Department of Civil and Environmental Engineering, The Pennsylvania State University, 231Q Sackett Building, University Park, PA 16802, USA.
Department of Civil and Environmental Engineering, The Pennsylvania State University, 231Q Sackett Building, University Park, PA 16802, USA.
Bioresour Technol. 2016 May;208:58-63. doi: 10.1016/j.biortech.2016.02.067. Epub 2016 Feb 22.
Anaerobic fluidized membrane bioreactors (AFMBRs) have been mainly developed as a post-treatment process to produce high quality effluent with very low energy consumption. The performance of an AFMBR was examined using the effluent from a microbial fuel cell (MFC) treating domestic wastewater, as a function of AFMBR hydraulic retention times (HRTs) and organic matter loading rates. The MFC-AFMBR achieved 89 ± 3% removal of the chemical oxygen demand (COD), with an effluent of 36 ± 6 mg-COD/L over 112 days operation. The AFMBR had very stable operation, with no significant changes in COD removal efficiencies, for HRTs ranging from 1.2 to 3.8h, although the effluent COD concentration increased with organic loading. Transmembrane pressure (TMP) was low, and could be maintained below 0.12 bar through solids removal. This study proved that the AFMBR could be operated with a short HRT but a low COD loading rate was required to achieve low effluent COD.
厌氧流动膜生物反应器(AFMBR)主要作为一种后处理工艺开发,以非常低的能耗生产高质量的出水。研究了 AFMBR 水力停留时间(HRT)和有机物负荷率对处理生活污水的微生物燃料电池(MFC)出水的性能。在 112 天的运行过程中,MFC-AFMBR 对化学需氧量(COD)的去除率达到 89±3%,出水 COD 为 36±6mg/L。AFMBR 运行非常稳定,COD 去除效率没有明显变化,HRT 范围为 1.2-3.8h,尽管随着有机负荷的增加,出水 COD 浓度也随之增加。跨膜压力(TMP)较低,通过固体去除可将其维持在 0.12 巴以下。这项研究证明,AFMBR 可以在较短的 HRT 下运行,但需要较低的 COD 负荷率才能达到低的出水 COD。