Performance of bench-scale membrane bioreactor under real work conditions using pure oxygen: viscosity and oxygen transfer analysis

被引:15
作者
Rodriguez, F. A. [1 ,2 ]
Martinez-Toledo, M. V. [2 ]
Gonzalez-Lopez, J. [2 ]
Hontoria, E. [1 ,2 ]
Poyatos, J. M. [1 ,2 ]
机构
[1] Univ Granada, Dept Civil Engn, ETSICCP, E-18071 Granada, Spain
[2] Univ Granada, Inst Water Res, E-18071 Granada, Spain
关键词
Membrane bioreactor; Wastewater; Re-uses; Pure oxygen; Sludge viscosity; WASTE-WATER TREATMENT; ACTIVATED-SLUDGE; RATES;
D O I
10.1007/s00449-010-0411-0
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Pure oxygen to supply the aerobic condition was used in the performance of a bench-scale submerged membrane bioreactor (MBR). The pilot plant was located in the wastewater treatment plant of the city of Granada (Spain) and the experimental work was divided into two stages (Unsteady state and steady state conditions). Operation parameters (MLSS, MLVSS and dissolved oxygen concentration) and physical characteristics (temperature, conductivity, pH, COD and BOD(5)) were daily monitored. The results showed the capacity of the MBR systems to remove organic material under a hydraulic retention time of 18.46 h and sludge retention time of 18.6 days. Therefore, Viscosity of the sludge and alpha kLa-factor of the aeration, were determinate in the steady stage condition to understand the behavior of the system when pure oxygen has been used to supply the aerobic conditions of the MBR system showed an alpha-factor of 0.238 when the viscosity of the system was 4.04 Cp.
引用
收藏
页码:885 / 892
页数:8
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