{"title":"在平行板介电阻挡放电反应器中使用 Ni/Mg-Al2O3 催化剂提高非热等离子体催化 CO2 重整 CH4 的能力","authors":"Thitiporn Suttikul , Chantaraporn Phalakornkule , Patcharin Naemchanthara , Annop Klamchuen , Tuksadon Wutikhun , Kulwadee Theanngern , Sanchai Kuboon , Sasikarn Nuchdang","doi":"10.1016/j.joei.2024.101781","DOIUrl":null,"url":null,"abstract":"<div><p>CO<sub>2</sub> and CH<sub>4</sub> are converted to syngas by dry reforming of methane (DRM) reaction. This research investigated the effects of the Mg promoter on Al<sub>2</sub>O<sub>3</sub>-supported Ni catalysts and Mg calcination temperature on the DRM performance in a parallel plate dielectric barrier discharge reactor. The Mg promoter played a crucial role in the DRM performance, as increasing the Mg calcination temperature from 700 °C to 800 °C significantly improved the DRM performance and catalyst properties, including increased specific surface area, decreased total acidity, reduced crystallite and particle sizes, and more uniform dispersion of the Ni nanoparticles. Under these conditions, the H<sub>2</sub> and CO selectivity were 77.0 % and 70.7 %, the CH<sub>4</sub> and CO<sub>2</sub> conversion were 25.1 % and 20.6 %, and the energy efficiency was 8.4 %. In addition, the catalyst was associated with a lower coking rate (0.5 mg C/g<sub>cat</sub> h), a relatively low carbon deposit of 1.5 %, and a carbon loss of 2.8 %, possibly because the weak acidity hindered the Boudouard reaction and CH<sub>4</sub> decomposition. However, increasing the Mg calcination temperature to 900 °C increased the total acidity and Ni particle size, decreasing H<sub>2</sub> and CO selectivities and increasing carbon deposits on the catalyst surface.</p></div>","PeriodicalId":17287,"journal":{"name":"Journal of The Energy Institute","volume":"117 ","pages":"Article 101781"},"PeriodicalIF":5.6000,"publicationDate":"2024-08-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Enhancement of non-thermal plasma-catalytic CO2 reforming of CH4 using Ni/Mg–Al2O3 catalysts in a parallel plate dielectric barrier discharge reactor\",\"authors\":\"Thitiporn Suttikul , Chantaraporn Phalakornkule , Patcharin Naemchanthara , Annop Klamchuen , Tuksadon Wutikhun , Kulwadee Theanngern , Sanchai Kuboon , Sasikarn Nuchdang\",\"doi\":\"10.1016/j.joei.2024.101781\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>CO<sub>2</sub> and CH<sub>4</sub> are converted to syngas by dry reforming of methane (DRM) reaction. This research investigated the effects of the Mg promoter on Al<sub>2</sub>O<sub>3</sub>-supported Ni catalysts and Mg calcination temperature on the DRM performance in a parallel plate dielectric barrier discharge reactor. The Mg promoter played a crucial role in the DRM performance, as increasing the Mg calcination temperature from 700 °C to 800 °C significantly improved the DRM performance and catalyst properties, including increased specific surface area, decreased total acidity, reduced crystallite and particle sizes, and more uniform dispersion of the Ni nanoparticles. Under these conditions, the H<sub>2</sub> and CO selectivity were 77.0 % and 70.7 %, the CH<sub>4</sub> and CO<sub>2</sub> conversion were 25.1 % and 20.6 %, and the energy efficiency was 8.4 %. In addition, the catalyst was associated with a lower coking rate (0.5 mg C/g<sub>cat</sub> h), a relatively low carbon deposit of 1.5 %, and a carbon loss of 2.8 %, possibly because the weak acidity hindered the Boudouard reaction and CH<sub>4</sub> decomposition. However, increasing the Mg calcination temperature to 900 °C increased the total acidity and Ni particle size, decreasing H<sub>2</sub> and CO selectivities and increasing carbon deposits on the catalyst surface.</p></div>\",\"PeriodicalId\":17287,\"journal\":{\"name\":\"Journal of The Energy Institute\",\"volume\":\"117 \",\"pages\":\"Article 101781\"},\"PeriodicalIF\":5.6000,\"publicationDate\":\"2024-08-10\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Journal of The Energy Institute\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S1743967124002599\",\"RegionNum\":2,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"ENERGY & FUELS\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of The Energy Institute","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S1743967124002599","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0
摘要
CO2 和 CH4 可通过甲烷干转化(DRM)反应转化为合成气。本研究探讨了 Al2O3 支承镍催化剂上的镁促进剂和镁煅烧温度对平行板介电阻挡放电反应器中 DRM 性能的影响。镁促进剂对 DRM 性能起着至关重要的作用,因为将镁煅烧温度从 700 °C 提高到 800 °C,可显著改善 DRM 性能和催化剂特性,包括比表面积增加、总酸度降低、结晶和颗粒尺寸减小以及镍纳米颗粒的分散更均匀。在这些条件下,H2 和 CO 的选择性分别为 77.0 % 和 70.7 %,CH4 和 CO2 的转化率分别为 25.1 % 和 20.6 %,能效为 8.4 %。此外,该催化剂的结焦率较低(0.5 mg C/gcat h),碳沉积相对较低,为 1.5 %,碳损失为 2.8 %,这可能是因为弱酸性阻碍了布杜尔反应和 CH4 分解。然而,将镁的煅烧温度提高到 900 °C,会增加总酸度和镍的粒径,从而降低 H2 和 CO 的选择性,增加催化剂表面的碳沉积。
Enhancement of non-thermal plasma-catalytic CO2 reforming of CH4 using Ni/Mg–Al2O3 catalysts in a parallel plate dielectric barrier discharge reactor
CO2 and CH4 are converted to syngas by dry reforming of methane (DRM) reaction. This research investigated the effects of the Mg promoter on Al2O3-supported Ni catalysts and Mg calcination temperature on the DRM performance in a parallel plate dielectric barrier discharge reactor. The Mg promoter played a crucial role in the DRM performance, as increasing the Mg calcination temperature from 700 °C to 800 °C significantly improved the DRM performance and catalyst properties, including increased specific surface area, decreased total acidity, reduced crystallite and particle sizes, and more uniform dispersion of the Ni nanoparticles. Under these conditions, the H2 and CO selectivity were 77.0 % and 70.7 %, the CH4 and CO2 conversion were 25.1 % and 20.6 %, and the energy efficiency was 8.4 %. In addition, the catalyst was associated with a lower coking rate (0.5 mg C/gcat h), a relatively low carbon deposit of 1.5 %, and a carbon loss of 2.8 %, possibly because the weak acidity hindered the Boudouard reaction and CH4 decomposition. However, increasing the Mg calcination temperature to 900 °C increased the total acidity and Ni particle size, decreasing H2 and CO selectivities and increasing carbon deposits on the catalyst surface.
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