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Process Optimization for Biodiesel Production from Moringa oleifera Oil Using Conch Shells as Heterogeneous Catalyst

机译:使用海螺壳作为异质催化剂的生物柴油生产的过程优化

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The potential of conch shells (CSs) as a suitable heterogeneous basic catalyst for transesterification of high FFA content non-edible Moringa oleifera oil (MOO) was investigated. Biodiesel was produced by a two-step transesterification process. In the first step, high FFA content of the oil was reduced from 40.25 to 1.4% using reaction conditions of 1:2 v/v methanol to oil ratio, 1.5 vol% H2SO4 concentration, 2 h reaction time and 60 degrees C reaction temperature. In the second step, the esterified oil was converted into biodiesel by reacting with methanol using calcined conch shells (CCSs) as a heterogeneous basic catalyst. The physiochemical characteristics of the CCS catalyst were studied by X-ray diffraction (XRD), scanning electron microscopy, and energy dispersive X-ray (SEM-EDAX), Fourier transform infrared spectroscopy (FTIR), and Brunauer-Emmett-Teller (BET) analysis. The characterization results revealed that calcium oxide (CaO) was the major phase of CCS. The effect of process variables on biodiesel conversion was investigated by response surface methodology using Box-Behnken design and the independent variables taken for study are catalyst concentration, methanol to oil ratio and reaction time. The optimum process conditions were found to be 8.02 wt % catalyst concentration, 8.66:1 methanol to oil molar ratio and 130 min reaction time. Under these experimental conditions, methyl ester conversion of 97.06% was obtained which was in reasonable agreement with the predicted value. The structure of Moringa oleifera methyl ester (MOME) was characterized by FTIR and methyl ester conversion was determined by proton nuclear magnetic resonance (H-1-NMR) spectroscopy. (c) 2018 American Institute of Chemical Engineers Environ Prog, 38:e13015, 2019
机译:研究了作为合适的非均相碱性催化剂的高FFA含量不可食用的辣木(MOO)的合适的非均相碱性催化剂的电壳(CSS)。生物柴油是通过两步酯交换过程生产的。在第一步中,使用1:2V / V甲醇与油比的反应条件,从40.25降至1.4%,将1.5体积%H 2 SO 4浓度,2小时反应时间和60℃反应温度,从40.25〜1.4%降低。在第二步中,通过使用煅烧的己烷壳(CCSS)反应作为非均相碱性催化剂,将酯化的油转化为生物柴油。通过X射线衍射(XRD),扫描电子显微镜和能量分散X射线(SEM-EDAX),傅里叶变换红外光谱(FTIR)和Brunauer-emmett-externer(Bets ) 分析。表征结果表明,氧化钙(CaO)是CCS的主要阶段。使用Box-Behnken设计研究了工艺变量对生物柴油转换的影响,并使用Box-Behnken设计研究了研究的独立变量是催化剂浓度,甲醇与油比和反应时间。发现最佳过程条件为8.02wt%的催化剂浓度,8.66:1甲醇与油摩尔比和130分钟的反应时间。在这些实验条件下,获得了97.06%的甲酯转化率与预测值合理一致。通过FTIR和甲酯转化通过质子核磁共振(H-1-NMR)光谱法测定了Moringa Oleifera甲酯(Mome)的结构。 (c)2018美国化学工程师研究所环境PROG,38:E13015,2019

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