Efficient construction of SiC membranes to filtrate high-temperature dust-laden gas for environmental sustainability

During the production processes of energy, metallurgy, chemical engineering, and other process industries, substantial high-temperature dust-laden flue gas is generated. Asymmetric silicon carbide (SiC) membranes exhibit significant potential in flue gas filtration since they enable direct filtration of high-temperature gas and facilitate thermal energy recovery. However, membrane particle penetration is a prevalent issue when constructing membrane layer directly on macroporous support, which contributes to a considerable mass transfer resistance. Herein, a novel hydrophobic modification strategy was developed to avoid the slurry penetration, thereby fabricating the asymmetric SiC membrane without the necessity of any intermediate or sacrificial layer. Firstly, the modifier concentration was adjusted to guarantee that the support was hydrophobic enough to prevent the slurry from penetrating. Subsequently, the slurry surface tension was fine-tuned by introducing ethanol to enhance the integrity of the SiC membrane. Furthermore, the effect of solid content was systematically investigated. It was demonstrated that the optimized SiC membranes obtained excellent gas permeance from 100.8 to 199.8 m 3 ·m −2 ·h −1 ·kPa −1 with the pore size ranging from 1.93 to 3.89 μm. Also, the SiC membrane exhibited excellent stability for 24 h and achieved an excellent dust removal efficiency (99.99%) when filtering ultrafine dust particles (∼300 nm) under high temperatures. This method effectively bridges the membrane particle penetration issue caused by the particle size disparity among different layers of the asymmetric membrane, establishing an efficient strategy to fabricate high-permeance SiC membranes applied in high-temperature dust-laden gas filtration. An innovative support hydrophobization method was proposed to effectively solve particle penetration, enabling fabrication of defect-free asymmetric SiC membranes. The membranes achieve high gas permeance and 99.99% rejection towards PM 0.3 nanoparticles for high-temperature dust-laden gas filtration. • SiC membrane without intermediate layer was fabricated via support hydrophobization method. • The support hydrophobicity and slurry properties were systematically balanced. • The membranes exhibited great gas permeance compared with the literature. • The membranes showed above 99.99 % rejection towards PM 0.3 nanoparticles at 300 °C.

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Publication Details

Journal
Green Energy & Environment
Published
2025-09-01
DOI
https://doi.org/10.1016/j.gee.2025.08.003
Citations
3
Primary Topic
Aerosol Filtration and Electrostatic Precipitation
Type
article
Field-Weighted Citation Impact
2.19
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article

Efficient construction of SiC membranes to filtrate high-temperature dust-laden gas for environmental sustainability

Weihong Xing, Zhaoxiang Zhong, Yuqi Song, Dong Zou et al.
3 citations
Green Energy & Environment
Aerosol Filtration and Electrostatic Precipitation
2.19
article

Efficient construction of SiC membranes to filtrate high-temperature dust-laden gas for environmental sustainability

Weihong Xing, Zhaoxiang Zhong, Yuqi Song, Dong Zou, Shiying Ni
article en
3 citations

Abstract

During the production processes of energy, metallurgy, chemical engineering, and other process industries, substantial high-temperature dust-laden flue gas is generated. Asymmetric silicon carbide (SiC) membranes exhibit significant potential in flue gas filtration since they enable direct filtration of high-temperature gas and facilitate thermal energy recovery. However, membrane particle penetration is a prevalent issue when constructing membrane layer directly on macroporous support, which contributes to a considerable mass transfer resistance. Herein, a novel hydrophobic modification strategy was developed to avoid the slurry penetration, thereby fabricating the asymmetric SiC membrane without the necessity of any intermediate or sacrificial layer. Firstly, the modifier concentration was adjusted to guarantee that the support was hydrophobic enough to prevent the slurry from penetrating. Subsequently, the slurry surface tension was fine-tuned by introducing ethanol to enhance the integrity of the SiC membrane. Furthermore, the effect of solid content was systematically investigated. It was demonstrated that the optimized SiC membranes obtained excellent gas permeance from 100.8 to 199.8 m 3 ·m −2 ·h −1 ·kPa −1 with the pore size ranging from 1.93 to 3.89 μm. Also, the SiC membrane exhibited excellent stability for 24 h and achieved an excellent dust removal efficiency (99.99%) when filtering ultrafine dust particles (∼300 nm) under high temperatures. This method effectively bridges the membrane particle penetration issue caused by the particle size disparity among different layers of the asymmetric membrane, establishing an efficient strategy to fabricate high-permeance SiC membranes applied in high-temperature dust-laden gas filtration. An innovative support hydrophobization method was proposed to effectively solve particle penetration, enabling fabrication of defect-free asymmetric SiC membranes. The membranes achieve high gas permeance and 99.99% rejection towards PM 0.3 nanoparticles for high-temperature dust-laden gas filtration. • SiC membrane without intermediate layer was fabricated via support hydrophobization method. • The support hydrophobicity and slurry properties were systematically balanced. • The membranes exhibited great gas permeance compared with the literature. • The membranes showed above 99.99 % rejection towards PM 0.3 nanoparticles at 300 °C.

Green Energy & EnvironmentVol. 10(12)
Nanjing Tech University (CN), Suzhou University of Science and Technology (CN)
Openalex Percentile: Top 11%
Aerosol Filtration and Electrostatic Precipitation
2.19
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