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Membrane Type Wastewater Decolorization Using Culture Supernatant of Trametes versicolor and Squeezing of Physiologically Active Substance from Fungus Body

机译:黑斑病菌培养上清液对膜型废水的脱色及菌体中生理活性物质的压榨

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摘要

An enzymatic membrane bioreactor using the culture supernatant of white-rot fungus Trametes versicolor was developed to perform the decolorization of dye wastewater. The culture supernatant exhibiting high laccase activity and the model dye wastewater containing anthraquinone type dye were mixed in a continuous stirred tank membrane reactor with an ultrafiltration membrane which permitted the recycling of the enzyme in the reactor. The results obtained from the enzymatic membrane bioreactor showed that 80% of decolorization and approximately-constant permeation resistance were maintained for continuous treatment periods. The decolorization behaviors were well described using the combined equation on the basis of mass balance and enzyme kinetics. In addition, dehydration of excess fungus that grown in the process of the decolorization treatment was carried out by mechanical expression. It should be noted that the moisture content in the compressed cake of fungus was finally reduced to 20wt% under pressure of 7 MPa. The kinetics of expression such as the time variation of the moisture content in the compressed cake were accurately described on the basis of the multi-stage creep model. Furthermore, we confirmed that the squeezed liquid from the fungus body contains physiologically active substances such as (3-glucan showing antitumor activity.
机译:开发了一种使用白腐真菌Trametes versicolor的培养上清液的酶膜生物反应器,以进行染料废水的脱色。具有高漆酶活性的培养上清液和含有蒽醌型染料的模型染料废水在带有超滤膜的连续搅拌釜膜反应器中混合,使酶在反应器中循环。从酶促膜生物反应器获得的结果表明,连续处理期间可保持80%的脱色和大致恒定的抗渗透性。基于质量平衡和酶动力学,使用组合方程很好地描述了脱色行为。另外,通过机械表达进行在脱色处理过程中生长的过量真菌的脱水。应当注意的是,在7MPa的压力下,真菌的压滤饼中的水分含量最终降低至20wt%。在多阶段蠕变模型的基础上,准确地描述了压缩动力学,如压缩饼中水分含量的时间变化。此外,我们确认从真菌体中挤出的液体含有生理活性物质,例如(3-葡聚糖显示出抗肿瘤活性)。

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  • 会议地点 Sapporom(JP)
  • 作者单位

    Department of Chemical Engineering, Nagoya University, Furo-cho, Chikusa-ku, Nagoya 464-8603, Japan;

    Department of Chemical Engineering, Nagoya University, Furo-cho, Chikusa-ku, Nagoya 464-8603, Japan;

    Department of Chemical Engineering, Nagoya University, Furo-cho, Chikusa-ku, Nagoya 464-8603, Japan;

    Department of Chemical Engineering, Nagoya University, Furo-cho, Chikusa-ku, Nagoya 464-8603, Japan;

    Department of Chemical Engineering, Nagoya University, Furo-cho, Chikusa-ku, Nagoya 464-8603, Japan;

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