Sequencing batch reactor biofilm system for treatment of milk industry wastewater

被引:67
作者
Sirianuntapiboon, S [1 ]
Jeeyachok, N
Larplai, R
机构
[1] KMUTT, Sch Energy & Mat, Div Environm Technol, Bangkok 10140, Thailand
[2] KMUTT, Sch Bioresources & Technol, Div Biochem Technol, Bangkok 10140, Thailand
关键词
sequencing batch reactor (SBR); bio-film; milk industry wastewater; excess bio-sludge;
D O I
10.1016/j.jenvman.2005.01.018
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A sequencing batch reactor biofilm (MSBR) system was modified from the conventional sequencing batch reactor (SBR) system by installing 2.7 m(2) surface area of plastic media on the bottom of the reactor to increase the system efficiency and bio-sludge quality by increasing the bio-sludge in the system. The COD, BOD5, total kjeldahl nitrogen (TKN) and oil & grease removal efficiencies of the MSBR system, under a high organic loading of 1340 g BOD5/m(3) d, were 89.3 +/- 0.1, 83.0 +/- 0.2, 59.4 +/- 0.8, and 82.4 +/- 0.4%, respectively, while they were only 87.0 +/- 0.2, 79.9 +/- 0.3, 48.7 +/- 1.7 and 79.3 +/- 10%, respectively, in the conventional SBR system. The amount of excess bio-sludge in the MSBR system was about 3 times lower than that in the conventional SBR system. The sludge volume index (SVI) of the MSBR system was lower than 100 ml/g under an organic loading of up to 1340 g BOD5/m(3) d. However, the MSBR under an organic loading of 680 g BOD5/m(3) d gave the highest COD, BOD5, TKN and oil & grease removal efficiencies of 97.9 +/- 0.0, 97.9 +/- 0.1, 79.3 +/- 1.0 and 94.8 +/- 0.5%, respectively, without any excess bio-sludge waste. The SVI of suspended bio-sludge in the MSBR system was only 44 +/- 3.4 ml/g under an organic loading of 680 a BOD5/m(3) d. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:177 / 183
页数:7
相关论文
共 25 条
[1]  
*APHA AWWA WPCF, 1995, STAND METH EX WAT WA, P535
[2]  
Barnett J. W., 1994, Australasian Biotechnology, V4, P26
[3]  
Cecen F, 1996, J CHEM TECHNOL BIOT, V65, P229, DOI 10.1002/(SICI)1097-4660(199603)65:3<229::AID-JCTB429>3.0.CO
[4]  
2-3
[5]   A new fixed-film mobile bed bioreactor for denitrification of wastewaters [J].
Chudoba, P ;
Pannier, M ;
Truc, A ;
Pujol, R .
WATER SCIENCE AND TECHNOLOGY, 1998, 38 (8-9) :233-240
[6]  
*DEP IND WORKS, 2001, FUND POLL PREV CLEAN
[7]   Carbon and nitrogen removal from a wastewater of an industrial dairy laboratory with a coupled anaerobic filter-sequencing batch reactor system [J].
Garrido, JM ;
Omil, F ;
Arrojo, B ;
Méndez, R ;
Lema, JM .
WATER SCIENCE AND TECHNOLOGY, 2001, 43 (03) :249-256
[8]   Activated sludge biofilm wastewater treatment system [J].
Gebara, F .
WATER RESEARCH, 1999, 33 (01) :230-238
[9]   Simultaneous nitrification/denitrification in an aerobic biofilm system [J].
Helmer, C ;
Kunst, S .
WATER SCIENCE AND TECHNOLOGY, 1998, 37 (4-5) :183-187
[10]   Performance of a two-phase anaerobic digestion system when treating dairy wastewater [J].
Ince, O .
WATER RESEARCH, 1998, 32 (09) :2707-2713