Biomethane production from vinasse in upflow anaerobic sludge blanket reactors inoculated with granular sludge

ABSTRACT The main objective of this study was to evaluate the anaerobic conversion of vinasse into biomethane with gradual increase in organic loading rate (OLR) in two upflow anaerobic sludge blanket (UASB) reactors, R1 and R2, with volumes of 40.5 and 21.5 L in the mesophilic temperature range. The UASB reactors were operated for 230 days with a hydraulic detection time (HDT) of 2.8 d (R1) and 2.8-1.8 d (R2). The OLR values applied in the reactors were 0.2-7.5 g totalCOD (L d)−1 in R1 and 0.2-11.5 g totalCOD (L d)−1 in R2. The average total chemical oxygen demand (totalCOD) removal efficiencies ranged from 49% to 82% and the average conversion efficiencies of the removed totalCOD into methane were 48-58% in R1 and 39-65% in R2. The effluent recirculation was used for an OLR above 6 g totalCOD (L d)−1 in R1 and 8 gtotalCOD (L d)−1 in R2 and was able to maintain the pH of the influent in R1 and R2 in the range from 6.5 to 6.8. However, this caused a decrease for 53-39% in the conversion efficiency of the removed totalCOD into methane in R2 because of the increase in the recalcitrant COD in the influent. The largest methane yield values were 0.181 and 0.185 (L) CH4 (gtotal COD removed)−1 in R1 and R2, respectively. These values were attained after 140 days of operation with an OLR of 5.0-7.5 g totalCOD (L d)−1 and total COD removal efficiencies around 70 and 80%.

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Main Authors: Barros,Valciney Gomes de, Duda,Rose Maria, Oliveira,Roberto Alves de
Format: Digital revista
Language:English
Published: Sociedade Brasileira de Microbiologia 2016
Online Access:http://old.scielo.br/scielo.php?script=sci_arttext&pid=S1517-83822016000300628
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spelling oai:scielo:S1517-838220160003006282016-08-02Biomethane production from vinasse in upflow anaerobic sludge blanket reactors inoculated with granular sludgeBarros,Valciney Gomes deDuda,Rose MariaOliveira,Roberto Alves de Biogas Mesophilic anaerobic treatment Methane Organic loading rate Startup ABSTRACT The main objective of this study was to evaluate the anaerobic conversion of vinasse into biomethane with gradual increase in organic loading rate (OLR) in two upflow anaerobic sludge blanket (UASB) reactors, R1 and R2, with volumes of 40.5 and 21.5 L in the mesophilic temperature range. The UASB reactors were operated for 230 days with a hydraulic detection time (HDT) of 2.8 d (R1) and 2.8-1.8 d (R2). The OLR values applied in the reactors were 0.2-7.5 g totalCOD (L d)−1 in R1 and 0.2-11.5 g totalCOD (L d)−1 in R2. The average total chemical oxygen demand (totalCOD) removal efficiencies ranged from 49% to 82% and the average conversion efficiencies of the removed totalCOD into methane were 48-58% in R1 and 39-65% in R2. The effluent recirculation was used for an OLR above 6 g totalCOD (L d)−1 in R1 and 8 gtotalCOD (L d)−1 in R2 and was able to maintain the pH of the influent in R1 and R2 in the range from 6.5 to 6.8. However, this caused a decrease for 53-39% in the conversion efficiency of the removed totalCOD into methane in R2 because of the increase in the recalcitrant COD in the influent. The largest methane yield values were 0.181 and 0.185 (L) CH4 (gtotal COD removed)−1 in R1 and R2, respectively. These values were attained after 140 days of operation with an OLR of 5.0-7.5 g totalCOD (L d)−1 and total COD removal efficiencies around 70 and 80%.info:eu-repo/semantics/openAccessSociedade Brasileira de MicrobiologiaBrazilian Journal of Microbiology v.47 n.3 20162016-09-01info:eu-repo/semantics/articletext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S1517-83822016000300628en10.1016/j.bjm.2016.04.021
institution SCIELO
collection OJS
country Brasil
countrycode BR
component Revista
access En linea
databasecode rev-scielo-br
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region America del Sur
libraryname SciELO
language English
format Digital
author Barros,Valciney Gomes de
Duda,Rose Maria
Oliveira,Roberto Alves de
spellingShingle Barros,Valciney Gomes de
Duda,Rose Maria
Oliveira,Roberto Alves de
Biomethane production from vinasse in upflow anaerobic sludge blanket reactors inoculated with granular sludge
author_facet Barros,Valciney Gomes de
Duda,Rose Maria
Oliveira,Roberto Alves de
author_sort Barros,Valciney Gomes de
title Biomethane production from vinasse in upflow anaerobic sludge blanket reactors inoculated with granular sludge
title_short Biomethane production from vinasse in upflow anaerobic sludge blanket reactors inoculated with granular sludge
title_full Biomethane production from vinasse in upflow anaerobic sludge blanket reactors inoculated with granular sludge
title_fullStr Biomethane production from vinasse in upflow anaerobic sludge blanket reactors inoculated with granular sludge
title_full_unstemmed Biomethane production from vinasse in upflow anaerobic sludge blanket reactors inoculated with granular sludge
title_sort biomethane production from vinasse in upflow anaerobic sludge blanket reactors inoculated with granular sludge
description ABSTRACT The main objective of this study was to evaluate the anaerobic conversion of vinasse into biomethane with gradual increase in organic loading rate (OLR) in two upflow anaerobic sludge blanket (UASB) reactors, R1 and R2, with volumes of 40.5 and 21.5 L in the mesophilic temperature range. The UASB reactors were operated for 230 days with a hydraulic detection time (HDT) of 2.8 d (R1) and 2.8-1.8 d (R2). The OLR values applied in the reactors were 0.2-7.5 g totalCOD (L d)−1 in R1 and 0.2-11.5 g totalCOD (L d)−1 in R2. The average total chemical oxygen demand (totalCOD) removal efficiencies ranged from 49% to 82% and the average conversion efficiencies of the removed totalCOD into methane were 48-58% in R1 and 39-65% in R2. The effluent recirculation was used for an OLR above 6 g totalCOD (L d)−1 in R1 and 8 gtotalCOD (L d)−1 in R2 and was able to maintain the pH of the influent in R1 and R2 in the range from 6.5 to 6.8. However, this caused a decrease for 53-39% in the conversion efficiency of the removed totalCOD into methane in R2 because of the increase in the recalcitrant COD in the influent. The largest methane yield values were 0.181 and 0.185 (L) CH4 (gtotal COD removed)−1 in R1 and R2, respectively. These values were attained after 140 days of operation with an OLR of 5.0-7.5 g totalCOD (L d)−1 and total COD removal efficiencies around 70 and 80%.
publisher Sociedade Brasileira de Microbiologia
publishDate 2016
url http://old.scielo.br/scielo.php?script=sci_arttext&pid=S1517-83822016000300628
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AT dudarosemaria biomethaneproductionfromvinasseinupflowanaerobicsludgeblanketreactorsinoculatedwithgranularsludge
AT oliveirarobertoalvesde biomethaneproductionfromvinasseinupflowanaerobicsludgeblanketreactorsinoculatedwithgranularsludge
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