Effect of impeller type and mechanical agitation on the mass transfer and power consumption aspects of ASBR operation treating synthetic wastewater


Autoria(s): MICHELAN, Rogerio; ZIMMER, Thiago R.; RODRIGUES, Jose A. D.; RATUSZNEI, Suzana M.; MORAES, Deovaldo de; ZAIAT, Marcelo; FORESTI, Eugenio
Contribuinte(s)

UNIVERSIDADE DE SÃO PAULO

Data(s)

18/10/2012

18/10/2012

2009

Resumo

The effect of flow type and rotor speed was investigated in a round-bottom reactor with 5 L useful volume containing 2.0 L of granular biomass. The reactor treated 2.0 L of synthetic wastewater with a concentration of 800 mgCOD/L in 8-h cycles at 30 degrees C. Five impellers, commonly used in biological processes, have been employed to this end, namely: a turbine and a paddle impeller with six-vertical-flat-blades, a turbine and a paddle impeller with six-45 degrees-inclined-flat-blades and a three-blade-helix impeller. Results showed that altering impeller type and rotor speed did not significantly affect system stability and performance. Average organic matter removal efficiency was about 84% for filtered samples, total volatile acids concentration was below 20 mgHAc/L and bicarbonate alkalinity a little less than 400 mgCaCO(3)/L for most of the investigated conditions. However, analysis of the first-order kinetic model constants showed that alteration in rotor speed resulted in an increase in the values of the kinetic constants (for instance, from 0.57 h(-1) at 50 rpm to 0.84 h(-1) at 75 rpm when the paddle impeller with six-45 degrees-inclined-flat-blades was used) and that axial flow in mechanically stirred reactors is preferable over radial-flow when the vertical-flat-blade impeller is compared to the inclined-flat-blade impeller (for instance at 75 rpm, from 0.52 h(-1) with the six-flat-blade-paddle impeller to 0.84 h(-1) with the six-45 degrees-inclined-flat-blade-paddle impeller), demonstrating that there is a rotor speed and an impeller type that maximize solid-liquid mass transfer in the reaction medium. Furthermore, power consumption studies in this reduced reactor volume showed that no high power transfer is required to improve mass transfer (less than 0.6 kW/10(3) m(3)). (C) 2008 Elsevier Ltd. All rights reserved.

Fundacao de Amparo a Pesquisa do Estado de Sao Paulo-FAPESP (Sao Paulo, Brasil)[01/05.489-0]

Fundacao de Amparo a Pesquisa do Estado de Sao Paulo-FAPESP (Sao Paulo, Brasil)[04/04.699-0]

Fundacao de Amparo a Pesquisa do Estado de Sao Paulo-FAPESP (Sao Paulo, Brasil)[04/03.216-5]

Identificador

JOURNAL OF ENVIRONMENTAL MANAGEMENT, v.90, n.3, p.1357-1364, 2009

0301-4797

http://producao.usp.br/handle/BDPI/17973

10.1016/j.jenvman.2008.08.003

http://dx.doi.org/10.1016/j.jenvman.2008.08.003

Idioma(s)

eng

Publicador

ACADEMIC PRESS LTD ELSEVIER SCIENCE LTD

Relação

Journal of Environmental Management

Direitos

restrictedAccess

Copyright ACADEMIC PRESS LTD ELSEVIER SCIENCE LTD

Palavras-Chave #ASBR #Impeller #Power consumption #Granulated biomass #Synthetic wastewater #SEQUENCING BATCH REACTOR #PERFORMANCE #RECIRCULATION #BIOMASS #ANSBBR #Environmental Sciences #Environmental Studies
Tipo

article

original article

publishedVersion