Application of biochemical oxygen demand (BOD) biosensor for optimization of biological carbon and nitrogen removal from synthetic wastewater in a sequencing batch reactor system

被引:23
作者
Jang, JD
Barford, JP [1 ]
Lindawati
Renneberg, R
机构
[1] Hong Kong Univ Sci & Technol, Dept Chem Engn, Hong Kong, Hong Kong, Peoples R China
[2] Hong Kong Univ Sci & Technol, Dept Chem, Hong Kong, Hong Kong, Peoples R China
[3] Univ Surabaya, Dept Chem Engn, Raya Kalirungkut, Surabaya, Indonesia
关键词
SBR; BOD biosensor; real time; optimization; carbon; nitrogen removal;
D O I
10.1016/j.bios.2003.08.009
中图分类号
Q6 [生物物理学];
学科分类号
071011 ;
摘要
A bench scale reactor using a sequencing batch reactor process was used to evaluate the applicability of biosensors for the process optimization of biological carbon and nitrogen removal. A commercial biochemical oxygen demand (BOD) biosensor with a novel microbial membrane was used to determine the duration of each phase by measuring samples in real time in an SBR cycle with filling/anoxic-anaerobic/aerobic/sludge wasting/settling/withdrawal periods. Possible strategies to increase the efficiency for the biological removal of carbon and nitrogen from synthetic wastewater have been developed. The results show that application of a BOD biosensor enables estimation of organic carbon, in real time, allowing the optimization or reduction the SBR cycle time. Some typical consumption patterns for organic carbon in the non-aeration phase of a typical SBR operation were identified. The rate of decrease of BOD measured using a sensor BOD, was the highest in the initial glucose breakdown period and during denitrification. It then slowed down until a 'quiescent period' was observed, which may be considered as the commencement of the aeration period. Monitoring the BOD curve with a BOD biosensor allowed the reduction of the SBR cycle time, which leads to an increase in the removal efficiency. By reducing the cycle time from 8 to 4 h cycle, the removal efficiencies of nitrate, glucose, and phosphorus in a given time interval, were increased to nearly double, while the removal of nitrogen ammonium was increased by one-third. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:805 / 812
页数:8
相关论文
共 16 条
[1]   COMBINED ORGANIC-CARBON AND COMPLETE NITROGEN REMOVAL USING ANAEROBIC AND AEROBIC UPFLOW FILTERS [J].
AKUNNA, J ;
BIZEAU, C ;
MOLETTA, R ;
BERNET, N ;
HEDUIT, A .
WATER SCIENCE AND TECHNOLOGY, 1994, 30 (12) :297-306
[2]  
[Anonymous], 2001, SEQUENCING BATCH REA
[3]  
BARFORD JP, 2000, P 2 INT S SEQ BATCH, P23
[4]   SBR as a relevant technology to combine anaerobic digestion and denitrification in a single reactor [J].
Bernet, N ;
Delgenès, N ;
Delgenès, JP ;
Moletta, R .
WATER SCIENCE AND TECHNOLOGY, 2001, 43 (03) :209-214
[5]   Measurement of biodegradable substances using the salt-tolerant yeast Arxula adeninivorans for a microbial sensor immobilized with poly(carbamoyl) sulfonate (PCS) part I:: Construction and characterization of the microbial sensor [J].
Chan, CY ;
Lehmann, M ;
Tag, K ;
Lung, M ;
Kunze, G ;
Riedel, K ;
Gruendig, B ;
Renneberg, R .
BIOSENSORS & BIOELECTRONICS, 1999, 14 (02) :131-138
[6]   Strategy for nitrogen removal from piggery waste [J].
Choi, E ;
Eum, Y .
WATER SCIENCE AND TECHNOLOGY, 2002, 46 (6-7) :347-354
[7]   THE EFFECT OF PARTICULATE ORGANIC-MATTER ON BIOFILM NITRIFICATION [J].
FIGUEROA, LA ;
SILVERSTEIN, J .
WATER ENVIRONMENT RESEARCH, 1992, 64 (05) :728-733
[8]   EFFECTS OF THE ACTIVITY OF HETEROTROPHS ON NITRIFICATION IN A SUSPENDED-GROWTH REACTOR [J].
HANAKI, K ;
WANTAWIN, C ;
OHGAKI, S .
WATER RESEARCH, 1990, 24 (03) :289-296
[9]   NITRIFICATION AT LOW-LEVELS OF DISSOLVED-OXYGEN WITH AND WITHOUT ORGANIC LOADING IN A SUSPENDED-GROWTH REACTOR [J].
HANAKI, K ;
WANTAWIN, C ;
OHGAKI, S .
WATER RESEARCH, 1990, 24 (03) :297-302
[10]  
Horan N.J., 1990, Biological Wastewater Treatment Systems, Theory and Operation