osmosis, membrane distillation and forward osmosis hybrids: An experimental investigation

2021 ◽  
Vol 293 ◽  
pp. 112836
Author(s):  
Hyuk Soo Son ◽  
Sofiane Soukane ◽  
Junggil Lee ◽  
Youngjin Kim ◽  
Young-Deuk Kim ◽  
...  
2006 ◽  
Vol 60 (6) ◽  
Author(s):  
K. Karakulski ◽  
M. Gryta ◽  
M. Sasim

AbstractApplication of ultrafiltration, nanofiltration, reverse osmosis, membrane distillation, and integrated membrane processes for the preparation of process water from natural water or industrial effluents was investigated. A two-stage reverse osmosis plant enabled almost complete removal of solutes from the feed water. High-purity water was prepared using the membrane distillation. However, during this process a rapid membrane fouling and permeate flux decline was observed when the tap water was used as a feed. The precipitation of deposit in the modules was limited by the separation of sparingly soluble salts from the feed water in the nanofiltration. The combined reverse osmosis—membrane distillation process prevented the formation of salt deposits on the membranes employed for the membrane distillation. Ultrafiltration was found to be very effective removing trace amounts of oil from the feed water. Then the ultrafiltration permeate was used for feeding of the remaining membrane modules resulting in the total removal of oil residue contamination. The ultrafiltration allowed producing process water directly from the industrial effluents containing petroleum derivatives.


2021 ◽  
Vol 4 (1) ◽  
Author(s):  
S.-J. Im ◽  
S. Jeong ◽  
A. Jang

AbstractCurrently, desalination is limited by high energy consumption and high operational and maintenance costs. In this study, a new concept of a hollow fiber forward osmosis (HFFO)-based infinity desalination process with minor environmental impacts (free-energy intake and no pretreatment or brine discharge) is suggested. To evaluate the concept, an element-scale HFFO was conducted in both conventional FO and pressure-assisted FO modes, simulating a submerged HFFO operation. In the HFFO test, the impacts of several operating conditions on the performance of the HFFO were investigated to select the best case. Based on these results, the energy costs were calculated and compared with those of a hybrid FO–seawater reverse osmosis (SWRO) process. The HFFO showed a high dilution rate of the draw solution (up to approximately 400%), allowing the downstream SWRO process to operate at 25 bar with the same permeate volume production (recovery rate of 60%). Consequently, the HFFO-based infinity desalination process has an annual energy revenue of 183.83 million USD, compared with a stand-alone two-stage RO process based on a 100,000 m3/day plant.


Desalination ◽  
2017 ◽  
Vol 403 ◽  
pp. 153-160 ◽  
Author(s):  
Manvoudou Pissibanganga Ordelia Gwenaelle ◽  
Jungwoo Jung ◽  
Yongjun Choi ◽  
Sangho Lee

Desalination ◽  
1980 ◽  
Vol 32 ◽  
pp. 25-31 ◽  
Author(s):  
J.E. Cadotte ◽  
R.J. Petersen ◽  
R.E. Larson ◽  
E.E. Erickson

Desalination ◽  
2013 ◽  
Vol 311 ◽  
pp. 24-30 ◽  
Author(s):  
Axel Ettori ◽  
Emmanuelle Gaudichet-Maurin ◽  
Pierre Aimar ◽  
Christel Causserand

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