Removal of organic matter and suspended solids by a new configuration of biological aerated filter in the post-treatment of UASB reactor effluent

被引:0
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作者
Della Giustina, Saulo Varela [1 ]
Schiavo Miranda, Luis Alcides [1 ,2 ]
Monteggia, Luiz Olinto [1 ,3 ]
机构
[1] Univ Fed Rio Grande do Sul, Inst Pesquisas Hidraul, BR-90046900 Porto Alegre, RS, Brazil
[2] Univ Vale Rio dos Sinos UNISINOS, Programa Posgrad Engn Civil, Sao Leopoldo, RS, Brazil
[3] Newcastle Univ, Newcastle Upon Tyne NE1 7RU, Tyne & Wear, England
关键词
Post-treatment of UASB reactor; BAS multi-stage; removal of COD; SS removal; WASTE-WATER TREATMENT; PERFORMANCE; MEDIA;
D O I
暂无
中图分类号
TV21 [水资源调查与水利规划];
学科分类号
081501 ;
摘要
The post-treatment of effluents from anaerobic reactors is normally a mandatory step to meet the emission standards. The results presented here show the feasibility of using a new configuration of biological aerated filter (BAF) in the post-treatment of UASB reactors. The multi-stage BAF presents an anaerobic chamber (V=12.6L), followed by an aerobic chamber (V=30L) and an anoxic chamber (V=26.4L), all in series (total V=70L). This study examined the removal of suspended solids (SS), COD and BOD(5). Three multi-stage BAF filled with three different packing materials were used: lids and bottlenecks of PET bottles (165m(2)/m(3)), gravel n. 4 (50m(2)/m(3)) and Pall rings 1.5 '' (135m(2)/m(3)). The reactors were operated with the values of hydraulic detention time (HDT) of 4.1, 8.2 and 12.3 hours, and three superficial application rates (21, 12 and 8m(3)/m(2).d). COD removal efficiencies of 90% for BAF 1 and 3, and 85% for BAF 2 were obtained, being the removal independent of the HDT applied to BAF. The removal of SS was higher in BAF containing Pall rings, probably due to the higher voidage of this material.
引用
收藏
页码:257 / 266
页数:10
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