Optimum cycle time for intermittent UASB reactors treating dairy wastewater

被引:26
作者
Nadais, H
Capela, I
Arroja, L
Duarte, A
机构
[1] Univ Aveiro, Envirorn & Planning Dept, P-3810193 Aveiro, Portugal
[2] Univ Aveiro, Dept Chem, P-3810193 Aveiro, Portugal
关键词
UASB; intermittent operation; dairy wastewater; optimum cycle time; flocculent sludge;
D O I
10.1016/j.watres.2005.01.020
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This work accesses the influence of cycle duration on the intermittent operation of mesophilic UASB reactors inoculated with flocculent sludge and used in dairy wastewater (DWW) treatment. Five cycle lengths ranging from 24 to 144h were compared for loads between 2.5 and 29.0 g COD/l/d. COD balances are presented which demonstrate the importance of a feedless period in the conversion to methane of the substrates removed during the feed period. The maximum applicable loads determined for the system were higher for the longer cycle times. The higher conversion to methane of the removed COD was obtained for the 96 h cycle (48 h feed + 48 h feedless) resulting in a more stable operation. The 96 It cycle (48 h feed + 48 h feedless) was considered as the optimum for the treatment of dairy effluents in intermittent UASB reactors. Compared to the maximum applicable loads reported in the literature for continuous systems (3-6 g COD/l/d) treating dairy effluents the stable operation loads attained with intermittent operation were considerably higher (22 g COD/l/d). (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1511 / 1518
页数:8
相关论文
共 35 条
[11]   UASB-PROCESS DESIGN FOR VARIOUS TYPES OF WASTEWATERS [J].
LETTINGA, G ;
POL, LWH .
WATER SCIENCE AND TECHNOLOGY, 1991, 24 (08) :87-107
[12]  
MARQUES DMLD, 1990, ENVIRON TECHNOL, V11, P1093
[13]   CHANGES TO THE MICROBIAL ECOLOGY IN ANAEROBIC DIGESTERS TREATING ICE-CREAM WASTE-WATER DURING START-UP [J].
MORGAN, JW ;
EVISON, LM ;
FORSTER, CF .
WATER RESEARCH, 1991, 25 (06) :639-653
[14]   Effects of organic, hydraulic and fat shocks on the performance of UASB reactors with intermittent operation [J].
Nadais, H ;
Capela, I ;
Arroja, L ;
Duarte, A .
WATER SCIENCE AND TECHNOLOGY, 2001, 44 (04) :49-56
[15]  
Nadais H., 2002, THESIS U AVEIRO AVEI
[16]  
NADAIS H, IN PRESS TREATMENT D
[17]  
NADAIS H, 2001, 9 WORLD C AN DIG ANT, P203
[18]   Biosorption of milk substrates onto anaerobic flocculent and granular sludge [J].
Nadais, MH ;
Capela, MI ;
Arroja, LM ;
Duarte, AC .
BIOTECHNOLOGY PROGRESS, 2003, 19 (03) :1053-1055
[19]   Anaerobic filter reactor performance for the treatment of complex dairy wastewater at industrial scale [J].
Omil, F ;
Garrido, JM ;
Arrojo, B ;
Méndez, R .
WATER RESEARCH, 2003, 37 (17) :4099-4108
[20]  
PETRUY R, 1999, THESIS AGR U WAGENIN