{"title":"Hydrocracking of Crude Palm Oil over Bimetallic Oxide NiO-CdO/biochar Catalyst","authors":"A. Allwar, Rina Maulina, T. Julianto, Annisa Ayu Widyaningtyas","doi":"10.9767/bcrec.17.2.14074.476-485","DOIUrl":null,"url":null,"abstract":"The bimetallic oxide NiO-CdO/biochar catalyst was prepared by coprecipitation and calcination methods. Characterizations of catalyst were carried out using Fourier Transform Infra Red (FTIR), Surface Area Analyzer (SAA), X-ray Diffraction (XRD), and Scanning Electron Microscope-Energy Dispersive X-ray (SEM-EDX) mapping methods. The catalyst showed a good average crystalized size of 12.30 nm related to the nanoparticles and high dispersion of Ni and Cd metals on the biochar surface. Analysis of liquid fuel products was observed using Gas Chromatography - Mass Spectrometry (GC-MS) which was separated to the main product of gasoline fraction (C6–C10), and the second product of kerosene fraction (C11–C16), and diesel fraction (C17–C23). The presence of the catalyst in the hydrocracking resulted in more liquid product of 56.55 wt% than the thermal cracking with a liquid product of 20.55 wt%. The best performance activity of catalyst was found at a temperature of 150 °C with high selectivity to hydrocarbon fuel with 12 types of gasoline fractions (39.24 wt%) compared to gasoline fractions obtained at higher hydrocracking temperatures of 250 °C and 350 °C. The results of this study showed that the bimetallic oxide catalyst supported with biochar from palm kernel shell plays an important role in the hydrocracking process to increase the selectivity of the gasoline fraction. Copyright © 2022 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0). ","PeriodicalId":9366,"journal":{"name":"Bulletin of Chemical Reaction Engineering & Catalysis","volume":"16 1","pages":""},"PeriodicalIF":0.0000,"publicationDate":"2022-06-17","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"3","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Bulletin of Chemical Reaction Engineering & Catalysis","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.9767/bcrec.17.2.14074.476-485","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 3
双金属氧化物NiO-CdO/生物炭催化下粗棕榈油加氢裂化研究
采用共沉淀法和煅烧法制备了双金属氧化物NiO-CdO/生物炭催化剂。采用傅里叶变换红外(FTIR)、表面积分析仪(SAA)、x射线衍射(XRD)和扫描电子显微镜-能量色散x射线(SEM-EDX)作图方法对催化剂进行了表征。催化剂的平均结晶尺寸为12.30 nm,这与纳米颗粒和Ni和Cd金属在生物炭表面的高度分散有关。采用气相色谱-质谱法(GC-MS)对液体燃料产品进行分析,分离出主要产品为汽油馏分(C6-C10)、煤油馏分(C11-C16)和柴油馏分(C17-C23)。在加氢裂化过程中,催化剂的存在使加氢裂化反应的液体产物达到56.55 wt%,而热裂化反应的液体产物为20.55 wt%。与在250℃和350℃加氢裂化温度下得到的汽油馏分相比,在150℃温度下催化剂的性能活性最好,对12种汽油馏分的烃类燃料具有高选择性(39.24 wt%)。研究结果表明,棕榈仁壳生物炭负载的双金属氧化物催化剂在加氢裂化过程中对提高汽油馏分的选择性起着重要作用。版权所有©2022作者所有,BCREC集团出版。这是一篇基于CC BY-SA许可(https://creativecommons.org/licenses/by-sa/4.0)的开放获取文章。
本文章由计算机程序翻译,如有差异,请以英文原文为准。