Start-up and performance of a downflow fluidised bed reactor for biological treatment of yellow wastewater and nutrient recovery
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作者:
Espinosa-Chavez, Belem
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Univ Mar, Inst Ecol, Ciudad Univ, Puerto Angel 70902, Oaxaca, Mexico
Univ Autonoma Metropolitana, Dept Biotechnol, Av San Rafael Atlixco 186, Mexico City 09340, DF, MexicoUniv Mar, Inst Ecol, Ciudad Univ, Puerto Angel 70902, Oaxaca, Mexico
Espinosa-Chavez, Belem
[1
,2
]
Ramirez-Vives, Florina
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Univ Autonoma Metropolitana, Dept Biotechnol, Av San Rafael Atlixco 186, Mexico City 09340, DF, MexicoUniv Mar, Inst Ecol, Ciudad Univ, Puerto Angel 70902, Oaxaca, Mexico
Ramirez-Vives, Florina
[2
]
Zeeman, Grietje
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Churchillweg 66, NL-6706 AD Wageningen, NetherlandsUniv Mar, Inst Ecol, Ciudad Univ, Puerto Angel 70902, Oaxaca, Mexico
Zeeman, Grietje
[3
]
Monroy-Hermosillo, Oscar
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Univ Autonoma Metropolitana, Dept Biotechnol, Av San Rafael Atlixco 186, Mexico City 09340, DF, MexicoUniv Mar, Inst Ecol, Ciudad Univ, Puerto Angel 70902, Oaxaca, Mexico
Monroy-Hermosillo, Oscar
[2
]
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[1] Univ Mar, Inst Ecol, Ciudad Univ, Puerto Angel 70902, Oaxaca, Mexico
[2] Univ Autonoma Metropolitana, Dept Biotechnol, Av San Rafael Atlixco 186, Mexico City 09340, DF, Mexico
[3] Churchillweg 66, NL-6706 AD Wageningen, Netherlands
The treatment of yellow water (human urine) in a downflow fluidised bed reactor (DFFBR) was investigated to evaluate biological ureolysis and nutrient recovery. The reactor was operated at 30 +/- 4 degrees C in batch mode, and hydraulic retention time=1 d. The average immobilised biomass (as volatile solids, IVS) in the reactor was 2.5 +/- 0.9 g L-support(-1), and specific ureolytic activity was 121 g(-1) Urea-N g(-1) IVS d(-1). The kinetic parameters were 0.152 mol L-1 (K-m) and 8 mol g(-1 )IVS d(-1) (V-max). The ureolysis efficiency was 93.4% and chemical oxygen demand removal efficiency was 31.2%, while total ammonium nitrogen (NH4+-N) production rate was 7 g L-1 d(-1) and phosphate removal reached 26%. Precipitates recovery during biological treatment was 1.72 +/- 0.8 g. These results suggest that the treatment of yellow water in a DFFBR is a viable option for partial recovery of N and P.
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College of Environment and Municipal Engineering, North China University of Water Resources and Electric Power, Zhengzhou 450011, ChinaCollege of Environment and Municipal Engineering, North China University of Water Resources and Electric Power, Zhengzhou 450011, China
Su, Caili
Li, Haihua
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College of Environment and Municipal Engineering, North China University of Water Resources and Electric Power, Zhengzhou 450011, ChinaCollege of Environment and Municipal Engineering, North China University of Water Resources and Electric Power, Zhengzhou 450011, China
Li, Haihua
Tian, Yane
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College of Environment and Municipal Engineering, North China University of Water Resources and Electric Power, Zhengzhou 450011, ChinaCollege of Environment and Municipal Engineering, North China University of Water Resources and Electric Power, Zhengzhou 450011, China
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Univ Fed Parana, Sch Engn, Campus Polytech Ctr, Dept Hydraul & Sanitat, Av Cel Francisco H dos Santos 100, BR-81530990 Curitiba, Parana, BrazilUniv Fed Parana, Sch Engn, Campus Polytech Ctr, Dept Hydraul & Sanitat, Av Cel Francisco H dos Santos 100, BR-81530990 Curitiba, Parana, Brazil
de Morais, Ricardo Goncalves
Braga, Sergio Michelotto
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Univ Fed Parana, Sch Engn, Campus Polytech Ctr, Dept Hydraul & Sanitat, Av Cel Francisco H dos Santos 100, BR-81530990 Curitiba, Parana, BrazilUniv Fed Parana, Sch Engn, Campus Polytech Ctr, Dept Hydraul & Sanitat, Av Cel Francisco H dos Santos 100, BR-81530990 Curitiba, Parana, Brazil
Braga, Sergio Michelotto
Borba Braga, Maria Cristina
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Univ Fed Parana, Sch Engn, Campus Polytech Ctr, Dept Hydraul & Sanitat, Av Cel Francisco H dos Santos 100, BR-81530990 Curitiba, Parana, BrazilUniv Fed Parana, Sch Engn, Campus Polytech Ctr, Dept Hydraul & Sanitat, Av Cel Francisco H dos Santos 100, BR-81530990 Curitiba, Parana, Brazil