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用于甲烷二氧化碳重整的氧化钇改性ZrO负载Ni催化剂:Ce助剂的作用

Yttria Modified ZrO Supported Ni Catalysts for CO Reforming of Methane: The Role of Ce Promoter.

作者信息

Fakeeha Anis H, Al Fatesh Ahmed S, Ibrahim Ahmed A, Kurdi Abdulrahman N, Abasaeed Ahmed E

机构信息

Chemical Engineering Department, College of Engineering, King Saud University, P.O. Box 800, Riyadh 11421, Saudi Arabia.

King Abdullah City for Atomic & Renewable Energy, Energy Research & Innovation Center (ERIC) in Riyadh, Riyadh 11451, Saudi Arabia.

出版信息

ACS Omega. 2021 Jan 7;6(2):1280-1288. doi: 10.1021/acsomega.0c04731. eCollection 2021 Jan 19.

Abstract

Yttria modified zirconia (YZ) supported on 5 wt % of Ni-based catalysts promoted with ceria (1-3 wt %) were prepared by the impregnation process to investigate their performance for dry reforming of methane. The reforming reactions, conducted at 700 °C and at atmospheric pressure using a CO/CH/N fixed feed ratio of 3/3/1, with a total flow rate of 70 mL/min, revealed that the ceria-promoted catalysts (Ce-Ni-YZ; = 1-3 wt %) enhanced the CH and CO conversions as compared to the reference catalyst (Ni-YZ). A CO conversion of 85% was exhibited by the 3Ce-Ni-YZ catalyst. Despite increased conversions, Ce-Ni-YZ catalysts showed more amounts of carbon deposition as evidenced by the values of TGA, and hence were found to be less stable as compared to the reference Ni-YZ catalyst. The used and fresh catalysts were characterized by BET, H-TPR, XRD, TEM, Raman, TPD, and TGA. TEM images displayed nanoparticle sizes of Ni in the fresh catalysts, while carbon filaments were formed on the spent catalysts. The CO-TPD, H-TPR, and BET results revealed the existence of only weak and moderate basic sites, the increase of total hydrogen consumption, and the surface area values with the addition of the Ce promoter, respectively. The TGA analysis showed that the Ce promoter increased the carbon deposition, while the Raman results indicated the dominance of crystallinity due to the graphitized carbon.

摘要

通过浸渍法制备了负载在5 wt%氧化钇稳定氧化锆(YZ)上、以氧化铈(1 - 3 wt%)促进的镍基催化剂,以研究其在甲烷干重整中的性能。重整反应在700℃、大气压下进行,使用固定进料比CO/CH₄/N₂为3/3/1,总流速为70 mL/min,结果表明,与参比催化剂(Ni - YZ)相比,氧化铈促进的催化剂(Ce - Ni - YZ; = 1 - 3 wt%)提高了CH₄和CO的转化率。3Ce - Ni - YZ催化剂的CO转化率达到85%。尽管转化率有所提高,但热重分析(TGA)结果表明,Ce - Ni - YZ催化剂的积碳量更多,因此与参比Ni - YZ催化剂相比,其稳定性较差。采用比表面积分析仪(BET)、程序升温还原(H - TPR)、X射线衍射(XRD)、透射电子显微镜(TEM)、拉曼光谱( Raman)、程序升温脱附(TPD)和热重分析(TGA)对使用过的和新鲜的催化剂进行了表征。TEM图像显示了新鲜催化剂中Ni的纳米颗粒尺寸,而在使用过的催化剂上形成了碳丝。CO - TPD、H - TPR和BET结果分别表明,仅存在弱碱性和中等碱性位点、总氢消耗量增加以及添加Ce促进剂后表面积值增加。TGA分析表明,Ce促进剂增加了积碳,而拉曼光谱结果表明由于石墨化碳,结晶度占主导。

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