## Abstract The biodegradation of syntheticallyโprepared phenol wastewater was studied in a single stage, benchโscale rotating biological contactor (RBC). The effect of process variables, namely rotational speed (40โ175โrpm), input phenol loading (1754โ3508โmg phenol m^โ2^โh^โ1^), input hydraulic l
Modeling of rotating biological contactor systems
โ Scribed by Yeun C. Wu; Ed D. Smith; Yung T. Hung
- Publisher
- John Wiley and Sons
- Year
- 1980
- Tongue
- English
- Weight
- 421 KB
- Volume
- 22
- Category
- Article
- ISSN
- 0006-3592
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โฆ Synopsis
Abstract
An investigation of the rotating biological contractor (RBC) process variables to determine the efficiency of biological oxygen demand (BOD) removal is presented. Operating parameters including influent BOD content (<355 mg/liter), flow rate, disk surface area, hydraulic loading, disk rotational speed, liquid retention time, stage number, and wastewater temperature were evaluated. The BOD predictive model was developed using literature data with multiple regression analysis. This study shows that influent BOD concentration, hydraulic loading, stage number, and wastewater temperature are the most significant variables in predicting the RBC system performance. The model presently developed was verified by field data concerned with the treatment of both domestic and lowโstrength industrial wastewaters. Also, the results calculated by this model were compared to those obtained from Weng's model.
๐ SIMILAR VOLUMES
## Abstract In this study, the mass transfer efficiencies of a novel horizontal rotating packed (hโRPB) bed and the conventional discโtype rotating biological contactor (RBC) were studied at four speeds and seven submergences. Pall rings of two different sizes (25, 38 mm), superintalox saddles and