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Fungal based nitrogen and phosphorus concentration reduction in wastewater.

机译:以真菌为基础的废水中氮和磷的浓度降低。

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摘要

This research project investigated the development of a fungal nitrogen a phosphorus wastewater treatment system. Fungi were isolated from a unit process at the Gold Bar Wastewater Treatment Plant. A subset of the isolates were tested using batch reactors to determine the initial kinetic description of nitrogen and phosphorus decrease from wastewater. Test conditions evaluated included: aerobic, microaerophilic and anoxic atmospheres; pH; dilute wastewater; mixed culture; and successive inoculations. Additional testing was performed using batch and fed-batch attached growth systems with surface to volume ratios of 25 and 50 m2 m-3. It was found that the fungi isolated were capable of a single-step direct ammonium (NH4 +) concentration decrease pathway. This nitrogen decrease system was most active using a microaerophilic environment. A zero-order kinetic model best fit the NH4+ decrease data. Calculated NH 4+ substrate utilisation rates ranged between 0.033 to 0.08 mg-N L-1 hr-1 for the five fungal species tests. However, with suspended growth conditions NH4+ decrease suffered from variable performance. The attached growth NH4 + decrease tests saw a 50% decrease in the variation of the NH4+ utilisation rates. NH4 + utilisation rates observed for the attached growth decrease were also in the range of 0.031 to 0.076 mg-N L-1 hr-1. Fungi were shown to be capable of phosphate (o-PO43-) concentration decrease from wastewater. It was also found that the oxygen tension has a clear role in fungal o-PO43- decrease. Fungi will reduce the concentration of o-PO43- under all three oxygen tensions tested. However, the mechanism of uptake and final biochemical destination of o-PO43- cannot be stated with the data collected. However the data support different mechanisms for the concentration decrease, especially for anoxic uptake and that energy requirements were substantially less than conventional bacterial o-PO 43- systems. The COD to o-PO43- decrease ratio was estimated to be 6.5 g COD:1 g of o-PO4 3-. The major issue for further development of fungal nitrogen and phosphorus treatment technology, the slow substrate utilisation rates, may be addressed by increasing the microbial mass.
机译:该研究项目研究了真菌氮磷废水处理系统的开发。从金条废水处理厂的单元过程中分离出真菌。使用间歇反应器测试了一部分分离株,以确定废水中氮和磷减少的初始动力学描述。评估的测试条件包括:有氧,微需氧和缺氧气氛; pH值稀释废水;混养;和连续接种。使用分批补料和分批补料的生长系统进行了额外的测试,表面积与体积之比为25和50 m2 m-3。发现分离的真菌能够进行单步直接铵(NH4 +)浓度降低途径。在微需氧环境下,该氮减少系统最为活跃。零级动力学模型最适合NH4 +减少量数据。对于五个真菌物种测试,计算得出的NH 4+底物利用率为0.033至0.08 mg-N L-1 hr-1。但是,在生长条件暂停的情况下,NH4 +的下降会产生可变的性能。附带的生长NH4 +减少测试显示,NH4 +利用率变化减少了50%。伴随着生长下降而观察到的NH4 +利用率也在0.031至0.076 mg-N L-1 hr-1的范围内。研究表明,真菌能够使废水中的磷酸盐(o-PO43-)浓度降低。还发现氧张力在真菌o-PO43-降低中具有明显作用。在所有测试的三个氧气压力下,真菌都会降低o-PO43-的浓度。但是,o-PO43-的摄取机理和最终生化终点无法用收集到的数据说明。然而,数据支持浓度降低的不同机制,尤其是对于缺氧吸收而言,并且能量需求大大低于常规细菌o-PO 43-系统。 COD与o-PO43-的减少比例估计为6.5 g COD:1 g o-PO4 3-。真菌氮和磷处理技术进一步发展的主要问题是底物利用率低,这可以通过增加微生物数量来解决。

著录项

  • 作者

    Guest, Rodney Keith.;

  • 作者单位

    University of Alberta (Canada).;

  • 授予单位 University of Alberta (Canada).;
  • 学科 Engineering Environmental.
  • 学位 Ph.D.
  • 年度 2005
  • 页码 150 p.
  • 总页数 150
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 环境污染及其防治;
  • 关键词

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