TY - JOUR
T1 - Oil-in-water emulsion separation
T2 - Fouling of alumina membranes with and without a silicon carbide deposition in constant flux filtration mode
AU - Chen, Mingliang
AU - Heijman, Sebastiaan G.J.
AU - Luiten-Olieman, Mieke W.J.
AU - Rietveld, Luuk C.
N1 - Funding Information:
Mingliang Chen acknowledges the China Scholarship Council for his PhD scholarship under the State Scholarship Fund (No. 201704910894). We thank WaterLab at TU Delft for providing the help on the measurement of samples. We would like to thank Nadia van Pelt (TU Delft, The Netherlands) for her help on language and grammar issues of the manuscript. Bob Siemerink, and Iske Achterhuis from Twente University are acknowledged for the support concerning the zeta potential measurements. Guangze Qin is acknowledged for measuring the membrane water permeance.
Funding Information:
Mingliang Chen acknowledges the China Scholarship Council for his PhD scholarship under the State Scholarship Fund (No. 201704910894 ). We thank WaterLab at TU Delft for providing the help on the measurement of samples. We would like to thank Nadia van Pelt (TU Delft, The Netherlands) for her help on language and grammar issues of the manuscript. Bob Siemerink, and Iske Achterhuis from Twente University are acknowledged for the support concerning the zeta potential measurements. Guangze Qin is acknowledged for measuring the membrane water permeance.
Publisher Copyright:
© 2022
PY - 2022/6/1
Y1 - 2022/6/1
N2 - Ceramic membranes have drawn increasing attention in oily wastewater treatment as an alternative to their traditional polymeric counterparts, yet persistent membrane fouling is still one of the largest challenges. Particularly, little is known about ceramic membrane fouling by oil-in-water (O/W) emulsions in constant flux filtration modes. In this study, the effects of emulsion chemistry (surfactant concentration, pH, salinity and Ca2+) and operation parameters (permeate flux and filtration time) were comparatively evaluated for alumina and silicon carbide (SiC) deposited ceramic membranes, with different physicochemical surface properties. The original membranes were made of 100% alumina, while the same membranes were also deposited with a SiC layer to change the surface charge and hydrophilicity. The SiC-deposited membrane showed a lower reversible and irreversible fouling when permeate flux was below 110 L m−2 h−1. In addition, it exhibited a higher permeance recovery after physical and chemical cleaning, as compared to the alumina membranes. Increasing sodium dodecyl sulfate (SDS) concentration in the feed decreased the fouling of both membranes, but to a higher extent in the alumina membranes. The fouling of both membranes could be reduced with increasing the pH of the emulsion due to the enhanced electrostatic repulsion between oil droplets and membrane surface. Because of the screening of surface charge in a high salinity solution (100 mM NaCl), only a small difference in irreversible fouling was observed for alumina and SiC-deposited membranes under these conditions. The presence of Ca2+ in the emulsion led to high irreversible fouling of both membranes, because of the compression of diffusion double layer and the interactions between Ca2+ and SDS. The low fouling tendency and/or high cleaning efficiency of the SiC-deposited membranes indicated their potential for oily wastewater treatment.
AB - Ceramic membranes have drawn increasing attention in oily wastewater treatment as an alternative to their traditional polymeric counterparts, yet persistent membrane fouling is still one of the largest challenges. Particularly, little is known about ceramic membrane fouling by oil-in-water (O/W) emulsions in constant flux filtration modes. In this study, the effects of emulsion chemistry (surfactant concentration, pH, salinity and Ca2+) and operation parameters (permeate flux and filtration time) were comparatively evaluated for alumina and silicon carbide (SiC) deposited ceramic membranes, with different physicochemical surface properties. The original membranes were made of 100% alumina, while the same membranes were also deposited with a SiC layer to change the surface charge and hydrophilicity. The SiC-deposited membrane showed a lower reversible and irreversible fouling when permeate flux was below 110 L m−2 h−1. In addition, it exhibited a higher permeance recovery after physical and chemical cleaning, as compared to the alumina membranes. Increasing sodium dodecyl sulfate (SDS) concentration in the feed decreased the fouling of both membranes, but to a higher extent in the alumina membranes. The fouling of both membranes could be reduced with increasing the pH of the emulsion due to the enhanced electrostatic repulsion between oil droplets and membrane surface. Because of the screening of surface charge in a high salinity solution (100 mM NaCl), only a small difference in irreversible fouling was observed for alumina and SiC-deposited membranes under these conditions. The presence of Ca2+ in the emulsion led to high irreversible fouling of both membranes, because of the compression of diffusion double layer and the interactions between Ca2+ and SDS. The low fouling tendency and/or high cleaning efficiency of the SiC-deposited membranes indicated their potential for oily wastewater treatment.
KW - Alumina membrane
KW - Ceramic membranes
KW - Membrane fouling
KW - Oil-in-water emulsion
KW - Silicon carbide membrane
UR - http://www.scopus.com/inward/record.url?scp=85126541827&partnerID=8YFLogxK
U2 - 10.1016/j.watres.2022.118267
DO - 10.1016/j.watres.2022.118267
M3 - Article
C2 - 35306459
AN - SCOPUS:85126541827
SN - 0043-1354
VL - 216
JO - Water research
JF - Water research
M1 - 118267
ER -
