| contributor author | D. K. Laughlin | |
| contributor author | F. G. Edwards | |
| contributor author | E. Egemen | |
| contributor author | N. Nirmalakhandan | |
| date accessioned | 2017-05-08T21:26:26Z | |
| date available | 2017-05-08T21:26:26Z | |
| date copyright | March 1999 | |
| date issued | 1999 | |
| identifier other | %28asce%290733-9372%281999%29125%3A3%28285%29.pdf | |
| identifier uri | http://yetl.yabesh.ir/yetl/handle/yetl/51553 | |
| description abstract | The feasibility of bench scale sequencing batch reactors (SBRs) in treating a bottling plant effluent is demonstrated at various influent chemical oxygen demands (CODs) ranging from 300 to over 4,000 mg/L. The SBRs removed over 75% of the biodegradable fraction of the influent COD at a fixed react time of 5.5 h. An easy to use process model is presented to predict the temporal variations of substrate, biomass, and dissolved oxygen concentrations during the fill and react periods in SBRs. The model satisfactorily predicted effluent COD and final biomass concentrations, as well as temporal variations of COD, biomass, and dissolved oxygen throughout the fill and react cycles. | |
| publisher | American Society of Civil Engineers | |
| title | SBR Treatment of High COD Effluent from Bottling Plant | |
| type | Journal Paper | |
| journal volume | 125 | |
| journal issue | 3 | |
| journal title | Journal of Environmental Engineering | |
| identifier doi | 10.1061/(ASCE)0733-9372(1999)125:3(285) | |
| tree | Journal of Environmental Engineering:;1999:;Volume ( 125 ):;issue: 003 | |
| contenttype | Fulltext | |
