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

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 °C in batch mode, and reaction time = 1 d. The average immobilised biomass (as volatile solids, IVS) in th...

Full description

Bibliographic Details
Main Authors: Belem Espinosa-Chávez, Florina Ramírez-Vives, Grietje Zeeman, Oscar Monroy-Hermosillo
Format: Article
Language:English
Published: IWA Publishing 2022-06-01
Series:Water Science and Technology
Subjects:
Online Access:http://wst.iwaponline.com/content/85/11/3208
_version_ 1798041016922537984
author Belem Espinosa-Chávez
Florina Ramírez-Vives
Grietje Zeeman
Oscar Monroy-Hermosillo
author_facet Belem Espinosa-Chávez
Florina Ramírez-Vives
Grietje Zeeman
Oscar Monroy-Hermosillo
author_sort Belem Espinosa-Chávez
collection DOAJ
description 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 °C in batch mode, and reaction time = 1 d. The average immobilised biomass (as volatile solids, IVS) in the reactor was 2.5±0.9 g L−1support, and specific ureolytic activity was 121 g Urea-N g−1 IVS d−1. The kinetic parameters were 0.152 mol L−1 (Km) and 8 mol g−1 IVS d−1 (Vmax). 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. HIGHLIGHTS A new biological treatment of yellow water is proposed.; Yellow waters were treated effectively in a downflow fluidised bed reactor.; The biological ureolysis of human urine was reached within six hours.; After addition of Mg2+/PO43− (1.6/1), 82.3 g of precipitates were recovered.; Struvite was the major component of the recovered precipitates.;
first_indexed 2024-04-11T22:15:36Z
format Article
id doaj.art-a7f24542371c49f69977a70bcdabb4cf
institution Directory Open Access Journal
issn 0273-1223
1996-9732
language English
last_indexed 2024-04-11T22:15:36Z
publishDate 2022-06-01
publisher IWA Publishing
record_format Article
series Water Science and Technology
spelling doaj.art-a7f24542371c49f69977a70bcdabb4cf2022-12-22T04:00:26ZengIWA PublishingWater Science and Technology0273-12231996-97322022-06-0185113208322410.2166/wst.2022.167167Start-up and performance of a downflow fluidised bed reactor for biological treatment of yellow wastewater and nutrient recoveryBelem Espinosa-Chávez0Florina Ramírez-Vives1Grietje Zeeman2Oscar Monroy-Hermosillo3 Institute of Ecology, Universidad del Mar, Ciudad Universitaria, 70902 Puerto Ángel, Oaxaca, México Department of Biotechnology, Universidad Autónoma Metropolitana, Av. San Rafael Atlixco. 186. Col. Vicentina, 09340 Iztapalapa, México City, México Churchillweg 66, 6706 AD Wageningen, The Netherlands Department of Biotechnology, Universidad Autónoma Metropolitana, Av. San Rafael Atlixco. 186. Col. Vicentina, 09340 Iztapalapa, México City, México 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 °C in batch mode, and reaction time = 1 d. The average immobilised biomass (as volatile solids, IVS) in the reactor was 2.5±0.9 g L−1support, and specific ureolytic activity was 121 g Urea-N g−1 IVS d−1. The kinetic parameters were 0.152 mol L−1 (Km) and 8 mol g−1 IVS d−1 (Vmax). 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. HIGHLIGHTS A new biological treatment of yellow water is proposed.; Yellow waters were treated effectively in a downflow fluidised bed reactor.; The biological ureolysis of human urine was reached within six hours.; After addition of Mg2+/PO43− (1.6/1), 82.3 g of precipitates were recovered.; Struvite was the major component of the recovered precipitates.;http://wst.iwaponline.com/content/85/11/3208downflow fluidised bed reactorkinetic parametersstruviteureolysisyellow water
spellingShingle Belem Espinosa-Chávez
Florina Ramírez-Vives
Grietje Zeeman
Oscar Monroy-Hermosillo
Start-up and performance of a downflow fluidised bed reactor for biological treatment of yellow wastewater and nutrient recovery
Water Science and Technology
downflow fluidised bed reactor
kinetic parameters
struvite
ureolysis
yellow water
title Start-up and performance of a downflow fluidised bed reactor for biological treatment of yellow wastewater and nutrient recovery
title_full Start-up and performance of a downflow fluidised bed reactor for biological treatment of yellow wastewater and nutrient recovery
title_fullStr Start-up and performance of a downflow fluidised bed reactor for biological treatment of yellow wastewater and nutrient recovery
title_full_unstemmed Start-up and performance of a downflow fluidised bed reactor for biological treatment of yellow wastewater and nutrient recovery
title_short Start-up and performance of a downflow fluidised bed reactor for biological treatment of yellow wastewater and nutrient recovery
title_sort start up and performance of a downflow fluidised bed reactor for biological treatment of yellow wastewater and nutrient recovery
topic downflow fluidised bed reactor
kinetic parameters
struvite
ureolysis
yellow water
url http://wst.iwaponline.com/content/85/11/3208
work_keys_str_mv AT belemespinosachavez startupandperformanceofadownflowfluidisedbedreactorforbiologicaltreatmentofyellowwastewaterandnutrientrecovery
AT florinaramirezvives startupandperformanceofadownflowfluidisedbedreactorforbiologicaltreatmentofyellowwastewaterandnutrientrecovery
AT grietjezeeman startupandperformanceofadownflowfluidisedbedreactorforbiologicaltreatmentofyellowwastewaterandnutrientrecovery
AT oscarmonroyhermosillo startupandperformanceofadownflowfluidisedbedreactorforbiologicaltreatmentofyellowwastewaterandnutrientrecovery