Eduardo Valdemar Silva , José Luiz Francisco Alves , Guilherme Davi Mumbach , Gabriel Francisco Reus , Ricardo Antonio Francisco Machado , Ariovaldo Bolzan , Cintia Marangoni
{"title":"用于节能乙醇-水分离的降膜式蒸馏工艺配置的性能比较","authors":"Eduardo Valdemar Silva , José Luiz Francisco Alves , Guilherme Davi Mumbach , Gabriel Francisco Reus , Ricardo Antonio Francisco Machado , Ariovaldo Bolzan , Cintia Marangoni","doi":"10.1016/j.jiec.2024.01.059","DOIUrl":null,"url":null,"abstract":"<div><p>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.</p></div>","PeriodicalId":363,"journal":{"name":"Journal of Industrial and Engineering Chemistry","volume":"135 ","pages":"Pages 480-492"},"PeriodicalIF":5.9000,"publicationDate":"2024-02-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Performance comparison of falling film distillation process configurations for energy-saving ethanol-water separation\",\"authors\":\"Eduardo Valdemar Silva , José Luiz Francisco Alves , Guilherme Davi Mumbach , Gabriel Francisco Reus , Ricardo Antonio Francisco Machado , Ariovaldo Bolzan , Cintia Marangoni\",\"doi\":\"10.1016/j.jiec.2024.01.059\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>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.</p></div>\",\"PeriodicalId\":363,\"journal\":{\"name\":\"Journal of Industrial and Engineering Chemistry\",\"volume\":\"135 \",\"pages\":\"Pages 480-492\"},\"PeriodicalIF\":5.9000,\"publicationDate\":\"2024-02-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Journal of Industrial and Engineering Chemistry\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S1226086X24000595\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"CHEMISTRY, MULTIDISCIPLINARY\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of Industrial and Engineering Chemistry","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S1226086X24000595","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"CHEMISTRY, MULTIDISCIPLINARY","Score":null,"Total":0}
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.
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.