Optimization of chemical cleaning of a reverse osmosis membrane from a desalination plant by means of two-step static tests

2014 ◽  
Vol 55 (12) ◽  
pp. 3367-3379 ◽  
Author(s):  
B. Garcia-Fayos ◽  
J.M. Arnal ◽  
A. Gimenez ◽  
S. Alvarez-Blanco ◽  
M. Sancho
2009 ◽  
Vol 34 (5) ◽  
pp. 1535-1557 ◽  
Author(s):  
S.S. MADAENI ◽  
A. SASANIHOMA ◽  
S. ZERESHKI

2016 ◽  
Vol 162 ◽  
pp. 171-179 ◽  
Author(s):  
Sanghyun Jeong ◽  
Gayathri Naidu ◽  
Robert Vollprecht ◽  
TorOve Leiknes ◽  
Saravanamuthu Vigneswaran

Desalination ◽  
2021 ◽  
Vol 500 ◽  
pp. 114830
Author(s):  
Yong-Gu Lee ◽  
Sangwon Kim ◽  
Jaegwan Shin ◽  
Hojung Rho ◽  
Young Mi Kim ◽  
...  

1991 ◽  
Vol 23 (7-9) ◽  
pp. 1629-1638 ◽  
Author(s):  
Yoshiaki Suzuki ◽  
Takeshi Minami

The purpose of this survey is to explore ways of reclaiming wastewater to produce high-quality low-cost water for recreational reuse by using a reverse osmosis membrane in advanced wastewater treatment. We examined membrane modules that were able to be used for wastewater treatment in fiscal year 1988. The parameters used to evaluate the membrane were the permeate quantity, permeate water quality, flux decline coefficient, and recovery rate of the permeate quantity by chemical cleaning. As a result, spiral-wound polyvinyl alcohol composite membrane and hollow-fiber cellulose triacetate reverse osmosis membrane were found to be of high practical value. The permeate through these membranes was colorless, transparent, and odorless, with an appearance equivalent to city water. The rejection rate of the fecal coliform group was 100% and the COD of the permeate was 1-2 mg/l, with a chromaticity of 1 degree or less and a phosphorus content of 0.01 mg/l. Under the same pressure condition, these membranes provided three times more permeate quantity than a conventional acetyl cellulose membrane having a time-proven performance. Moreover, these membranes were sufficiently resistant to fouling that they can recover to a 100% permeate quantity by chemical cleaning when they were fouled.


Desalination ◽  
2010 ◽  
Vol 257 (1-3) ◽  
pp. 80-86 ◽  
Author(s):  
S.S. Madaeni ◽  
S. Samieirad

Author(s):  
H. K. Plummer ◽  
E. Eichen ◽  
C. D. Melvin

Much of the work reported in the literature on cellulose acetate reverse osmosis membranes has raised new and important questions with regard to the dense or “active” layer of these membranes. Several thickness values and structures have been attributed to the dense layer. To ensure the correct interpretation of the cellulose acetate structure thirteen different preparative techniques have been used in this investigation. These thirteen methods included various combinations of water substitution, freeze drying, freeze sectioning, fracturing, embedding, and microtomy techniques with both transmission and scanning electron microscope observations.It was observed that several factors can cause a distortion of the structure during sample preparation. The most obvious problem of water removal can cause swelling, shrinking, and folds. Improper removal of embedding materials, when used, can cause a loss of electron image contrast and, or structure which could hinder interpretation.


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