Process Biotechnology
 

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
RESEARCH ARTICLE

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

Abstract   Full Text

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.

Supported by UNESCO / MIRCEN network