首页> 外文期刊>Journal of Cleaner Production >Investigation of ultrasound-assisted KOH and CaO catalyzed transesterification for biodiesel production from waste cotton-seed cooking oil: Process optimization and conversion rate evaluation
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Investigation of ultrasound-assisted KOH and CaO catalyzed transesterification for biodiesel production from waste cotton-seed cooking oil: Process optimization and conversion rate evaluation

机译:对废棉籽油厂生物柴油生产超声辅助KOH和CAO催化酯交换的研究:工艺优化和转化率评价

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摘要

Development of Ultrasound (US)-assisted biodiesel production from Waste Cotton-seed Cooking Oil (WCCO) is gaining importance due to significantly lower reaction time and high energy-efficiency. In the present novel work, a comprehensive experimental study for KOH and CaO catalyzed transesterification process with detailed process optimization was performed. Kinetic modeling, scalability and energy analysis were performed to confirm the relative importance of US compared to Mechanical Stirring (MS). The optimized process parameters for KOH and CaO catalyst conditions were determined as methanol/oil molar proportion: 6.1:1 and 10.9:1, catalyst amount (w/w) %: 0.46 % and 0.96 %, reaction temperature: 53.2 degrees C and 48.3 degrees C, and the corresponding yield: 97.76 % +/- 0.03 and 96.16 % +/- 0.03 respectively. BoxBehnken model exhibits a significant correlation with experimental results in case of KOH (R-2 = 0.98) and CaO (R-2 = 0.97) catalyzed conditions. Triglyceride conversion follows pseudo-first-order reaction kinetics. The activation energy calculated for KOH and CaO catalyzed conditions was 21.36 and 33.83 kJ/mol respectively, which is 1.5 - 1.7 times lower as compared to MS process. Energy analysis showed that dissipated energy in US process is higher compared to MS. The scalability effect (with tenfold batch size), and ultrasonic duty cycle analysis showed that the continuous sonication is more effective in comparison to pulse mode. Physicochemical properties of produced biodiesel were observed in accordance with fuel specification as prescribed by ASTM D6751. Outcomes of this study are useful for development of energy-efficient US-assisted biodiesel production process on industrial scale. (C) 2020 Elsevier Ltd. All rights reserved.
机译:超声(美国)的开发 - 废棉籽烹饪油(WCCO)的生物柴油生产由于反应时间明显较低和高能量效率而导致的重要性。在本新的工作中,进行了具有详细工艺优化的KOH和CAO催化酯交换过程的综合实验研究。与机械搅拌(MS)相比,进行动力学建模,可扩展性和能量分析以确认我们的相对重要性。 KOH和CAO催化剂条件的优化工艺参数确定为甲醇/油摩尔比例:6.1:1和10.9:1,催化剂量(w / w)%:0.46%和0.96%,反应温度:53.2℃和48.3摄影度C,相应的产率:97.76%+/- 0.03和96.16%+/- 0.03。 Boxbehnken模型与KOH(R-2 = 0.98)和CaO(R-2 = 0.97)催化条件的情况表现出与实验结果的显着相关性。甘油三酯转换遵循伪一阶反应动力学。对于KOH和CAO催化条件计算的活化能量分别为21.36和33.83 kJ / mol,与MS工艺相比,其比为1.5-1.7倍。能量分析表明,与MS相比,美国工艺中的耗散能量较高。可扩展性效果(具有十倍批量尺寸)和超声占空比分析表明,与脉冲模式相比,连续超声处理更有效。根据ASTM D6751规定的燃料说明,观察产生生物柴油的物理化学性质。该研究的结果对于在工业规模上的节能美国辅助生物柴油生产过程中有助于发展。 (c)2020 elestvier有限公司保留所有权利。

著录项

  • 来源
    《Journal of Cleaner Production》 |2020年第20期|120982.1-120982.20|共20页
  • 作者单位

    Pandit Deendayal Petr Univ Dept Chem Engn Gandhinagar 382007 Gujarat India|Pandit Deendayal Petr Univ Ctr Biofuels & Bioenergy Studies Gandhinagar 382007 Gujarat India;

    Pandit Deendayal Petr Univ Dept Chem Engn Gandhinagar 382007 Gujarat India|Pandit Deendayal Petr Univ Ctr Biofuels & Bioenergy Studies Gandhinagar 382007 Gujarat India;

    Pandit Deendayal Petr Univ Dept Mech Engn Gandhinagar 382007 Gujarat India|Pandit Deendayal Petr Univ Ctr Biofuels & Bioenergy Studies Gandhinagar 382007 Gujarat India;

  • 收录信息
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Waste cotton-seed cooking oil; Biodiesel; Ultrasonic cavitation; Box-behnken design; Kinetic study;

    机译:废棉籽烹饪油;生物柴油;超声波空化;Box-Behnken设计;动力学研究;
  • 入库时间 2022-08-18 20:53:02

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