Comparison of two PAC/UF processes for the removal of micropollutants from wastewater treatment plant effluent: Process performance and removal efficiency

2014 ◽  
Vol 56 ◽  
pp. 26-36 ◽  
Author(s):  
Jonas Löwenberg ◽  
Armin Zenker ◽  
Martin Baggenstos ◽  
Gerhard Koch ◽  
Christian Kazner ◽  
...  
Keyword(s):  
Wastewater Treatment ◽  
Removal Efficiency ◽  
Wastewater Treatment Plant ◽  
Treatment Plant ◽  
Process Performance ◽  
Wastewater Treatment Plant Effluent

Influence of temperature on process performance of activated sludge in coking wastewater treatment plant

2011 ◽  
Vol 6 (1) ◽  
Author(s):  
Chu-I Cheng ◽  
Yu Mei Chao ◽  
Ming-Chuan Lin ◽  
Chiung-Hsun Lin
Keyword(s):  
Wastewater Treatment ◽  
Activated Sludge ◽  
Water Temperature ◽  
Removal Efficiency ◽  
Wastewater Treatment Plant ◽  
Removal Rate ◽  
Treatment Plant ◽  
Alternative Measure ◽  
Coking Wastewater ◽  
Process Performance

Coking wastewater contains toxic compounds such as ammonia, phenolics, cyanides, thiocyanate, and thiosulfate. In normal situation, these compounds can be 100% decomposed by activated sludge in the wastewater treatment plant. However, a new factor, high water temperature, caused by the covering of the basins, has been found to reduce the removal rate of the pollutants, especially the thiocyanate. Several remediation measures were applied to improve the biological process performance. A series of batch and continuous-flow biodegradation tests have demonstrated that the relatively low temperature ranging from 20 to 37°C attained perfect removal efficiency (∼100%) of SCN− from the coke plant wastewater. When the temperature is increased to 38, 39°C, the SCN− removal rate decreased to 30 ∼ 50% after 48 hours of temperature shift. Moreover, when the temperature is increased to 40 to 45°C, SCN− biodegradation is significantly decayed one day after the temperature shock, and the SCN− removal efficiency dropped gradually to 0%, with microbial deterioration during day 1 to day 4. Meanwhile, the COD removal has also decreased from 85% down to 45% at 45°C. Both laboratory verifications confirmed that 40°C should be the critical water temperature for the SCN− degrading microbe to function well in the activated sludge process. In order to stabilize the pollutant removing ability of the procedure, the water temperature of aeration basin is set to operate under 37°C. Four modifications were practiced on site to decrease the temperature of activated sludge. Only the last alternative measure worked well with the opened hand hole, 50% of total cover area, to discharge the water vapor and gas emission from the head space of aeration basin. The water temperature has dropped from 41 to 36°C in the early summer of June with ambient temperature of 37°C, suggesting that partially uncovering the basin does help maintain the water temperature. Finally, we suggest some measures that can be applied to establish a standard process on site in order to ensure that the aeration basin temperature stays under 37°C and that our biotreatment system can maintain its function in the future.

Modelling the performance of anaerobic wastewater stabilization ponds

1995 ◽  
Vol 31 (12) ◽  
pp. 171-183 ◽  
Author(s):  
M. M. Saqqar ◽  
M. B. Pescod
Keyword(s):  
Wastewater Treatment ◽  
Water Temperature ◽  
Removal Efficiency ◽  
Wastewater Treatment Plant ◽  
Suspended Solids ◽  
Treatment Plant ◽  
Pond Water ◽  
Removal Efficiencies ◽  
Wastewater Stabilization Ponds ◽  
Raw Wastewater

The performance of the primary anaerobic pond at the Alsamra Wastewater Treatment Plant in Jordan was monitored over 48 months. Overall averages for the removal efficiencies of BOD5, COD and suspended solids were 53%, 53% and 74%, respectively. An improvement in removal efficiency with increase in pond water temperature was demonstrated. A model, which takes into account the variability of raw wastewater at different locations, has been developed to describe the performance of a primary anaerobic pond in terms of a settleability ratio for the raw wastewater. The model has been verified by illustrating the high correlation between actual and predicted pond performance.

scholarly journals Persulfate mediated solar photo-Fenton aiming at wastewater treatment plant effluent improvement at neutral PH: emerging contaminant removal, disinfection, and elimination of antibiotic-resistant bacteria

2021 ◽  
Author(s):  
Maria Clara V. M. Starling ◽  
Elizângela P. Costa ◽  
Felipe A. Souza ◽  
Elayne C. Machado ◽  
Juliana Calábria de Araujo ◽  
...  
Keyword(s):  
Wastewater Treatment ◽  
Wastewater Treatment Plant ◽  
Treatment Plant ◽  
Resistant Bacteria ◽  
Antibiotic Resistant Bacteria ◽  
Antibiotic Resistant ◽  
E Coli ◽  
Effluent Quality ◽  
Neutral Ph ◽  
Wastewater Treatment Plant Effluent

AbstractThis work investigated an innovative alternative to improve municipal wastewater treatment plant effluent (MWWTP effluent) quality aiming at the removal of contaminants of emerging concern (caffeine, carbendazim, and losartan potassium), and antibiotic-resistant bacteria (ARB), as well as disinfection (E. coli). Persulfate was used as an alternative oxidant in the solar photo-Fenton process (solar/Fe/S2O82−) due to its greater stability in the presence of matrix components. The efficiency of solar/Fe/S2O82− at neutral pH using intermittent iron additions is unprecedented in the literature. At first, solar/Fe/S2O82− was performed in a solar simulator (30 W m−2) leading to more than 60% removal of CECs, and the intermittent iron addition strategy was proved effective. Then, solar/Fe/S2O82− and solar/Fe/H2O2 were compared in semi-pilot scale in a raceway pond reactor (RPR) and a cost analysis was performed. Solar/Fe/S2O82− showed higher efficiencies of removal of target CECs (55%), E. coli (3 log units), and ARB (3 to 4 log units) within 1.9 kJ L−1 of accumulated irradiation compared to solar/Fe/H2O2 (CECs, 49%; E. coli, 2 log units; ARB, 1 to 3 log units in 2.5 kJ L−1). None of the treatments generated acute toxicity upon Allivibrio fischeri. Lower total cost was obtained using S2O82− (0.6 € m−3) compared to H2O2 (1.2 € m−3). Therefore, the iron intermittent addition aligned to the use of persulfate is suitable for MWWTP effluent quality improvement at neutral pH.

Inactivation of Clostridium perfringens, Total Coliforms, and Escherichia coli by UV/H2O2 in Wastewater Treatment Plant Effluent

2016 ◽  
Vol 19 (1) ◽  
Author(s):  
José Roberto Guimarães ◽  
Regiane Aparecida Guadagnini ◽  
Regina Maura Bueno Franco ◽  
Luciana Urbano dos Santos
Keyword(s):  
Escherichia Coli ◽  
Wastewater Treatment ◽  
Clostridium Perfringens ◽  
Wastewater Treatment Plant ◽  
Treatment Plant ◽  
Total Coliforms ◽  
Wastewater Treatment Plant Effluent

AbstractThis study evaluated the effectiveness of H

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