| contributor author | Ricky C. Clifft | |
| contributor author | Michael W. Barnett | |
| date accessioned | 2017-05-08T21:01:29Z | |
| date available | 2017-05-08T21:01:29Z | |
| date copyright | April 1988 | |
| date issued | 1988 | |
| identifier other | %28asce%290733-9372%281988%29114%3A2%28415%29.pdf | |
| identifier uri | http://yetl.yabesh.ir/yetl/handle/yetl/35787 | |
| description abstract | The validity of a dynamic model based on the two‐film theory is examined for predicting gas transfer in an oxygen system using surface mixers. Model predictions are compared to field measurements taken from a four stage, closed‐tank carbonaceous reactor at the City of Houston, Texas, 69th Street Complex. A liquid film limited model is found to be effective in predicting gas and liquid phase composition although direct interfacial transfer increased the overall oxygen transfer rate. | |
| publisher | American Society of Civil Engineers | |
| title | Gas Transfer Kinetics in Oxygen Activated Sludge | |
| type | Journal Paper | |
| journal volume | 114 | |
| journal issue | 2 | |
| journal title | Journal of Environmental Engineering | |
| identifier doi | 10.1061/(ASCE)0733-9372(1988)114:2(415) | |
| tree | Journal of Environmental Engineering:;1988:;Volume ( 114 ):;issue: 002 | |
| contenttype | Fulltext | |
