Process Biotechnology |
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Environmental Biotechnology |
Electronic Journal of Biotechnology ISSN: 0717-3458 |
Vol.
12 No. 3, Issue of July 15, 2009 |
© 2009 by Pontificia Universidad Católica
de Valparaíso -- Chile |
Received September 15, 2008
/ Accepted April 21, 2009 |
DOI: 10.2225/vol12-issue3-fulltext-15 |
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Treatment of low strength sewage with high suspended
organic matter content in an anaerobic sequencing batch reactor and modeling
application
Andrés Donoso-Bravo*
Escuela de Ingeniería Bioquímica
Pontificia Universidad Católica de Valparaíso
General Cruz 34, Valparaíso, Chile
Tel: 56322273819
Fax: 56322273803
E-mail: andres.donoso.b@mail.ucv.cl
Marta Carballa
Escuela de Ingeniería Bioquímica
Pontificia Universidad Católica de Valparaíso
General Cruz 34, Valparaíso, Chile
Valparaíso, Chile
Gonzalo Ruiz- Filippi
Escuela de Ingeniería Bioquímica
Pontificia Universidad Católica de Valparaíso
General Cruz 34, Valparaíso, Chile
Valparaíso, Chile
Rolando Chamy
Escuela de Ingeniería Bioquímica
Pontificia Universidad Católica de Valparaíso
General Cruz 34, Valparaíso, Chile
Valparaíso, Chile
*Corresponding author
Financial support: FONDECYT project (n°1080329).
Keywords: acidogenesis, anaerobic treatment, hydrolysis, low
strength wastewater, modeling.
Abbreviations: |
α: particulate organic matter fraction
ASBR: anaerobic sequencing
batch reactor
CSTR: continuous
stirred tank reactor
COD: chemical oxygen demand
IA: intermediate alkalinity
OLR: organic load rate
PA: partial alkalinity
pCOD: particulate COD
sCOD: soluble COD
TA: total alkalinity
tCOD: total COD
TSS: total suspended solids
UASB: up-flow anaerobic
sludge blanket
VFA: volatile fatty acid
VSS: volatile suspended solids |
In this work, an anaerobic sequencing batch reactor
(ASBR) was operated for 8 months to treat low strength sewage with high
suspended organic matter content. Three phases of operation with increasing organic
loading rates (OLR) were performed: 0.4 kg COD/m3 x d (phase I), 0 .8 kg COD/m3 x d (phase II) and 1.2 kg COD/m3 x d (phase III). Adequate stability parameters (pH, total alkalinity) were obtained
through all three experimental phases. During phases I and II, the removal efficiencies
of organic matter (expressed as total chemical oxygen demand (COD) and total
suspended solids ranged between 50-60%. However, these values decreased to
15-25% in phase III. In addition, a non-complex model, including hydrolysis,
acidogenesis and methanogenesis, was applied to predict the reactor behavior.
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