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Entrapped Mixed Microbial Cell Process for Combined Secondary and Tertiary Wastewater Treatment
An entrapped mixed microbial cell (EMMC) process was investigated for simultaneous removal of carbon and nitrogen from a synthetic wastewater in a single bioreactor. The influent had a soluble chemical oxygen demand (SCOD)/nitrogen ratio varying from 4 to 15 and an alkalinity of 140 and 230 mg/L as calcium carbonate. An alternating schedule of intermittent aeration was used for two sizes of carriers: 10 × 10 × 10 mm3 and 20 × 20 × 20 mm3. The medium carrier (10 × 10 × 10 mm3) was found to achieve higher removals of nitrogen, chemical oxygen demand, and 5‐day biochemical oxygen demand of 92, 95, and 97%, respectively. These higher removal rates occurred at a 12‐hour hydraulic retention time (HRT), an aeration/nonaeration ratio of 0.5:2 hours, and an SCOD/nitrogen ratio of 15 in the influent. Influent alkalinity concentrations of 140 and 230 mg/L as calcium carbonate were found to have minimum effect on the removal of carbon and nitrogen. However, the oxidation‐reduction potential, ranging from – 100 to 400 mV (during air‐off period), provides better nitrogen removal efficiency to maintain the total nitrogen (nitrate, nitrite, and ammonium) less than 10 mg/L when an SCOD/nitrogen ratio of 10 or 15 is maintained in the influent. Nitrogen removal efficiency increased with increasing ratios of SCOD/nitrogen in the influent (i.e., SCOD/nitrogen ratio of 15 > 10 > 7 > 4.0). The results of actual wastewater operation based on a study of synthetic wastewater show that organics removal efficiencies (94.6 and 94.2%) and nitrogen removal efficiencies (61.0 and 60.9%) are similar for reactors packed with medium and large carriers, respectively, when they are operated with a 9‐hour HRT, an air on/air off ratio of 1 hour:2 hours and an SCOD/nitrogen ratio of 4.6.
Entrapped Mixed Microbial Cell Process for Combined Secondary and Tertiary Wastewater Treatment
An entrapped mixed microbial cell (EMMC) process was investigated for simultaneous removal of carbon and nitrogen from a synthetic wastewater in a single bioreactor. The influent had a soluble chemical oxygen demand (SCOD)/nitrogen ratio varying from 4 to 15 and an alkalinity of 140 and 230 mg/L as calcium carbonate. An alternating schedule of intermittent aeration was used for two sizes of carriers: 10 × 10 × 10 mm3 and 20 × 20 × 20 mm3. The medium carrier (10 × 10 × 10 mm3) was found to achieve higher removals of nitrogen, chemical oxygen demand, and 5‐day biochemical oxygen demand of 92, 95, and 97%, respectively. These higher removal rates occurred at a 12‐hour hydraulic retention time (HRT), an aeration/nonaeration ratio of 0.5:2 hours, and an SCOD/nitrogen ratio of 15 in the influent. Influent alkalinity concentrations of 140 and 230 mg/L as calcium carbonate were found to have minimum effect on the removal of carbon and nitrogen. However, the oxidation‐reduction potential, ranging from – 100 to 400 mV (during air‐off period), provides better nitrogen removal efficiency to maintain the total nitrogen (nitrate, nitrite, and ammonium) less than 10 mg/L when an SCOD/nitrogen ratio of 10 or 15 is maintained in the influent. Nitrogen removal efficiency increased with increasing ratios of SCOD/nitrogen in the influent (i.e., SCOD/nitrogen ratio of 15 > 10 > 7 > 4.0). The results of actual wastewater operation based on a study of synthetic wastewater show that organics removal efficiencies (94.6 and 94.2%) and nitrogen removal efficiencies (61.0 and 60.9%) are similar for reactors packed with medium and large carriers, respectively, when they are operated with a 9‐hour HRT, an air on/air off ratio of 1 hour:2 hours and an SCOD/nitrogen ratio of 4.6.
Entrapped Mixed Microbial Cell Process for Combined Secondary and Tertiary Wastewater Treatment
Yang, P.Y. (Autor:in) / Cao, K. (Autor:in) / Kim, S.J. (Autor:in)
Water Environment Research ; 74 ; 226-234
01.05.2002
9 pages
Aufsatz (Zeitschrift)
Elektronische Ressource
Englisch
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