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Economic, energy and carbon footprint assessment of integrated forward osmosis membrane bioreactor (FOMBR) process in urban wastewater treatment

机译:城市废水处理中综合前渗透膜生物反应器(FOMBR)过程的经济,能源和碳足迹评估

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The application of forward osmosis (FO) membrane-based technology in urban wastewater treatment has received increased attention, however, its techno-economic feasibility and sustainability have not been fully demonstrated. In this study, the feasibility of FO application in urban wastewater treatment was assessed in terms of economic performance, energy consumption and greenhouse gas (GHG) emissions benchmarked against microfiltration (MF). Three different scenarios of wastewater treatment and water reclamation were proposed: (A) forward osmosis aerobic membrane bioreactor (FOAeMBR); (B) FOAeMBR integrated with reverse osmosis (RO); (C) forward osmosis anaerobic membrane bioreactor (FOAnMBR) integrated with partial nitrification/anammox (PN/AMOX) process. In this study, the wastewater treatment and reclamation costs by using FO in scenarios A and B were more expensive than MF by $0.16 per m(3) and $0.75 per m(3) respectively due to the larger surface area of FO membrane required. In scenario C, the wastewater treatment cost of using FO ($1.11 per m(3)) was equivalent to MF. This was due to the good rejection performance of FO and its ability to concentrate wastewater, hence, resulting in a higher efficiency of (PN/AMOX) in comparison to MF. In addition, the application of FO in scenario C generated total GHG emissions to be as low as 0.93 kg CO2 equivalent m(-3), which was 1.5 and 4.1 times lower than scenarios A and B respectively. The minimal net energy consumption and low carbon footprint of FO application in scenario C suggests this integration will likely be a feasible membrane-based technology for the next generation of wastewater treatment.
机译:前渗透(FO)膜的技术在城市废水处理中的应用受到增加的关注,然而,其技术经济可行性和可持续性尚未完全证明。在这项研究中,根据经济绩效,能源消耗和温室气体(GHG)排放来评估对城市废水处理的可行性,用于针对微滤(MF)的经济性能,能耗和温室气体(GHG)排放。提出了三种不同的废水处理和水填海的情况:(a)前渗透量好氧膜生物反应器(FOAEMBR); (b)FOAEMBR与反渗透(RO)集成; (c)前渗透渗透厌氧膜生物反应器(FOANMBR)与部分硝化/厌氧毒素(PN / Amox)方法集成。在这项研究中,通过在情景A和B中使用FO的废水处理和回收成本比MF更昂贵,每MF为每M(3)和0.75美元,因为所需的膜的表面积较大。在场景C中,使用FO的废水处理成本(每M(3)$ 1.11)相当于MF。这是由于FO的抑制性能及其集中废水的能力,因此与MF相比,导致(PN / Amox)的效率更高。此外,FO在场景C中的应用生成的温室气体排放量低至0.93kg CO2等效M(-3),分别比场景A和B的1.5%和4.1倍。在情景C中应用的最小净能量消耗和低碳足迹表明,这种集成可能是下一代废水处理的可行膜的技术。

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    Univ Queensland Sch Chem Engn Brisbane Qld 1072 Australia;

    Univ Queensland Sch Chem Engn Brisbane Qld 1072 Australia;

    Univ Sydney Sch Chem & Biomol Engn Sydney NSW 2006 Australia;

    Univ Queensland Sch Chem Engn Brisbane Qld 1072 Australia|Ngee Ann Polytech Singapore 599489 Singapore;

    Univ Queensland Sch Chem Engn Brisbane Qld 1072 Australia|Ngee Ann Polytech Singapore 599489 Singapore;

    Univ Queensland Sch Chem Engn Brisbane Qld 1072 Australia;

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