Control of a swine manure treatment process using a specific feature of oxidation reduction potential

被引:24
作者
Ra, CS
Lo, KV
Mavinic, DS
机构
[1] Univ British Columbia, Chem & Bioresource Engn Dept, Vancouver, BC V6T 1Z4, Canada
[2] Univ British Columbia, Dept Civil Engn, Environm Engn Grp, Vancouver, BC V6T 1Z4, Canada
[3] Kangweon Natl Univ, Anim Resource Res Inst, Chunchon 200701, South Korea
关键词
oxidation-reduction potential (ORP); real-time control; nitrogen break point; moving range (MRG); swine manure;
D O I
10.1016/S0960-8524(99)00035-8
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
A real-time control strategy for waste treatment, using a specific feature of oxidation-reduction potential (ORP) feature, was developed; the usefulness of this technology was evaluated through two separate operations. A newly designed, two-stage, bench-scale wastewater treatment process for swine wastewater was successfully operated with this real-time control technology. The nitrogen break point (NBP) on the ORP-time profile was designated as a real-lime control point. By designating the NBP as such, sufficient organic carbon matter for denitrification could be left in the mixed liquor and completely removed during denitrification. Since the treatment stages were not controlled by a timer, but by the ORP real-time control point, the process could provide consistently high reduction of combined organic carbon (C), nitrogen (N) and phosphorus (P) concentrations, despite the large fluctuation of animal wastewater characteristics. The average system performance, relative to influent strength, was in excess of 96% for the C, N and P. Real-time control techniques worked effectively without the addition of an external carbon source in the treatment of swine manure: effective N and P removal was achieved, using internally available organic matter. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:117 / 127
页数:11
相关论文
共 12 条
[1]  
*AM PUBL HLTH ASS, 1995, STAND METH EX WAT WA
[2]   Denitrification behaviour in biological excess phosphorus removal activated sludge systems [J].
Barker, PS ;
Dold, PL .
WATER RESEARCH, 1996, 30 (04) :769-780
[3]   NITRIFICATION, DENITRIFICATION AND BIOLOGICAL PHOSPHATE REMOVAL IN SEQUENCING BATCH REACTORS TREATING PIGGERY WASTE-WATER [J].
BORTONE, G ;
GEMELLI, S ;
RAMBALDI, A ;
TILCHE, A .
WATER SCIENCE AND TECHNOLOGY, 1992, 26 (5-6) :977-985
[4]   Microbiological Basis of Phosphate Removal in the Activated Sludge Process for the Treatment of Wastewater [J].
Fuhs, G. W. ;
Chen, Min .
MICROBIAL ECOLOGY, 1975, 2 (02) :119-138
[5]   ANAEROBIC AEROBIC BIOLOGICAL TREATMENT OF SCREENED DAIRY MANURE [J].
LO, KV ;
LIAO, PH .
BIOMASS, 1986, 10 (03) :187-193
[6]  
Ng W. J., 1987, Biological Wastes, V22, P285
[7]   REMOVAL OF NITROGEN AND PHOSPHORUS FROM SWINE WASTE-WATER BY THE ACTIVATED-SLUDGE UNITS WITH THE INTERMITTENT AERATION PROCESS [J].
OSADA, T ;
HAGA, K ;
HARADA, Y .
WATER RESEARCH, 1991, 25 (11) :1377-1388
[8]   Real-time control of nitrogen removal using three ORP bending-points: Signification, control strategy and results [J].
PlissonSaune, S ;
Capdeville, B ;
Mauret, M ;
Deguin, A ;
Baptiste, P .
WATER SCIENCE AND TECHNOLOGY, 1996, 33 (01) :275-280
[9]   Real-time control of two-stage sequencing batch reactor system for the treatment of animal wastewater [J].
Ra, CS ;
Lo, KV ;
Mavinic, DS .
ENVIRONMENTAL TECHNOLOGY, 1998, 19 (04) :343-356
[10]   Phosphate uptake under anoxic conditions and fixed-film nitrification in nutrient removal activated sludge system [J].
Sorm, R ;
Bortone, G ;
Saltarelli, R ;
Jenicek, P ;
Wanner, J ;
Tilche, A .
WATER RESEARCH, 1996, 30 (07) :1573-1584