粘土掺杂BaCl和离子催化剂催化乳木果油酯交换工艺参数影响及动力学评价

Kenechi Nwosu-Obieogu , Ude Callistus Nonso , Onukwuli Dominic Okechukwu , Ezeugo Joseph
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摘要

本文建立了乳木果油(SB)与甲醇酯交换反应的动力学模型,该反应采用一种新型粘土浸渍BaCl和离子液体(CD-BaCl-IL)催化剂制备生物柴油和甘油。为了验证催化剂的适用性,采用扫描电子显微镜(SEM)、x射线衍射(XRD)、傅里叶变换红外光谱(FT-IR)、x射线荧光(XRF)和Braut Emmet Teller (BET)对合成的催化剂进行了表征。采用气相色谱-质谱联用仪(GCMS)和红外光谱(FT-IR)对生物柴油进行了表征。采用CD-BaCl-IL催化剂,在4 wt%催化剂、2 小时反应时间、300 rpm、10:1甲醇/油比、60 ℃条件下获得动力学数据。采用Eley-Rideal (ER)和Langmuir-Hinshelwood-Hougen-Watson (LHHW)两种基本反应机制对反应动力学进行了评价。动力学分析表明,LHHW模型准确反映了实验数据,参数良好,在40℃时R2值为0.999,方差为2.61E-14。速率决定步骤(RDS)是连接吸附甘油三酯和吸附醇的表面反应。速率随着温度的升高而升高,表明这是一个吸热过程。在低于醇沸点的温度下,反应的频率因子和活化能分别为6.33E6h-1和45.3 kJ/mol。LHHW模型确定了CD-BaCl-IL催化剂的RDS和SB燃料性能符合ASTM D 6751标准,从而确定了CD-BaCl-IL催化剂的可行性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Shea butter transesterification through clay-doped BaCl and ionic catalyst; process parameter impacts and kinetic evaluation
In this work, Kinetic models were developed to evaluate shea butter (SB) transesterification with methanol using a novel developed clay impregnated with BaCl and ionic liquid (CD-BaCl-IL) catalyst to produce biodiesel and glycerol. To verify their suitability for the process, the synthesized catalyst was characterized using Scanning Electron Micrograph (SEM), X-ray diffraction (XRD), Fourier Transform Infrared Spectroscopy (FT-IR), X-ray Fluorescence (XRF), and Braut Emmet Teller (BET). The biodiesel was characterized using GCMS (Gas Chromatography Mass Spectrometer) and FT-IR. Kinetic data using CD-BaCl-IL catalyst were obtained at 4 wt% catalyst, 2 hours reaction time, 300 rpm, 10:1 methanol/oil ratio, and 60 °C. Two elementary reaction mechanisms, Eley-Rideal (ER) and Langmuir-Hinshelwood-Hougen-Watson (LHHW) were employed to evaluate the kinetics. The kinetic analysis indicated that the LHHW model accurately represented the experimental data, exhibiting favorable parameters, an R2 value of 0.999, and a variance of 2.61E-14 at 40°C. The rate-determining step (RDS) was the surface reaction that connected the adsorbed triglyceride and adsorbed alcohol. The rate rose as the temperature increased, suggesting an endothermic process. At a temperature less than the boiling point of alcohol, the frequency factor and activation energy for the reaction were 6.33E6h-1 and 45.3 kJ/mol, respectively. The feasibility of the CD-BaCl-IL catalyst was ascertained as the LHHW model determined that the RDS and the SB fuel properties complied with the ASTM D 6751 standards.
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