Simplified Mathematical Model for an Anaerobic Sequencing Batch Biofilm Reactor Treating Lipid-Rich Wastewater Subject to Rising Organic Loading Rates


Autoria(s): FUZZATO, Maira Ciaramello; ADORNO, Maria Angela Tallarico; PINHO, Samantha Cristina de; RIBEIRO, Rogers; TOMMASO, Giovana
Contribuinte(s)

UNIVERSIDADE DE SÃO PAULO

Data(s)

18/04/2012

18/04/2012

2009

Resumo

This study proposes a simplified mathematical model to describe the processes occurring in an anaerobic sequencing batch biofilm reactor (ASBBR) treating lipid-rich wastewater. The reactor, subjected to rising organic loading rates, contained biomass immobilized cubic polyurethane foam matrices, and was operated at 32 degrees C +/- 2 degrees C, using 24-h batch cycles. In the adaptation period, the reactor was fed with synthetic substrate for 46 days and was operated without agitation. Whereas agitation was raised to 500 rpm, the organic loading rate (OLR) rose from 0.3 g chemical oxygen demand (COD) . L(-1) . day(-1) to 1.2 g COD . L(-1) . day(-1). The ASBBR was fed fat-rich wastewater (dairy wastewater), in an operation period lasting for 116 days, during which four operational conditions (OCs) were tested: 1.1 +/- 0.2 g COD . L(-1) . day(-1) (OC1), 4.5 +/- 0.4 g COD . L(-1) . day(-1) (OC2), 8.0 +/- 0.8 g COD . L(-1) . day(-1) (OC3), and 12.1 +/- 2.4 g COD . L(-1) . day(-1) (OC4). The bicarbonate alkalinity (BA)/COD supplementation ratio was 1:1 at OC1, 1:2 at OC2, and 1:3 at OC3 and OC4. Total COD removal efficiencies were higher than 90%, with a constant production of bicarbonate alkalinity, in all OCs tested. After the process reached stability, temporal profiles of substrate consumption were obtained. Based on these experimental data a simplified first-order model was fit, making possible the inference of kinetic parameters. A simplified mathematical model correlating soluble COD with volatile fatty acids (VFA) was also proposed, and through it the consumption rates of intermediate products as propionic and acetic acid were inferred. Results showed that the microbial consortium worked properly and high efficiencies were obtained, even with high initial substrate concentrations, which led to the accumulation of intermediate metabolites and caused low specific consumption rates.

FAPESP-Fundacao de Amparo a Pesquisa do Estado de Sao Paulo[2005/04353-9]

FAPESP-Fundacao de Amparo a Pesquisa do Estado de Sao Paulo[2006/02323-8]

Identificador

ENVIRONMENTAL ENGINEERING SCIENCE, v.26, n.7, p.1197-1206, 2009

1092-8758

http://producao.usp.br/handle/BDPI/15568

10.1089/ees.2008.0175

http://dx.doi.org/10.1089/ees.2008.0175

Idioma(s)

eng

Publicador

MARY ANN LIEBERT INC

Relação

Environmental Engineering Science

Direitos

closedAccess

Copyright MARY ANN LIEBERT INC

Palavras-Chave #anaerobic process #sequencing batch reactor #ASBBR #lipid-rich wastewater #kinetic model #DAIRY WASTEWATERS #IMMOBILIZED BIOMASS #WHEY TREATMENT #DEGRADATION #DIGESTION #KINETICS #BIODEGRADABILITY #METHANOGENESIS #TOXICITY #2-PHASE #Engineering, Environmental #Environmental Sciences
Tipo

article

original article

publishedVersion