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Techno-economic and energetic assessment of an innovative pilot-scale thermosyphon-assisted falling film distillation unit for sanitizer-grade ethanol recovery

机译:技术经济和精力充沛评估创新的试验级热旋流助液辅助薄膜蒸馏装置,用于消毒剂级乙醇回收

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The increasing demand for ethanol-based disinfectants due to the COVID-19 pandemic has driven the emergence of innovative strategies to avoid the risk of shortage and reduce production costs. Distillation is well-known as the major energy consumer and cost driver for ethanol recovery in conventional distilleries. Our research team has been developing a novel heat-intensified falling film distillation apparatus assisted by a two-phase closed thermosyphon, patented as Destubcal. Therefore, this study aims to provide a techno-economic and energetic assessment of the pilot-scale thermosyphon-assisted falling film distillation unit applied to recover sanitizergrade ethanol with 70 vol% in alcohol. Performance analysis showed that under a feed flow rate of 14 L/h, a feed temperature of 80 degrees C, and an evaporator temperature of 93 degrees C, the pilot-scale unit reaches the minimum specific thermal energy consumption with the maximum distillate ethanol recovery and energy efficiency (88.5%). The impact of the elements in the capital cost-share showed instrumentation and control (27.8%), and piping and auxiliary equipment (27.6%) as the predominant capital costs, while the cost for major process equipment represents only 6.2% which reveals a low-cost and easy-to-implement technology. The major operating cost-driver is the labor (51.3%) since the pilot-scale unit has a lower capacity than industrial plants. However, the Destubcal unit spends on utility costs about 31.6 $/m(feed)(3), which represents a total saving of 43.8% compared to conventional distilleries. Furthermore, the Destubcal unit saves about 1.78 MJ/kg (46.4%), with 59.2% less column height than a conventional column, being considered techno-economically feasible for sanitizer-grade ethanol recovery.
机译:由于Covid-19大流行导致乙醇基消毒剂的需求日益增加推动了创新策略的出现,以避免短缺的风险,降低生产成本。蒸馏是常规酿酒厂中乙醇回收的主要能量消耗和成本驱动器。我们的研究团队一直在开发一种新颖的热强化下落薄膜蒸馏装置,由两相封闭的热循环,专利为Destubal辅助。因此,本研究旨在为试验级热烃辅助落叶薄膜蒸馏装置提供技术经济和精力充沛的评估,以恢复70体积%的醇溶液。性能分析表明,在14L / h的进料流速下,进料温度为80℃,蒸发器温度为93摄氏度,导级单元达到最小的馏分乙醇回收率的最小特定热能消耗和能源效率(88.5%)。资本成本份额中的要素的影响显示仪器和控制(27.8%),以及管道和辅助设备(27.6%),作为主要的资本成本,而主要过程设备的成本仅占6.2%,显示出低位-cost且易于实现的技术。主要经营成本司机是劳动力(51.3%),因为飞行员规模单位的容量低于工业厂房。然而,目标机构花费约31.6 $ / m(饲料)(3),其与常规蒸馏液相比,该额率为43.8%。此外,目标单位可节省约1.78mJ / kg(46.4%),柱高于常规柱59.2%,被认为是用于消毒剂级乙醇回收的技术经济上可行的。

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