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首页> 外文期刊>Environmental Science: Water Research & Technology >A sequential membrane bioreactor followed by a membrane microalgal reactor for nutrient removal and algal biomass production
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A sequential membrane bioreactor followed by a membrane microalgal reactor for nutrient removal and algal biomass production

机译:序列膜生物反应器,然后是膜微藻反应器用于营养去除和藻类生物量产生

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A hybrid process combining a single compartment aerobic membrane bioreactor (MBR) and a membrane microalgal reactor (MMR) was evaluated for nutrient removal and microalgal biomass production. When operated without biomass extraction, the microalgal biomass in the MMR reached 920 mg L-1 on day 18 and then collapsed, rendering nutrient removal ineffective. Stable operation of the MMR was achieved by regular biomass extraction (i.e. 1/30 of the microalgal biomass in the reactor daily). The biomass production at steady state was approximately 26 g m(-3) d(-1). The NO3- and PO43- uptake values by microalgae were 4.0 +/- 1.1 and 1.5 +/- 0.9 g m(-3) d(-1), respectively. A facile flocculation and separation technique capable of recovering 98% microalgal biomass was demonstrated. Although the hybrid process can significantly enhance nutrient removal and biomass production, further research is needed to intensify the microalgal growth rate. At the current microalgal growth rate, a large MMR volume (37 times that of the MBR) is necessary for synchronous operation.
机译:评价组合单个隔室有氧膜生物反应器(MBR)和膜微藻反应器(MMR)的杂化过程以进行营养去除和微藻生物量产生。当没有生物质萃取的情况下操作时,MMR中的微藻生物量在第18天达到920mg L-1,然后折叠,呈现营养成分无效。通过常规生物质萃取(即,每天反应器中的微藻生物质中的1/30)实现MMR的稳定操作。稳态的生物质产生约为26g m(-3)d(-1)。 Microalgae的NO3和PO43摄取值分别为4.0 +/- 1.1和1.5 +/- 0.9g m(-3)d(-1)。证明了能够回收98%微藻生物量的容易絮凝和分离技术。虽然杂化过程可以显着增强营养消除和生物质生产,但需要进一步研究来加强微藻生长速率。在目前的微藻生长速率下,同步操作需要大的MMR体积(MBR的37倍)。

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    Univ Technol Sydney Sch Civil & Environm Engn Ctr Technol Water & Wastewater Sydney NSW 2007 Australia;

    Univ Technol Sydney Sch Civil & Environm Engn Ctr Technol Water & Wastewater Sydney NSW 2007 Australia;

    Univ Technol Sydney Sch Civil & Environm Engn Ctr Technol Water & Wastewater Sydney NSW 2007 Australia;

    Univ Technol Sydney Sch Civil & Environm Engn Ctr Technol Water & Wastewater Sydney NSW 2007 Australia;

    Univ Technol Sydney C3 Sydney NSW 2007 Australia;

    Univ Technol Sydney C3 Sydney NSW 2007 Australia;

    Western Sydney Univ Tech Serv Kingswood NSW 2747 Australia;

    Univ Technol Sydney Sch Civil & Environm Engn Ctr Technol Water & Wastewater Sydney NSW 2007 Australia|Nguyen Tat Thanh Univ NTT Inst Hitechnol Ho Chi Minh City Vietnam;

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