Enhanced biological nitrogen removal in MLE combined with post-denitrification process and EF clarifier

被引:18
作者
Chung, C. M. [2 ]
Cho, K. W. [3 ]
Kim, Y. J. [4 ]
Yamamoto, K. [5 ]
Chung, T. H. [1 ]
机构
[1] Seoul Natl Univ, Dept Civil & Environm Engn, Seoul 151742, South Korea
[2] Univ Tokyo, Dept Urban Engn, Bunkyo Ku, Tokyo 1138656, Japan
[3] Korea Inst Sci & Technol, Water Environm Ctr, Seoul 130650, South Korea
[4] POSCO E&C, R&D Ctr, Inchon, South Korea
[5] Univ Tokyo, Ctr Environm Sci, Bunkyo Ku, Tokyo 1130033, Japan
关键词
Modified ludzack ettinger; Post-denitrification; Electroflotation; Nitrogen removal; ACTIVATED-SLUDGE; DENITRIFICATION; ELECTROFLOTATION; PERFORMANCE; GENERATION; DESIGN;
D O I
10.1007/s00449-011-0623-y
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
A modified ludzack ettinger reactor (MLE) combined with a post-denitrification reactor (PDMLE) using electroflotation (EF) as a secondary clarifier was investigated on its feasibility and process performance. Results indicated that higher mixed liquor suspended solids (MLSS) concentrations in bioreactor (5,350 +/- A 352 mg L-1) were maintained via the highly concentrated return sludge (16,771 +/- A 991 mg L-1) from the EF clarifier and the effluent suspended solids (SS) concentrations continued relatively low, representing effluent SS concentration of 1.71 +/- A 1.16 mg L-1, compared with GS-A2O process during the operation of four months. The denitrification was improved by combining MLE process with post-denitrification based on endogenous decay (i.e. no additional carbon source was added), resulting in the removal efficiencies of TN were about 91 and 59% for the influent C/N ratio of 10 and 5, respectively, revealing relatively high nitrogen removal as compared with EF-A2O and gravity settling (GS)-A2O processes as a control. The nitrogen balance analysis indicates that pre-denitrification and post-denitrification contributed to 78 and 22% of TN removed, respectively.
引用
收藏
页码:503 / 511
页数:9
相关论文
共 24 条
[1]  
ABUFAYED AA, 1986, J WATER POLLUT CON F, V58, P398
[2]  
[Anonymous], 2003, WAST ENG TREATM REUS
[3]  
APHA (AMERICAN PUBLIC HEALTH ASSOCIATION), 1995, Standard Methods for the Examination of Water and Waste Water
[4]   DESIGN AND CONTROL OF FLOTATION THICKENERS [J].
BRATBY, JR ;
AMBROSE, WA .
WATER SCIENCE AND TECHNOLOGY, 1995, 31 (3-4) :247-261
[5]   Microbubble generation for environmental and industrial separations [J].
Burns, SE ;
Yiacoumi, S ;
Tsouris, C .
SEPARATION AND PURIFICATION TECHNOLOGY, 1997, 11 (03) :221-232
[6]   Effect of influent COD/N ratio on biological nitrogen removal (BNR) from high-strength ammonium industrial wastewater [J].
Carrera, J ;
Vicent, T ;
Lafuente, J .
PROCESS BIOCHEMISTRY, 2004, 39 (12) :2035-2041
[7]   Continuous clarification and thickening of activated sludge by electrolytic bubbles under control of scale deposition [J].
Cho, Kang Woo ;
Chung, Chong Min ;
Kim, Yun Jung ;
Chung, Tai Hak .
BIORESOURCE TECHNOLOGY, 2010, 101 (09) :2945-2951
[8]   Improvement of the thickening and dewatering characteristics of activated sludge be electroflotation (EF) [J].
Choi, YG ;
Kim, HS ;
Park, YH ;
Jeong, SH ;
Son, DH ;
Oh, YK ;
Yeom, IT .
WATER SCIENCE AND TECHNOLOGY, 2005, 52 (10-11) :219-226
[9]   Feasibility of electroflotation to separate solids and liquid in an activated sludge process [J].
Chung, C. M. ;
Cho, K. W. ;
Hong, S. W. ;
Kim, Y. J. ;
Chung, T. H. .
ENVIRONMENTAL TECHNOLOGY, 2009, 30 (14) :1565-1573
[10]   Effect of chloride concentration on the electrochemical treatment of a synthetic tannery wastewater [J].
Costa, Carla Regina ;
Olivi, Paulo .
ELECTROCHIMICA ACTA, 2009, 54 (07) :2046-2052