用于节能乙醇-水分离的降膜式蒸馏工艺配置的性能比较

IF 5.9 3区 工程技术 Q1 CHEMISTRY, MULTIDISCIPLINARY
Eduardo Valdemar Silva , José Luiz Francisco Alves , Guilherme Davi Mumbach , Gabriel Francisco Reus , Ricardo Antonio Francisco Machado , Ariovaldo Bolzan , Cintia Marangoni
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引用次数: 0

摘要

节能蒸馏塔是目前乙醇-水分离领域的重要研究方向。将降膜式蒸馏塔与双相热流器耦合用于乙醇-水分离,可显著节约能源和空间。为了使用于乙醇-水分离的热效率降膜式蒸馏塔技术更加成熟,现有的两种降膜式蒸馏配置(单管型和多管型)之间的比较分析仍然存在知识空白。在本研究中,对两种不同的中试规模降膜式蒸馏配置(即单管型和多管型,均与双相热虹吸管进行热集成)的稳态性能进行了比较研究,以实现从水流中富集乙醇。进行了中试试验,以研究操作条件(进料温度、进料质量流量和蒸汽室温度)对乙醇富集、蒸馏物流量和能耗的影响。同时,研究了从蒸汽室到蒸馏管的两种潜在热能传递方式(等温和非等温)。结果发现,单管型配置在提高乙醇富集方面更为有效,而多管型配置则表现出更高的乙醇回收率和更低的能耗要求。在工业相关的操作条件下,与传统的托盘蒸馏技术相比,可节省高达 78.5% 的能耗,这表明热效率降膜式蒸馏技术在乙醇-水分离中的实际应用潜力巨大。这项研究成功证实了热效降膜蒸馏技术在乙醇-水分离中的巨大潜力,并为支持大规模工业应用提供了新的实用知识。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Performance comparison of falling film distillation process configurations for energy-saving ethanol-water separation

Performance comparison of falling film distillation process configurations for energy-saving ethanol-water separation

Performance comparison of falling film distillation process configurations for energy-saving ethanol-water separation

Energy-saving distillation columns are currently of significant research interest for ethanol-water separation. The coupling of a falling film distillation column with a biphasic thermosyphon apparatus for ethanol-water separation can yield remarkable energy and space savings. In the pursuit of maturing the thermally efficient falling film distillation column technology for ethanol-water separation, knowledge gaps persist regarding the comparative analysis between two available falling-film distillation configurations: a single-tube and a multi-tube type. In this study, a comparative investigation of the steady-state performance of two distinct pilot-scale falling-film distillation configurations, namely a single-tube and a multi-tube type, both thermally integrated with a biphasic thermosiphon, was conducted to achieve ethanol enrichment from an aqueous stream. Pilot-scale tests were conducted to investigate the impact of operating conditions (feed temperature, feed mass flow rate, and temperature of the steam chamber) on ethanol enrichment, distillate flow rate, and energy consumption. Simultaneously, two potential thermal energy transfer arrangements were examined from the steam chamber to the distillation tubes (isothermal and non-isothermal). The single-tube type configuration was found to be more effective in enhancing ethanol enrichment, while the multi-tube type configuration exhibited higher ethanol recovery and lower energy requirements. An energy consumption savings of up to 78.5 % compared to traditional tray distillation technology was achieved using industrially relevant operating conditions, showing the potential for real-world application of thermally efficient falling-film distillation technology in ethanol-water separation. This study successfully confirmed the promising potential of thermally efficient falling-film distillation technology for ethanol-water separation and generated new practical knowledge to support large-scale industrial applications.

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来源期刊
CiteScore
10.40
自引率
6.60%
发文量
639
审稿时长
29 days
期刊介绍: Journal of Industrial and Engineering Chemistry is published monthly in English by the Korean Society of Industrial and Engineering Chemistry. JIEC brings together multidisciplinary interests in one journal and is to disseminate information on all aspects of research and development in industrial and engineering chemistry. Contributions in the form of research articles, short communications, notes and reviews are considered for publication. The editors welcome original contributions that have not been and are not to be published elsewhere. Instruction to authors and a manuscript submissions form are printed at the end of each issue. Bulk reprints of individual articles can be ordered. This publication is partially supported by Korea Research Foundation and the Korean Federation of Science and Technology Societies.
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