Mohammad Saleh-Abadi, Mohsen Rostami, Amir Hamzeh Farajollahi, Rasool Amirkhani, Mahdi Ebrahimi Farshchi, Mahdi Simiari
{"title":"Employing Granulated Bimetallic Nanocomposite of Ni/Cu@CuMOF Nanocomposite in Steam Reforming of Methanol Process for Hydrogen Production","authors":"Mohammad Saleh-Abadi, Mohsen Rostami, Amir Hamzeh Farajollahi, Rasool Amirkhani, Mahdi Ebrahimi Farshchi, Mahdi Simiari","doi":"10.1615/interjenercleanenv.2023047102","DOIUrl":null,"url":null,"abstract":"Conventional fossil-based energy sources have numerous environmental demerits; sustainable and renewable sources are attracting the undivided attention of researchers owing to their astounding physical and chemical features. Hydrogen as a green energy source is the most preferential source that has been employed in numerous industrial-scale technologies. Not only is hydrogen a potent energy carrier, but also it is not detrimental to the environment. Among many other hydrogen production processes, steam reforming of methanol (SRM) is deemed a practical method due to its low energy consumption. In this study, a metal-organic framework (copper benzenedicarboxylate (CuBDC)) has been utilized as a support of two various active metals, Cu and Ni in an SRM process (Ni/Cu@CuBDC). The catalyst is granulated with a self-created granulating machine in order to take a positive step toward utilizing the novel catalysts in a pilot scale process. Many characterization analyses (SEM, EDX, FTIR, XRD, BET, XPS, H2-TPR, CO2-TPD, and NH3-TPD) had been conducted in order to evaluate the accuracy of the synthetic catalysts and their performance. At the optimum temperature (300 ᵒC), which comparably is a low temperature for the SRM process, 99% methanol conversion with 98% H2 yield was achieved. Moreover, due to the employment of CuBDC as the support, the amount of acidic and basic active sites had been adjusted in a way that the CO selectivity of the process reached 3.59%.","PeriodicalId":38729,"journal":{"name":"International Journal of Energy for a Clean Environment","volume":"5 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2023-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"International Journal of Energy for a Clean Environment","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1615/interjenercleanenv.2023047102","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"Engineering","Score":null,"Total":0}
引用次数: 0
Abstract
Conventional fossil-based energy sources have numerous environmental demerits; sustainable and renewable sources are attracting the undivided attention of researchers owing to their astounding physical and chemical features. Hydrogen as a green energy source is the most preferential source that has been employed in numerous industrial-scale technologies. Not only is hydrogen a potent energy carrier, but also it is not detrimental to the environment. Among many other hydrogen production processes, steam reforming of methanol (SRM) is deemed a practical method due to its low energy consumption. In this study, a metal-organic framework (copper benzenedicarboxylate (CuBDC)) has been utilized as a support of two various active metals, Cu and Ni in an SRM process (Ni/Cu@CuBDC). The catalyst is granulated with a self-created granulating machine in order to take a positive step toward utilizing the novel catalysts in a pilot scale process. Many characterization analyses (SEM, EDX, FTIR, XRD, BET, XPS, H2-TPR, CO2-TPD, and NH3-TPD) had been conducted in order to evaluate the accuracy of the synthetic catalysts and their performance. At the optimum temperature (300 ᵒC), which comparably is a low temperature for the SRM process, 99% methanol conversion with 98% H2 yield was achieved. Moreover, due to the employment of CuBDC as the support, the amount of acidic and basic active sites had been adjusted in a way that the CO selectivity of the process reached 3.59%.