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Preparation, Characterization and Optimization of Silica-PDMS Superhydrophobic Composite Membrane for Pervaporation Concentration of an Aqueous Ethanol Solution.

机译:用于乙醇水溶液渗透蒸发的二氧化硅-PDMS超疏水复合膜的制备,表征和优化。

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摘要

Sweet sorghum bagasse pretreated with 5% (by weight) acetic acid was used in a 96 h fed-batch simultaneous saccharification and fermentation (SSF) at an accumulated solid biomass concentration of 20% (w/v). A composite membrane fabricated by depositing a hierarchy of hexamethyldisilazane modified 8 mum and 100 nm silica and thin layer of PDMS on a stainless steel support of 2 mum pores was used for the pervaporation concentration of ethanol-water solutions. The experimental data from the response surface methodology and central composite rotatable design have been modeled by a multiple regression (MR) quadratic model. The MR models were combined with the desirability function to optimize the pervaporation process via the Design-Expert 8.0.7.1 software. An ASPEN Plus user-defined pervaporation model coupled with a Microsoft Excel spreadsheet was then developed to predict the total permeate flux (Jt) and ethanol selectivity (alpha) from experimental conditions. The effects of the main by-products in a fermentation broth on the pervaporation process were studied.;The fed-batch SSF produced a maximum ethanol concentration of 53.1 g/L and an 88.7% ethanol yield. The SEM surface and cross-sectional morphologies showed a dense PDMS top layer and good interlayer adhesion. The water contact angle of the composite membrane was 151.8° as compared to 100° for the pure PDMS membrane. The optimal Jt and alpha were 589.8 g/m 2·h and 10.3, respectively, increasing the ethanol concentration from 8.5 to 48.9% wt. at 52.3°C (feed temperature) and 30 Pa (permeate pressure). The combined ASPEN Plus and Microsoft Excel model predicted accurately Jt and alpha within the range of experimental conditions and extrapolated with reasonable accuracy. The fermentation by-products increased alpha with the exception of glycerol that decreased alpha and a synergetic effect was observed when the entire components were combined. As expected, the components had reverse effect on Jt.
机译:在96 h补料分批同时糖化和发酵(SSF)中使用以5%(按重量计)乙酸预处理的甜高粱甘蔗渣,其累积的固体生物质浓度为20%(w / v)。通过将六甲基二硅氮烷改性的8微米和100纳米二氧化硅和PDMS薄层沉积在2微米孔的不锈钢支撑体上制成的复合膜用于乙醇水溶液的全蒸发浓度。来自响应面方法和中心复合材料可旋转设计的实验数据已通过多元回归(MR)二次模型进行建模。通过Design-Expert 8.0.7.1软件,将MR模型与所需功能相结合,以优化渗透蒸发过程。然后开发了ASPEN Plus用户定义的渗透蒸发模型以及Microsoft Excel电子表格,以根据实验条件预测总渗透通量(Jt)和乙醇选择性(alpha)。研究了发酵液中主要副产物对全蒸发过程的影响。补料分批SSF产生的最大乙醇浓度为53.1 g / L,乙醇产率为88.7%。 SEM表面和横截面形态显示出致密的PDMS顶层和良好的层间粘附性。与纯PDMS膜的100°相比,复合膜的水接触角为151.8°。最佳Jt和α分别为589.8 g / m 2·h和10.3,将乙醇浓度从8.5 wt%增加到48.9%wt。温度为52.3°C(进料温度)和30 Pa(渗透压)。结合ASPEN Plus和Microsoft Excel模型可以在实验条件范围内准确预测Jt和alpha并以合理的精度进行推断。发酵副产物增加了α,除了甘油降低了α,并且当将所有组分组合在一起时观察到了协同作用。不出所料,这些成分对Jt有相反的影响。

著录项

  • 作者

    Darkwah, Kwabena.;

  • 作者单位

    North Carolina Agricultural and Technical State University.;

  • 授予单位 North Carolina Agricultural and Technical State University.;
  • 学科 Engineering Chemical.
  • 学位 M.S.
  • 年度 2013
  • 页码 161 p.
  • 总页数 161
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

  • 入库时间 2022-08-17 11:41:58

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