Ferrer, J.; Pretel, R.; Durán Pinzón, F.; Giménez, J.; Robles Martínez, Á.; Ruano García, MV.; Serralta Sevilla, J.... (2015). Design methodology for submerged anaerobic membrane bioreactors (AnMBR): A case study. Separation and Purification Technology. 141:378-386. https://doi.org/10.1016/j.seppur.2014.12.018
Por favor, use este identificador para citar o enlazar este ítem: http://hdl.handle.net/10251/68520
Title:
|
Design methodology for submerged anaerobic membrane bioreactors (AnMBR): A case study
|
Author:
|
Ferrer, J.
Pretel, R.
Durán Pinzón, Freddy
Giménez, JB
Robles Martínez, Ángel
Ruano García, María Victoria
Serralta Sevilla, Joaquín
Ribes Bertomeu, Jose
Seco Torrecillas, Aurora
|
UPV Unit:
|
Universitat Politècnica de València. Departamento de Ingeniería Hidráulica y Medio Ambiente - Departament d'Enginyeria Hidràulica i Medi Ambient
Universitat Politècnica de València. Instituto Universitario de Ingeniería del Agua y del Medio Ambiente - Institut Universitari d'Enginyeria de l'Aigua i Medi Ambient
|
Issued date:
|
|
Abstract:
|
[EN] The main objective of this study is to propose guidelines for designing submerged anaerobic MBR (AnMBR) technology for municipal wastewater treatment. The design methodology was devised on the basis of simulation and ...[+]
[EN] The main objective of this study is to propose guidelines for designing submerged anaerobic MBR (AnMBR) technology for municipal wastewater treatment. The design methodology was devised on the basis of simulation and experimental results from an AnMBR plant featuring industrial-scale hollow-fibre
membranes. The proposed methodology aims to minimise both capital expenditure and operating expenses, and the key parameters considered were: hydraulic retention time, solids retention time, mixed liquor suspended solids concentration in the membrane tank, 20 C-standardised critical flux, specificgas demand per square metre of membrane area, and flow of sludge being recycled from the membrane tank to the anaerobic reactor. An AnMBR WWTP operating at 15 and 30 C with both sulphate-rich (5.7 mg COD mg 1 SO4-S) and low-sulphate (57 mg COD mg 1 SO4-S) municipal wastewater was designed. The minimum cost of the designed plant was 0.097 and 0.070 per m3 when treating sulphate- rich and low-sulphate wastewater, respectively.
[-]
|
Subjects:
|
CAPEX/OPEX
,
Design methodology
,
Industrial-scale hollow-fibre membranes
,
Submerged anaerobic MBR (AnMBR)
,
Municipal wastewater treatment
|
Copyrigths:
|
Reserva de todos los derechos
|
Source:
|
Separation and Purification Technology. (issn:
1383-5866
)
|
DOI:
|
10.1016/j.seppur.2014.12.018
|
Publisher:
|
Elsevier
|
Publisher version:
|
http://dx.doi.org/10.1016/j.seppur.2014.12.018
|
Project ID:
|
info:eu-repo/grantAgreement/MICINN//CTM2011-28595-C02-02/ES/ESTUDIO EXPERIMENTAL DE LA RECUPERACION COMO BIOGAS DE LA ENERGIA DE LA MATERIA ORGANICA Y NUTRIENTES DEL AGUA RESIDUAL, ACOPLANDO UN ANBRM Y UN CULTIVO DE MICROALGAS/
info:eu-repo/grantAgreement/MICINN//CTM2011-28595-C02-01/ES/MODELACION Y CONTROL DE LA RECUPERACION COMO BIOGAS DE LA ENERGIA DE LA MATERIA ORGANICA Y NUTRIENTES DEL AGUA RESIDUAL, ACOPLANDO UN ANBRM Y UN CULTIVO DE MICROALGAS/
info:eu-repo/grantAgreement/GVA//ACOMP%2F2013%2F203/
info:eu-repo/grantAgreement/MICINN//IPT-20111023/ES/INVESTIGACION INTEGRADA SOBRE ISLAS SOSTENIBLES. IISIS/
|
Thanks:
|
This research work was possible thanks to projects CTM2011-28595-C02-01/02 (funded by the Spanish Ministry of Economy and Competitiveness jointly with the European Regional Development Fund and Generalitat Valenciana ...[+]
This research work was possible thanks to projects CTM2011-28595-C02-01/02 (funded by the Spanish Ministry of Economy and Competitiveness jointly with the European Regional Development Fund and Generalitat Valenciana GVA-ACOMP2013/203) and FCC Aqualia INNPRONTA IISIS IPT-20111023 (partially funded by the CDTI (Centre for Industrial Technological Development) and supported by the Spanish Ministry of Economy and Competitiveness).
[-]
|
Type:
|
Artículo
|