Influence of total solids concentration on membrane permeability in a submerged hollow-fibre anaerobic membrane bioreactor
Fecha
Autores
Robles Martínez, Ángel
Durán Pinzón, Freddy
Ruano García, María Victoria
Ribes Bertomeu, Jose
Ferrer Polo, José
Directores
Unidades organizativas
Handle
https://riunet.upv.es/handle/10251/33015
Cita bibliográfica
Robles Martínez, Á.; Durán Pinzón, F.; Ruano García, MV.; Ribes Bertomeu, J.; Ferrer Polo, J. (2012). Influence of total solids concentration on membrane permeability in a submerged hollow-fibre anaerobic membrane bioreactor. Water Science and Technology. 66(2):377-384. https://doi.org/10.2166/wst.2012.196
Titulación
Resumen
The main aim of this work was to study the influence of the mixed liquor total solids (MLTS) concentration on membrane permeability (K 20) in a submerged anaerobic membrane bioreactor (SAnMBR) pilot plant, which is equipped with industrial hollow-fibre membranes and treats urban wastewater. This pilot plant was operated at 33°C and 70 days of SRT. Two different transmembrane fluxes (13.3 and 10 LMH) were tested with a gas sparging intensity of 0.23 Nm 3 m -2 h -1 (measured as Specific Gas Demand referred to membrane area). A linear dependence of K 20 on MLTS concentration was observed within a range of MLTS concentration from 13 to 32 g L -1 and J 20 of 10 LMH. K 20 was maintained at sustainable values (about 100 LMH bar -1) even at high MLTS concentrations (up to 20 g L -1). In addition, several short-tests were carried out when the membranes were operated at high MLTS concentrations in order to assess the effect of the physical cleaning strategies (relaxation and back-flush) on membrane performance. It was observed that, with the applied gas sparging intensity, the duration of the relaxation stage did not critically affect the membrane performance. On the other hand, the required back-flush frequency was considerably affected by the MLTS concentration. © IWA Publishing 2012.
Palabras clave
Fouling rate, Industrial membranes, Mixed liquor total solids concentration, Permeability, Submerged anaerobic membrane bioreactor
ISSN
0273-1223
ISBN
Fuente
Water Science and Technology
DOI
10.2166/wst.2012.196
Enlaces relacionados
Código de Proyecto
info:eu-repo/grantAgreement/MICINN//CTM2008-06809-C02-02/ES/MODELACION DE LA APLICACION DE LA TECNOLOGIA DE MEMBRANAS PARA LA VALORIZACION ENERGETICA DE LA MATERIA ORGANICA DEL AGUA RESIDUAL Y LA MINIMIZACION DE LOS FANGOS PRODUCIDOS. DESARROLLO DE LOS ALGORIT/
info:eu-repo/grantAgreement/GVA//ACOMP%2F2011%2F182/
info:eu-repo/grantAgreement/GVA//ACOMP%2F2010%2F130/
info:eu-repo/grantAgreement/MICINN//CTM2008-06809-C02-01/ES/ESTUDIO EN PLANTA PILOTO DE LA APLICACION DE LA TECNOLOGIA DE MEMBRANAS PARA LA VALORIZACION ENERGETICA DE LA MATERIA ORGANICA DEL AGUA RESIDUAL Y LA MINIMIZACION DE LOS FANGOS PRODUCIDOS. EVALUACION/
info:eu-repo/grantAgreement/MICINN//BES-2009-023712/ES/BES-2009-023712/
info:eu-repo/grantAgreement/GVA//ACOMP%2F2011%2F182/
info:eu-repo/grantAgreement/GVA//ACOMP%2F2010%2F130/
info:eu-repo/grantAgreement/MICINN//CTM2008-06809-C02-01/ES/ESTUDIO EN PLANTA PILOTO DE LA APLICACION DE LA TECNOLOGIA DE MEMBRANAS PARA LA VALORIZACION ENERGETICA DE LA MATERIA ORGANICA DEL AGUA RESIDUAL Y LA MINIMIZACION DE LOS FANGOS PRODUCIDOS. EVALUACION/
info:eu-repo/grantAgreement/MICINN//BES-2009-023712/ES/BES-2009-023712/
Patrocinadores
Agradecimientos
This research work has been supported by the Spanish Research Foundation (CICYT Projects CTM2008-06809-C02-01 and CTM2008-06809-C02-02, and MICINN FPI grant BES-2009-023712) and Generalitat Valenciana (Projects GVA-ACOMP2010/130 and GVA-ACOMP2011/182), which are gratefully acknowledged.