Performance and Kinetics of Membrane and Hybrid Moving Bed Biofilm-Membrane Bioreactors Treating Salinity Wastewater

被引:20
|
作者
Rodriguez-Sanchez, Alejandro [1 ,2 ]
Leyva-Diaz, Juan Carlos [1 ,2 ]
Poyatos, Jose Manuel [1 ,2 ]
Gonzalez-Lopez, Jesus [1 ]
机构
[1] Univ Granada, Inst Water Res, E-18071 Granada, Spain
[2] Univ Granada, Dept Civil Engn, Campus Fuentenueva, E-18071 Granada, Spain
关键词
membrane bioreactor; microbial kinetics; moving bed biofilm reactor; salinity; wastewater; REACTOR; REMOVAL; SYSTEMS; MBR;
D O I
10.1002/aic.15694
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A pilot-plant membrane bioreactor (MBR) and two pilot-plant hybrid moving bed biofilm reactor-membrane bioreactors (MBBR-MBRs), divided into three aerobic and one anoxic chambers, were started up for the treatment of salinity-amended urban wastewater. The MBBR-MBR systems worked with and without carriers in the anoxic zone (MBBR-MBRanox and MBBR-MBRn/anox, respectively). The systems were operated from start-up to stabilization, showing high removal of organic matter-a maximum of 90% chemical oxygen demand and 98% biochemical oxygen demand on the fifth day for MBBR-MBRn/anox in the stabilization phase-but low nitrogen elimination-30% maximum for MBBR-MBRn/anox in the stabilization phase. Biofilm attached to carriers reached less than 50 mg L-1 in the hybrid system. MBR showed faster kinetics than the two MBBR-MBR systems during start-up, but the opposite occurred during stabilization. Maximum specific growth rates for heterotrophic and autotrophic biomass were 0.0500 and 0.0059 h(-1) for MBBR-MBRn/anox in the stabilization phase. (C) 2017 American Institute of Chemical Engineers
引用
收藏
页码:3329 / 3342
页数:14
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