Effect of ZnO/γ-Al<sub>2</sub>O<sub>3</sub> Catalyst Packing on the Degradation of SF<sub>6</sub> in a Dual-Stage DBD Plasma Reactor

Sulfur hexafluoride (SF<sub>6</sub>) gas is widely used in the electric power industry as an excellent insulating gas. However, SF<sub>6</sub> is a potent greenhouse gas, and its degradation is an ideal method for emission reduction. In the field of SF<sub>6</sub> degradation, due to the harsh decomposition conditions, it is often difficult to achieve both a high degradation rate and favorable product distribution. To address this issue, a double-stage dielectric barrier discharge (DBD) series degradation experimental platform for SF<sub>6</sub> gas was designed in this study. A ZnO catalyst was packed in the first-stage reactor to improve the SF<sub>6</sub> degradation rate, while a γ-Al<sub>2</sub>O<sub>3</sub> catalyst was packed in the second-stage reactor to optimize the product distribution. Additionally, the selectivity of SF<sub>6</sub> degradation products was regulated by externally adding H<sub>2</sub>O. Experimental results showed that under an input power of 100 W, the SF<sub>6</sub> degradation rate reached 100% in the ZnO/γ-Al<sub>2</sub>O<sub>3</sub> double-stage packed system, achieving complete degradation of SF<sub>6</sub>. As the input power increased, the energy yield showed a gradually decreasing trend. The addition of an appropriate concentration of H<sub>2</sub>O effectively improved both the degradation rate and energy yield of SF<sub>6</sub>, with the maximum energy yields of the two-stage reactors reaching 23.9 and 17.9 g/kWh, respectively. With regard to decomposition products, the types of SF<sub>6</sub> decomposition products in both reactors remained unchanged, including SO<sub>2</sub>, SO<sub>2</sub>F<sub>2</sub>, SOF<sub>2</sub>, and SOF<sub>4</sub>. The main product in the first-stage reactor was SO<sub>2</sub>F<sub>2</sub>, whereas in the second-stage reactor, SO<sub>2</sub> was predominant. The addition of H<sub>2</sub>O also effectively increased the yield of SO<sub>2</sub> while suppressing the formation of SO<sub>2</sub>F<sub>2</sub>, which is more difficult to treat. This study provides experimental support for SF<sub>6</sub> exhaust gas degradation and offers a research direction for industrial applications.

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Journal
ACS Omega
Published
2025-09-10
DOI
https://doi.org/10.1021/acsomega.5c06029
Citations
1
Primary Topic
Plasma Applications and Diagnostics
Type
article
Field-Weighted Citation Impact
1.36
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Effect of ZnO/γ-Al2O3 Catalyst Packing on the Degradation of SF6 in a Dual-Stage DBD Plasma Reactor

Chi Zhang, Jianbo Shi, Ying Zhang, Yalong Li et al.
1 citations
ACS Omega
Plasma Applications and Diagnostics
1.36
article

Effect of ZnO/γ-Al2O3 Catalyst Packing on the Degradation of SF6 in a Dual-Stage DBD Plasma Reactor

Chi Zhang, Jianbo Shi, Ying Zhang, Yalong Li, Lei Yu, Huiyu Tan
article en
1 citations

Abstract

Sulfur hexafluoride (SF<sub>6</sub>) gas is widely used in the electric power industry as an excellent insulating gas. However, SF<sub>6</sub> is a potent greenhouse gas, and its degradation is an ideal method for emission reduction. In the field of SF<sub>6</sub> degradation, due to the harsh decomposition conditions, it is often difficult to achieve both a high degradation rate and favorable product distribution. To address this issue, a double-stage dielectric barrier discharge (DBD) series degradation experimental platform for SF<sub>6</sub> gas was designed in this study. A ZnO catalyst was packed in the first-stage reactor to improve the SF<sub>6</sub> degradation rate, while a γ-Al<sub>2</sub>O<sub>3</sub> catalyst was packed in the second-stage reactor to optimize the product distribution. Additionally, the selectivity of SF<sub>6</sub> degradation products was regulated by externally adding H<sub>2</sub>O. Experimental results showed that under an input power of 100 W, the SF<sub>6</sub> degradation rate reached 100% in the ZnO/γ-Al<sub>2</sub>O<sub>3</sub> double-stage packed system, achieving complete degradation of SF<sub>6</sub>. As the input power increased, the energy yield showed a gradually decreasing trend. The addition of an appropriate concentration of H<sub>2</sub>O effectively improved both the degradation rate and energy yield of SF<sub>6</sub>, with the maximum energy yields of the two-stage reactors reaching 23.9 and 17.9 g/kWh, respectively. With regard to decomposition products, the types of SF<sub>6</sub> decomposition products in both reactors remained unchanged, including SO<sub>2</sub>, SO<sub>2</sub>F<sub>2</sub>, SOF<sub>2</sub>, and SOF<sub>4</sub>. The main product in the first-stage reactor was SO<sub>2</sub>F<sub>2</sub>, whereas in the second-stage reactor, SO<sub>2</sub> was predominant. The addition of H<sub>2</sub>O also effectively increased the yield of SO<sub>2</sub> while suppressing the formation of SO<sub>2</sub>F<sub>2</sub>, which is more difficult to treat. This study provides experimental support for SF<sub>6</sub> exhaust gas degradation and offers a research direction for industrial applications.

ACS OmegaVol. 10(37)
Electric Power Research Institute (US), North China Electric Power University (CN), State Grid Corporation of China (China) (CN), Hubei University of Technology (CN)
Openalex Percentile: Top 16%
Plasma Applications and Diagnostics
1.36
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