Mudadla Umamaheswara Rao, Devthade Vidyasagar, Chandan Ghanty*, Mohd Zafar Iqbal, KVSS Bhargavi, Partha Ghosal, Giridhar Madras and Challapalli Subrahmanyam*,
{"title":"非热等离子体辅助增强 NiOx/γ-Al2O3 催化剂的二氧化碳转化能力","authors":"Mudadla Umamaheswara Rao, Devthade Vidyasagar, Chandan Ghanty*, Mohd Zafar Iqbal, KVSS Bhargavi, Partha Ghosal, Giridhar Madras and Challapalli Subrahmanyam*, ","doi":"10.1021/acs.iecr.4c00489","DOIUrl":null,"url":null,"abstract":"<p >The utilization of the dielectric barrier discharge (DBD) plasma process presents a promising avenue for transforming carbon dioxide (CO<sub>2</sub>) into valuable compounds. In this research, we explore the integration of DBD plasma with a NiO<sub><i>x</i></sub>/γ-Al<sub>2</sub>O<sub>3</sub> catalyst to amplify the efficiency and selectivity of the conversion of CO<sub>2</sub> into carbon monoxide (CO). A series of NiO<sub><i>x</i></sub>-loaded on γ-Al<sub>2</sub>O<sub>3</sub> catalysts were synthesized through wet impregnation and employed in the DBD plasma reactor. The synergy between nonthermal plasma and NiO<sub><i>x</i></sub>/γ-Al<sub>2</sub>O<sub>3</sub> resulted in a significant enhancement in CO<sub>2</sub> conversion, particularly demonstrating a notable increase in the energy content of produced carbon monoxide (CO). Enhanced conversion rates and selectivities were observed. Notably, the NiO<sub><i>x</i></sub>/γ-Al<sub>2</sub>O<sub>3</sub> catalyst with a 15 wt % loading exhibited the highest CO<sub>2</sub> conversion of approximately ∼9% at an applied voltage of 22 kV, accompanied by an energy efficiency of 1.13 mmol kJ<sup>–1</sup>. This study provides a comprehensive analysis of the impact of plasma catalyst coupling on CO<sub>2</sub> conversion into CO, showcasing the potential of hybrid DBD reactor systems for large-scale CO<sub>2</sub> conversion and contributing to sustainable and value-added fuel production. The superior performance of the hybridized system is attributed to enhanced charge deposition and modified gas-phase chemistry resulting from the integration of the catalyst. Furthermore, we employed BOLSIG+ software to calculate the mean electron energy and electron energy distribution function for different packing conditions, enhancing our understanding of the system’s behavior and contributing valuable insights to the overall study.</p>","PeriodicalId":39,"journal":{"name":"Industrial & Engineering Chemistry Research","volume":"63 21","pages":"9336–9346"},"PeriodicalIF":3.9000,"publicationDate":"2024-05-16","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Nonthermal Plasma-Assisted Enhanced CO2 Conversion over NiOx/γ-Al2O3 Catalyst\",\"authors\":\"Mudadla Umamaheswara Rao, Devthade Vidyasagar, Chandan Ghanty*, Mohd Zafar Iqbal, KVSS Bhargavi, Partha Ghosal, Giridhar Madras and Challapalli Subrahmanyam*, \",\"doi\":\"10.1021/acs.iecr.4c00489\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p >The utilization of the dielectric barrier discharge (DBD) plasma process presents a promising avenue for transforming carbon dioxide (CO<sub>2</sub>) into valuable compounds. In this research, we explore the integration of DBD plasma with a NiO<sub><i>x</i></sub>/γ-Al<sub>2</sub>O<sub>3</sub> catalyst to amplify the efficiency and selectivity of the conversion of CO<sub>2</sub> into carbon monoxide (CO). A series of NiO<sub><i>x</i></sub>-loaded on γ-Al<sub>2</sub>O<sub>3</sub> catalysts were synthesized through wet impregnation and employed in the DBD plasma reactor. The synergy between nonthermal plasma and NiO<sub><i>x</i></sub>/γ-Al<sub>2</sub>O<sub>3</sub> resulted in a significant enhancement in CO<sub>2</sub> conversion, particularly demonstrating a notable increase in the energy content of produced carbon monoxide (CO). Enhanced conversion rates and selectivities were observed. Notably, the NiO<sub><i>x</i></sub>/γ-Al<sub>2</sub>O<sub>3</sub> catalyst with a 15 wt % loading exhibited the highest CO<sub>2</sub> conversion of approximately ∼9% at an applied voltage of 22 kV, accompanied by an energy efficiency of 1.13 mmol kJ<sup>–1</sup>. This study provides a comprehensive analysis of the impact of plasma catalyst coupling on CO<sub>2</sub> conversion into CO, showcasing the potential of hybrid DBD reactor systems for large-scale CO<sub>2</sub> conversion and contributing to sustainable and value-added fuel production. The superior performance of the hybridized system is attributed to enhanced charge deposition and modified gas-phase chemistry resulting from the integration of the catalyst. Furthermore, we employed BOLSIG+ software to calculate the mean electron energy and electron energy distribution function for different packing conditions, enhancing our understanding of the system’s behavior and contributing valuable insights to the overall study.</p>\",\"PeriodicalId\":39,\"journal\":{\"name\":\"Industrial & Engineering Chemistry Research\",\"volume\":\"63 21\",\"pages\":\"9336–9346\"},\"PeriodicalIF\":3.9000,\"publicationDate\":\"2024-05-16\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Industrial & Engineering Chemistry Research\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://pubs.acs.org/doi/10.1021/acs.iecr.4c00489\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Industrial & Engineering Chemistry Research","FirstCategoryId":"5","ListUrlMain":"https://pubs.acs.org/doi/10.1021/acs.iecr.4c00489","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
Nonthermal Plasma-Assisted Enhanced CO2 Conversion over NiOx/γ-Al2O3 Catalyst
The utilization of the dielectric barrier discharge (DBD) plasma process presents a promising avenue for transforming carbon dioxide (CO2) into valuable compounds. In this research, we explore the integration of DBD plasma with a NiOx/γ-Al2O3 catalyst to amplify the efficiency and selectivity of the conversion of CO2 into carbon monoxide (CO). A series of NiOx-loaded on γ-Al2O3 catalysts were synthesized through wet impregnation and employed in the DBD plasma reactor. The synergy between nonthermal plasma and NiOx/γ-Al2O3 resulted in a significant enhancement in CO2 conversion, particularly demonstrating a notable increase in the energy content of produced carbon monoxide (CO). Enhanced conversion rates and selectivities were observed. Notably, the NiOx/γ-Al2O3 catalyst with a 15 wt % loading exhibited the highest CO2 conversion of approximately ∼9% at an applied voltage of 22 kV, accompanied by an energy efficiency of 1.13 mmol kJ–1. This study provides a comprehensive analysis of the impact of plasma catalyst coupling on CO2 conversion into CO, showcasing the potential of hybrid DBD reactor systems for large-scale CO2 conversion and contributing to sustainable and value-added fuel production. The superior performance of the hybridized system is attributed to enhanced charge deposition and modified gas-phase chemistry resulting from the integration of the catalyst. Furthermore, we employed BOLSIG+ software to calculate the mean electron energy and electron energy distribution function for different packing conditions, enhancing our understanding of the system’s behavior and contributing valuable insights to the overall study.
期刊介绍:
ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.