Graduate Program in Process Engineering, University of the Region of Joinville, Joinville, Santa Catarina, Brazil.
Graduate Program in Chemical Engineering, Federal University of Santa Catarina, Campus Universitário Reitor João David Ferreira Lima, Florianópolis, Santa Catarina, Brazil.
Biotechnol Prog. 2019 Jul;35(4):e2830. doi: 10.1002/btpr.2830. Epub 2019 May 14.
In this work, we performed recovery of ethanol from a fermentation broth of banana pseudostem by pervaporation (PV) as a lower-energy-cost alternative to traditional separation processes such as distillation. As real fermentation systems generally contain by-products, it was investigated the effects of different components from the fermentation broth of banana pseudostem on PV performance for ethanol recovery through commercial flat sheet polydimethylsiloxane (PDMS) membrane. The experiments were compared to a binary solution (ethanol/water) to determine differences in the results due to the presence of fermentation by-products. A real fermented broth of banana pseudostem was also used as feed for the PV experiments. Seven by-products from fermented broth were identified: propanol, isobutanol, methanol, isoamyl alcohol, 1-pentanol, acetic acid, and succinic acid. Moreover, the residual sugar content of 3.02 g/L was obtained. The presence of methanol showed the best results for total permeate flux (0.1626 kg·m ·h ) and ethanol permeate flux (0.0391 kg·m ·h ) during PV at 25°C and 3 wt% ethanol, also demonstrated by the selectivity and enrichment factor. The lowest total fluxes of permeate were observed in the experiments containing the acids. Better permeance of 0.1171 from 0.0796 kg·m ·h and membrane selectivity of 9.77 from 9.30 were obtained with real fermentation broth than with synthetic solutions, possibly due to the presence of by-products in the multicomponent mixtures, which contributed to ethanol permeation. The results of this work indicate that by-products influence pervaporation of ethanol with hydrophobic flat sheet membrane produced from the fermented broth of banana pseudostem.
在这项工作中,我们通过渗透蒸发(PV)从香蕉假茎发酵液中回收乙醇,作为替代传统分离工艺(如蒸馏)的低能耗方法。由于实际发酵系统通常含有副产物,因此研究了香蕉假茎发酵液中的不同成分对乙醇回收用商业平板聚二甲基硅氧烷(PDMS)膜渗透蒸发性能的影响。通过与二元溶液(乙醇/水)进行比较,确定了由于发酵副产物的存在而导致结果差异。还使用真正的发酵香蕉假茎发酵液作为 PV 实验的进料。从发酵液中鉴定出 7 种副产物:正丙醇、异丁醇、甲醇、异戊醇、1-戊醇、乙酸和琥珀酸。此外,还获得了 3.02 g/L 的残留糖含量。在 25°C 和 3 wt%乙醇下进行 PV 时,甲醇的存在表现出最佳的总渗透通量(0.1626 kg·m·h)和乙醇渗透通量(0.0391 kg·m·h),这也通过选择性和浓缩因子得到了证明。在含有酸的实验中观察到最低的总渗透通量。在含有实际发酵液的实验中,获得了更好的渗透通量 0.1171 (比 0.0796 kg·m·h)和膜选择性 9.77 (比 9.30),这可能是由于多组分混合物中副产物的存在有助于乙醇渗透。这项工作的结果表明,副产品影响了由香蕉假茎发酵液制成的疏水平板膜对乙醇的渗透蒸发。