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Modeling and fouling mechanisms for ultrafiltration of Huanggi (Radix astragalus) extracts

机译:黄芪提取物超滤的建模和结垢机理

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摘要

A semi-empirical model has been developed in ultrafiltration of huanggi (Radix astragulus) extracts. Three major fouling resistances were quantified with transmembrane pressure (TMP) ranged from 0.4 to 0.8 bar and process time lasted for 120 min. Adsorption grew fast at the initial 15 min and its contribution was more significant at 0.4 bar, nearly 50%. Pore blocking almost kept the same values of 1.28, 1.84, and 2.39 at pressures of 0.4, 0.6, and 0.8 bar, respectively. Cake layer grew linearly at 0.4 bar but it increased rapidly as the TMP arose. With the TMP increased, the contribution of cake layer became more significant, almost 75% at 0.8 bar which was triple of that at 0.4 bar. Prediction of flux decline fitted quite well with the experimental data, all within 5% errors. It demonstrates that adsorption, pore blocking, and cake layer are the main mechanisms for membrane fouling during the process.
机译:在黄gi提取物的超滤过程中,已经建立了一个半经验模型。用跨膜压力(TMP)在0.4至0.8 bar范围内量化了三个主要的耐污垢性,并且处理时间持续了120分钟。在开始的15分钟内,吸附迅速增长,在0.4 bar下的吸附作用更为显着,接近50%。在0.4、0.6和0.8 bar的压力下,毛孔阻塞几乎保持相同的值1.28、1.84和2.39。滤饼层在0.4 bar处线性增长,但随着TMP的出现迅速增加。随着TMP的增加,滤饼层的贡献变得更加显着,在0.8 bar时几乎达到75%,是0.4 bar时的三倍。通量下降的预测与实验数据非常吻合,所有误差均在5%以内。它表明吸附,孔堵塞和滤饼层是该过程中膜结垢的主要机理。

著录项

  • 来源
    《Food Science and Biotechnology》 |2013年第2期|407-412|共6页
  • 作者单位

    College of Biological and Environmental Engineering Zhejiang University of Technology">(194);

    Department of Applied Biology and Chemical Technology The Hong Kong Polytechnic University">(294);

    Department of Applied Biology and Chemical Technology The Hong Kong Polytechnic University">(294);

    Department of Applied Biology and Chemical Technology The Hong Kong Polytechnic University">(294);

  • 收录信息
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    flux decline; fouling resistance; mechanism; ultrafiltration; Radix astragalus extract;

    机译:通量下降耐污垢性机制;超滤;黄芪提取物;

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