Full-scale application of the SHARON process for treatment of rejection water of digested sludge dewatering

At the Rotterdam Dokhaven WWTP the first full-scale application of the SHARON process has been constructed. In the SHARON process, rejection water from dewatering of digested sludge is treated for N-removal. It concerns a highly active process operating without sludge retention. The single tank reac...

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Veröffentlicht in:Water science and technology : a journal of the International Association on Water Pollution Research. - 1986. - 43(2001), 11 vom: 01., Seite 127-34
1. Verfasser: Mulder, J W (VerfasserIn)
Weitere Verfasser: van Loosdrecht, M C, Hellinga, C, van Kempen, R
Format: Aufsatz
Sprache:English
Veröffentlicht: 2001
Zugriff auf das übergeordnete Werk:Water science and technology : a journal of the International Association on Water Pollution Research
Schlagworte:Journal Article Nitrogen Compounds Sewage Water 059QF0KO0R Carbon Dioxide 142M471B3J
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245 1 0 |a Full-scale application of the SHARON process for treatment of rejection water of digested sludge dewatering 
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520 |a At the Rotterdam Dokhaven WWTP the first full-scale application of the SHARON process has been constructed. In the SHARON process, rejection water from dewatering of digested sludge is treated for N-removal. It concerns a highly active process operating without sludge retention. The single tank reactor is intermittently aerated. Due to differences in growth rate nitrite oxidisers are washed out of the system while ammonia oxidisers can be maintained, resulting in N-removal over nitrite. The SHARON process has been selected after comparison with several other techniques. The feed of the SHARON tank is concentrated, with ammonia concentrations over 1 g N/l. The first results show that conversion rates of 90% are quite possible with N-removal mainly via the nitrite route. The process was shown to be stable. Due to the high inlet concentrations pH control is of great importance, preventing process inhibitions. The acidifying effect of nitrification can be compensated completely by CO2 stripping during aeration and by denitrification. Heat production by biological conversions appeared to be significant, due to the high inlet concentrations, and contributes to the optimal operating temperature of 30-40 degrees C 
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650 7 |a Sewage  |2 NLM 
650 7 |a Water  |2 NLM 
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650 7 |a Carbon Dioxide  |2 NLM 
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700 1 |a van Loosdrecht, M C  |e verfasserin  |4 aut 
700 1 |a Hellinga, C  |e verfasserin  |4 aut 
700 1 |a van Kempen, R  |e verfasserin  |4 aut 
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