Simultaneous nitrification-denitrification and clarification in a pseudoliquified activated sludge system

被引:1
作者
Nakhla, GF [1 ]
Lugowski, A
Sverdlikov, A
Scherbina, G
Babcock, K
机构
[1] Univ Western Ontario, Dept Chem & Biochem Engn, London, ON N6A 5B9, Canada
[2] CRA Consulting Engineers, Waterloo, ON, Canada
[3] Dev Inst Municipal Facil & Serv, Kiev, Ukraine
[4] Int Dev Res Council, Ottawa, ON, Canada
关键词
municipal wastewater treatment; nitrogen removal; tertiary treatment; nitrification; denitrification; simultaneous nitrification-denitrification; process modeling;
D O I
10.2175/106143005X41672
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This paper describes results from a pilot study of a novel wastewater treatment technology, which incorporates nutrient removal and solids separation to a single step. The pseudoliquified activated sludge process pilot system was tested on grit removal effluent at flowrates of 29.4 to 54.7 m(3)/d, three different solid residence times (SRT) (15, 37, and 57 days), and over a temperature range of 12 to 28degreesC. Despite wide fluctuations in the influent characteristics, the system performed reliably and consistently with respect to organics and total suspended solids (TSS) removals, achieving biochemical oxygen demand (BOD) and TSS reductions of > 96 % and approximately 90 %, respectively, with BOD5 and TSS concentrations as low as 3 mg/L. Although the system achieved average effluent ammonia concentrations of 2.7 to 3.2 mg/L, nitrification efficiency appeared to be hampered at low temperatures (< 15degreesC). The system achieved tertiary effluent quality with denitrification efficiencies of 90 and 91 % total nitrogen removal efficiency at a total hydraulic retention time of 4.8 hours and an SRT of 12 to 17 days. With ferric chloride addition, effluent phosphorous concentrations of 0.5 to 0.8 mg/L were achieved. Furthermore, because of operation at high biomass concentrations and relatively long biological SRTs, sludge yields were over 50 % below typical values for activated sludge plants. The process was modeled using activated sludge model No. 2, as a two-stage system comprised an aerobic activated sludge system followed by an anoxic system. Model predictions for soluble BOD, ammonia, nitrates, and orthophosphates agreed well with experimental data.
引用
收藏
页码:98 / 112
页数:15
相关论文
共 29 条
[1]  
[Anonymous], 1998, STAND METH EX WAT WA, V20th
[2]  
BARNARD JL, 1973, WATER POLLUT CONTROL, V72, P705
[3]   Dynamic loading tests for final settling tanks [J].
Baumer, P ;
Volkart, P ;
Krebs, P .
WATER SCIENCE AND TECHNOLOGY, 1996, 34 (3-4) :267-274
[4]   Simultaneous nitrification-denitrification process in extended aeration plants: Pilot and real scale experiences [J].
Bertanza, G .
WATER SCIENCE AND TECHNOLOGY, 1997, 35 (06) :53-61
[5]   Biological anoxic phosphorus removal - The dephanox process [J].
Bortone, G ;
Saltarelli, R ;
Alonso, V ;
Sorm, R ;
Wanner, J ;
Tilche, A .
WATER SCIENCE AND TECHNOLOGY, 1996, 34 (1-2) :119-128
[6]  
Collivignarelli C, 1999, WATER SCI TECHNOL, V40, P187, DOI 10.1016/S0273-1223(99)00575-2
[7]   MODELING OF THE SECONDARY CLARIFIER COMBINED WITH THE ACTIVATED-SLUDGE MODEL NO 1 [J].
DUPONT, R ;
HENZE, M .
WATER SCIENCE AND TECHNOLOGY, 1992, 25 (06) :285-300
[8]   Denitrification kinetics in biological N and P removal activated sludge systems treating municipal wastewaters [J].
Ekama, GA ;
Wentzel, MC .
WATER SCIENCE AND TECHNOLOGY, 1999, 39 (06) :69-77
[9]   Difficulties and developments in biological nutrient removal technology and modelling [J].
Ekama, GA ;
Wentzel, MC .
WATER SCIENCE AND TECHNOLOGY, 1999, 39 (06) :1-11
[10]   The cyclic activated sludge system for resort area wastewater treatment [J].
Goronszy, MC ;
Slater, N ;
Konicki, D .
WATER SCIENCE AND TECHNOLOGY, 1995, 32 (9-10) :105-114