Performance of plastic- and sponge-based trickling filters treating effluents from an UASB reactor

被引:19
作者
Almeida, P. G. S. [1 ]
Marcus, A. K. [2 ]
Rittmann, B. E. [2 ]
Chernicharo, C. A. L. [1 ]
机构
[1] Univ Fed Minas Gerais, Dept Sanit & Environm Engn, Belo Horizonte, MG, Brazil
[2] Arizona State Univ, Swette Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ USA
关键词
domestic wastewater; packing media; post-treatment; trickling filter; UASB reactor; UASB/TF system; SEWAGE-TREATMENT SYSTEM; WASTE-WATER; COMBINATION;
D O I
10.2166/wst.2013.658
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The paper compares the performance of two trickling filters (TFs) filled with plastic-or sponge-based packing media treating the effluent from an upflow anaerobic sludge blanket (UASB) reactor. The UASB reactor was operated with an organic loading rate (OLR) of 1.2 kgCOD m(-3) d(-1), and the OLR applied to the TFs was 0.30-0.65 kgCOD m(-3) d(-1) (COD: chemical oxygen demand). The sponge-based packing medium (Rotosponge) gave substantially better performance for ammonia, total-N, and organic matter removal. The superior TF-Rotosponge performance for NH4+-N removal (80-95%) can be attributed to its longer biomass and hydraulic retention times (SRT and HRT), as well as enhancements in oxygen mass transfer by dispersion and advection inside the sponges. Nitrogen removals were significant (15 mgN L-1) in TF-Rotosponge when the OLRs were close to 0.75 kgCOD m(-3) d(-1), due to denitrification that was related to solids hydrolysis in the sponge interstices. For biochemical oxygen demand removal, higher HRT and SRT were especially important because the UASB removed most of the readily biodegradable organic matter. The new configuration of the sponge-based packing medium called Rotosponge can enhance the feasibility of scaling-up the UASB/TF treatment, including when retrofitting is necessary.
引用
收藏
页码:1034 / 1042
页数:9
相关论文
共 19 条
[1]  
[Anonymous], 2003, WASTEWATER ENG TREAT
[2]  
[Anonymous], WATER SCI TECHNOLOGY
[3]  
[Anonymous], 2005, Standard methods for the examination of water and waste- water
[4]   Quantification of the Inert Chemical Oxygen Demand of Raw Wastewater and Evaluation of Soluble Microbial Product Production in Demo-Scale Upflow Anaerobic Sludge Blanket Reactors under Different Operational Conditions [J].
Aquino, Sergio F. ;
Gloria, Roberto M. ;
Silva, Silvana Q. ;
Chernicharo, Carlos A. L. .
WATER ENVIRONMENT RESEARCH, 2009, 81 (06) :608-616
[5]   Behaviors of nitrifiers in a novel biofilm reactor employing hanging sponge-cubes as attachment site [J].
Araki, N ;
Ohashi, A ;
Machdar, I ;
Harada, H .
WATER SCIENCE AND TECHNOLOGY, 1999, 39 (07) :23-31
[6]   Post-treatment options for the anaerobic treatment of domestic wastewater [J].
Chernicharo C.A.L. .
Reviews in Environmental Science and Bio/Technology, 2006, 5 (1) :73-92
[7]  
Chernicharo C. A. L., 2010, P C SUST SOL SMALL W
[8]   Nitrous oxide generation in full-scale biological nutrient removal wastewater treatment plants [J].
Foley, Jeffrey ;
de Haas, David ;
Yuan, Zhiguo ;
Lant, Paul .
WATER RESEARCH, 2010, 44 (03) :831-844
[9]   Sequential anaerobic-aerobic treatment for domestic wastewater - A review [J].
Kassab, G. ;
Halalsheh, M. ;
Klapwijk, A. ;
Fayyad, M. ;
van Lier, J. B. .
BIORESOURCE TECHNOLOGY, 2010, 101 (10) :3299-3310
[10]  
Machdar I, 1997, WATER SCI TECHNOL, V36, P189, DOI 10.2166/wst.1997.0447