Zhenhan Sun , Guoke Zhao , Gongqing Tang , Zhihu Zhao , Pei Li
{"title":"采用逐层自组装方法制备乙醇脱水用高性能渗透蒸发膜","authors":"Zhenhan Sun , Guoke Zhao , Gongqing Tang , Zhihu Zhao , Pei Li","doi":"10.1016/j.advmem.2025.100132","DOIUrl":null,"url":null,"abstract":"<div><div>To achieve fuel-grade purity (≥99.5 wt%), raw bioethanol needs to be purified. Adopting pervaporation membrane for bioethanol enrichment can greatly reduce the energy consumption compared with distillation. However, this requires the membrane having a high flux and high water to ethanol selectivity as well as good stability. In this study, a layer-by-layer self-assembled composite pervaporation membrane was prepared by alternately dip-coating polyallylamine hydrochloride (PAH) and sodium alginate (SA) solutions on the surface of a polyacrylonitrile (PAN) microfiltration membrane. The membrane flux and separation performance under different feed conditions are measured independently, and the results are mutually independent. These tests are conducted as short-term experiments to evaluate the membrane's separation performance under specific feed conditions. By optimizing the concentrations of PAH and SA, best separation performance of the composite membranes was obtained with a flux of 2.02 kg m<sup>−2</sup> h<sup>−1</sup> and a water to ethanol separation factor of 10993 using a 90 % ethanol water solution as feed at 70 °C. The composite membrane showed good stability in water. When keeping all other conditions unchanged, the feed ethanol concentration is adjusted to 50 wt%, the membrane flux increase to 12.61 kg m⁻<sup>2</sup> h⁻<sup>1</sup>, and the water concentration in the permeate reach 99.7743 wt%.</div></div>","PeriodicalId":100033,"journal":{"name":"Advanced Membranes","volume":"5 ","pages":"Article 100132"},"PeriodicalIF":0.0000,"publicationDate":"2025-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Preparation of high-performance pervaporation membranes for ethanol dehydration using a layer-by-layer self-assembly method\",\"authors\":\"Zhenhan Sun , Guoke Zhao , Gongqing Tang , Zhihu Zhao , Pei Li\",\"doi\":\"10.1016/j.advmem.2025.100132\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>To achieve fuel-grade purity (≥99.5 wt%), raw bioethanol needs to be purified. Adopting pervaporation membrane for bioethanol enrichment can greatly reduce the energy consumption compared with distillation. However, this requires the membrane having a high flux and high water to ethanol selectivity as well as good stability. In this study, a layer-by-layer self-assembled composite pervaporation membrane was prepared by alternately dip-coating polyallylamine hydrochloride (PAH) and sodium alginate (SA) solutions on the surface of a polyacrylonitrile (PAN) microfiltration membrane. The membrane flux and separation performance under different feed conditions are measured independently, and the results are mutually independent. These tests are conducted as short-term experiments to evaluate the membrane's separation performance under specific feed conditions. By optimizing the concentrations of PAH and SA, best separation performance of the composite membranes was obtained with a flux of 2.02 kg m<sup>−2</sup> h<sup>−1</sup> and a water to ethanol separation factor of 10993 using a 90 % ethanol water solution as feed at 70 °C. The composite membrane showed good stability in water. When keeping all other conditions unchanged, the feed ethanol concentration is adjusted to 50 wt%, the membrane flux increase to 12.61 kg m⁻<sup>2</sup> h⁻<sup>1</sup>, and the water concentration in the permeate reach 99.7743 wt%.</div></div>\",\"PeriodicalId\":100033,\"journal\":{\"name\":\"Advanced Membranes\",\"volume\":\"5 \",\"pages\":\"Article 100132\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2025-01-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Advanced Membranes\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S2772823425000065\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Advanced Membranes","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2772823425000065","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
摘要
为了达到燃料级纯度(≥99.5 wt%),原料生物乙醇需要纯化。采用渗透蒸发膜富集生物乙醇与精馏相比,可大大降低能耗。然而,这要求膜具有高通量和高水对乙醇的选择性以及良好的稳定性。在本研究中,通过在聚丙烯腈(PAN)微滤膜表面交替浸渍涂覆聚丙烯胺盐酸盐(PAH)和海藻酸钠(SA)溶液,制备了一层一层自组装的复合渗透蒸发膜。对不同进料条件下的膜通量和分离性能进行了独立的测定,结果是相互独立的。这些试验是作为短期实验进行的,以评估膜在特定进料条件下的分离性能。通过对PAH和SA的浓度进行优化,在70℃条件下,以90%乙醇水溶液为原料,在通量为2.02 kg m−2 h−1,水乙醇分离系数为10993的条件下,复合膜的分离性能最佳。复合膜在水中表现出良好的稳定性。在其他条件不变的情况下,将原料乙醇浓度调整到50 wt%,膜通量增加到12.61 kg m - 2 h - 1,渗透膜中的水浓度达到99.7743 wt%。
Preparation of high-performance pervaporation membranes for ethanol dehydration using a layer-by-layer self-assembly method
To achieve fuel-grade purity (≥99.5 wt%), raw bioethanol needs to be purified. Adopting pervaporation membrane for bioethanol enrichment can greatly reduce the energy consumption compared with distillation. However, this requires the membrane having a high flux and high water to ethanol selectivity as well as good stability. In this study, a layer-by-layer self-assembled composite pervaporation membrane was prepared by alternately dip-coating polyallylamine hydrochloride (PAH) and sodium alginate (SA) solutions on the surface of a polyacrylonitrile (PAN) microfiltration membrane. The membrane flux and separation performance under different feed conditions are measured independently, and the results are mutually independent. These tests are conducted as short-term experiments to evaluate the membrane's separation performance under specific feed conditions. By optimizing the concentrations of PAH and SA, best separation performance of the composite membranes was obtained with a flux of 2.02 kg m−2 h−1 and a water to ethanol separation factor of 10993 using a 90 % ethanol water solution as feed at 70 °C. The composite membrane showed good stability in water. When keeping all other conditions unchanged, the feed ethanol concentration is adjusted to 50 wt%, the membrane flux increase to 12.61 kg m⁻2 h⁻1, and the water concentration in the permeate reach 99.7743 wt%.