Porous SiC Ceramic Membranes Prepared by Low-Temperature Sintering: Filtration Performance in Mine Water Treatment and Alkaline Cleaning Stability

Low-temperature fabrication of porous silicon carbide (SiC) ceramic membranes using secondary bonding phases offers an alternative to conventional high-temperature sintering. This study compared aluminium-sol- and silica-sol-derived SiC membranes fabricated in air at 1300 °C with sol additions of 10–40 wt.%, focusing on pore structure, mechanical strength, mine-water filtration, fouling behaviour, and alkaline oxidative cleaning. X-ray diffraction revealed weak features potentially associated with mullite formation in the aluminium-sol membranes, while SiO2-related phases were observed in the silica-sol membranes. Increasing sol content reduced porosity, pore diameter, and permeate flux while improving flexural strength. SiC-30%Al-sol provided a favourable performance balance, achieving a flexural strength of 25.2 MPa, a permeate flux of approximately 230 L m−2 h−1 after 40 min of mine-water filtration, and a final permeate turbidity of approximately 0.3 NTU. For SiC-30%Al-sol, the cake-filtration model provided the best fit over the 5–20 min interval, without establishing the dominant fouling mechanism. Following a single NaOH/NaClO cleaning cycle, SiC-30%Al-sol exhibited 90.4% flux recovery and 15.1% flexural-strength loss. Aluminium-sol membranes generally showed smaller strength losses and surface-roughness changes than silica-sol membranes under the tested conditions. These findings highlight the influence of bonding-phase chemistry on membrane performance, although repeated cleaning and post-cleaning pore-structure measurements are needed to establish long-term durability.

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Publication Details

Journal
Membranes
Published
2026-10-29
DOI
https://doi.org/10.3390/membranes16110367
Primary Topic
Membrane Separation Technologies
Type
article
Field-Weighted Citation Impact
0.00

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article

Porous SiC Ceramic Membranes Prepared by Low-Temperature Sintering: Filtration Performance in Mine Water Treatment and Alkaline Cleaning Stability

杜海波, Xufeng Xu, Sai Ma, Yameng Li et al.
Membranes
Membrane Separation Technologies
article

Porous SiC Ceramic Membranes Prepared by Low-Temperature Sintering: Filtration Performance in Mine Water Treatment and Alkaline Cleaning Stability

杜海波, Xufeng Xu, Sai Ma, Yameng Li, Yuhang Jin, Binbin Du
article en

Abstract

Low-temperature fabrication of porous silicon carbide (SiC) ceramic membranes using secondary bonding phases offers an alternative to conventional high-temperature sintering. This study compared aluminium-sol- and silica-sol-derived SiC membranes fabricated in air at 1300 °C with sol additions of 10–40 wt.%, focusing on pore structure, mechanical strength, mine-water filtration, fouling behaviour, and alkaline oxidative cleaning. X-ray diffraction revealed weak features potentially associated with mullite formation in the aluminium-sol membranes, while SiO2-related phases were observed in the silica-sol membranes. Increasing sol content reduced porosity, pore diameter, and permeate flux while improving flexural strength. SiC-30%Al-sol provided a favourable performance balance, achieving a flexural strength of 25.2 MPa, a permeate flux of approximately 230 L m−2 h−1 after 40 min of mine-water filtration, and a final permeate turbidity of approximately 0.3 NTU. For SiC-30%Al-sol, the cake-filtration model provided the best fit over the 5–20 min interval, without establishing the dominant fouling mechanism. Following a single NaOH/NaClO cleaning cycle, SiC-30%Al-sol exhibited 90.4% flux recovery and 15.1% flexural-strength loss. Aluminium-sol membranes generally showed smaller strength losses and surface-roughness changes than silica-sol membranes under the tested conditions. These findings highlight the influence of bonding-phase chemistry on membrane performance, although repeated cleaning and post-cleaning pore-structure measurements are needed to establish long-term durability.

MembranesVol. 16(11)
China Coal Technology Engineering Group
Openalex Percentile: Top 25%
Membrane Separation Technologies
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