Start-up and performance of a downflow fluidised bed reactor for biological treatment of yellow wastewater and nutrient recovery

被引:1
作者
Espinosa-Chavez, Belem [1 ,2 ]
Ramirez-Vives, Florina [2 ]
Zeeman, Grietje [3 ]
Monroy-Hermosillo, Oscar [2 ]
机构
[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
关键词
downflow fluidised bed reactor; kinetic parameters; struvite; ureolysis; yellow water; SOURCE-SEPARATED URINE; UREA HYDROLYSIS; STRUVITE CRYSTALLIZATION; PHOSPHORUS RECOVERY; PRECIPITATION; REMOVAL; PH; FORMALDEHYDE; UREOLYSIS; SEAWATER;
D O I
10.2166/wst.2022.167
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
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.
引用
收藏
页码:3208 / 3224
页数:17
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