Crossflow filtration units

1994 ◽  
Vol 31 (1) ◽  
pp. 16
Keyword(s):  
2018 ◽  
Author(s):  
Richard C. Daniel ◽  
Carolyn A.M. Burns ◽  
Renee L. Russell ◽  
Philip P. Schonewill ◽  
Sabrina D. Hoyle ◽  
...  
Keyword(s):  

1994 ◽  
Vol 43 (11) ◽  
pp. 1094-1101 ◽  
Author(s):  
Takaaki Tanaka ◽  
Ryoji Kamimura ◽  
Ryo Fujiwara ◽  
Kazuhiro Nakanishi
Keyword(s):  

2001 ◽  
Vol 34 (12) ◽  
pp. 1524-1531 ◽  
Author(s):  
TAKAAKI TANAKA ◽  
YOSHINOBU YAMAGIWA ◽  
TETSUYA NAGANO ◽  
MASAYUKI TANIGUCHI ◽  
KAZUHIRO NAKANISHI

Membranes ◽  
2020 ◽  
Vol 10 (12) ◽  
pp. 399
Author(s):  
Ignacio Hegoburu ◽  
Karina Listiarini Zedda ◽  
Svetlozar Velizarov

Industrial adoption of nanofiltration (NF) for treatment of low-pH wastewater is hindered by the limited membrane lifetime at strongly acidic conditions. In this study, the electroplating wastewater (EPWW) filtration performance of a novel pH-stable NF membrane is compared against a commercial NF membrane and a reverse osmosis (RO) membrane. The presented membrane is relatively hydrophobic and has its isoelectric point (IEP) at pH 4.1, with a high and positive zeta potential of +10 mV at pH 3. A novel method was developed to determine the molecular weight cut-off (MWCO) at a pH of 2, with a finding that the membrane maintains the same MWCO (~500 Da) as under neutral pH operating conditions, whereas the commercial membrane significantly increases it. In crossflow filtration experiments with simulated EPWW, rejections above 75% are observed for all heavy metals (compared to only 30% of the commercial membrane), while keeping the same pH in the feed and permeate. Despite the relatively lower permeance of the prepared membrane (~1 L/(m2·h·bar) versus ~4 L/(m2·h·bar) of the commercial membrane), its high heavy metals rejection coupled with a very low acid rejection makes it suitable for acid recovery applications.


1992 ◽  
pp. 578-580 ◽  
Author(s):  
Shimizu Yasutoshi ◽  
Matsushita Kohnosuke ◽  
Shimodera Ken-ichi ◽  
Watanabe Atsuo

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