Study of Anionic Dye Removal from Aqueous Solutions by a Novel Ultrafiltration Ceramic Membrane with Carbon Coating

In this work, we propose a novel ultrafiltration ceramic membrane based on support from fly ash microspheres and selective layer from alumina nanofibers with carbon coating. The membrane is characterized by the average pore size of 19 nm and water permeability of 46 L/m2 h bar. The filtration experiments with aqueous solutions of anionic dyes are performed in cross-flow mode. The membrane demonstrates high rejection of 96–97 and 99.8% for Reactive blue 4 (681 Da) and Direct red 80 (1373 Da), respectively. A lower rejection of 55–60 and 79–81% is found for Orange II (350 Da) and Indigo carmine (466 Da), respectively. The permeate flux is in the range 147–171 L/m2 h at the transmembrane pressure of 5 bars. The solutions with lower dye concentration (20 vs. 100 mg/L) demonstrate higher degree of removal. The adsorption isotherms for considered dyes on the membrane support and selective layer as well as zeta potential of selective layer surface are measured. It allows us to reveal that the dye rejection occurs mainly due to electrostatic repulsion between anionic dyes and negatively charged membranes surface, while the contribution of adsorption to the rejection is minor. The present study provides new insights into the mechanisms of dye removal by ultrafiltration membranes and contributes to the development of solutions for wastewater treatment in dying and textile industries.

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Publication Details

Journal
Membranes and Membrane Technologies
Published
2025-12-01
DOI
https://doi.org/10.1134/s2517751625600943
Primary Topic
Membrane Separation Technologies
Type
article
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article

Study of Anionic Dye Removal from Aqueous Solutions by a Novel Ultrafiltration Ceramic Membrane with Carbon Coating

I. A. Kharchenko, G. V. Akimochkina, E. V. Fomenko, A. S. Goltaev et al.
Membranes and Membrane Technologies
Membrane Separation Technologies
article

Study of Anionic Dye Removal from Aqueous Solutions by a Novel Ultrafiltration Ceramic Membrane with Carbon Coating

I. A. Kharchenko, G. V. Akimochkina, E. V. Fomenko, A. S. Goltaev, E. V. Elsuf’ev, S. A. Vorobyev, I. R. Volkova, I. I. Ryzhkov
article en

Abstract

In this work, we propose a novel ultrafiltration ceramic membrane based on support from fly ash microspheres and selective layer from alumina nanofibers with carbon coating. The membrane is characterized by the average pore size of 19 nm and water permeability of 46 L/m2 h bar. The filtration experiments with aqueous solutions of anionic dyes are performed in cross-flow mode. The membrane demonstrates high rejection of 96–97 and 99.8% for Reactive blue 4 (681 Da) and Direct red 80 (1373 Da), respectively. A lower rejection of 55–60 and 79–81% is found for Orange II (350 Da) and Indigo carmine (466 Da), respectively. The permeate flux is in the range 147–171 L/m2 h at the transmembrane pressure of 5 bars. The solutions with lower dye concentration (20 vs. 100 mg/L) demonstrate higher degree of removal. The adsorption isotherms for considered dyes on the membrane support and selective layer as well as zeta potential of selective layer surface are measured. It allows us to reveal that the dye rejection occurs mainly due to electrostatic repulsion between anionic dyes and negatively charged membranes surface, while the contribution of adsorption to the rejection is minor. The present study provides new insights into the mechanisms of dye removal by ultrafiltration membranes and contributes to the development of solutions for wastewater treatment in dying and textile industries.

Membranes and Membrane TechnologiesVol. 7(6)
Saint Petersburg Academic University (RU), Krasnoyarsk Scientific Center (RU), Institute of Chemistry and Chemical Technology (RU), Siberian Branch of the Russian Academy of Sciences (RU), Institute of Computational Modeling (RU), Siberian Federal University (RU)
Clean water and sanitation
Openalex Percentile: Top 30%
Membrane Separation Technologies
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