• English 
    • español
    • English
    • français
  • FacebookPinterestTwitter
  • español
  • English
  • français
View Item 
  •   DIGIBUG Home
  • 1.-Investigación
  • Departamentos, Grupos de Investigación e Institutos
  • Departamento de Ingeniería Química
  • DIQ - Artículos
  • View Item
  •   DIGIBUG Home
  • 1.-Investigación
  • Departamentos, Grupos de Investigación e Institutos
  • Departamento de Ingeniería Química
  • DIQ - Artículos
  • View Item
JavaScript is disabled for your browser. Some features of this site may not work without it.

Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater

[PDF] OchandoPulidoJM_ModelingAndCostAnalysis.pdf (970.4Kb)
Identificadores
URI: http://hdl.handle.net/10481/45017
ISSN: 2077-0375
Exportar
untranslatedRefworksMendeley
Estadísticas
View Usage Statistics
Metadata
Show full item record
Author
Ochando-Pulido, Javier Miguel; Hodaifa, Gassan; Víctor-Ortega, María Dolores; Martínez-Férez, Antonio
Editorial
MDPI
Materia
Olive mill wastewater
 
advanced oxidation processes
 
Membrane processes
 
Reverse osmosis
 
Wastewater reclamation
 
Modelization
 
Date
2013
Referencia bibliográfica
Ochando-Pulido, J. M. [et al]. Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater. Membranes 2013, 3, 285-297. [http://hdl.handle.net/10481/45017]
Abstract
A secondary treatment for olive mill wastewater coming from factories working with the two-phase olive oil production process (OMW-2) has been set-up on an industrial scale in an olive oil mill in the premises of Jaén (Spain). The secondary treatment comprises Fenton-like oxidation followed by flocculation-sedimentation and filtration through olive stones. In this work, performance modelization and preliminary cost analysis of a final reverse osmosis (RO) process was examined on pilot scale for ulterior purification of OMW-2 with the goal of closing the loop of the industrial production process. Reduction of concentration polarization on the RO membrane equal to 26.3% was provided upon increment of the turbulence over the membrane to values of Reynolds number equal to 2.6 × 104. Medium operating pressure (25 bar) should be chosen to achieve significant steady state permeate flux (21.1 L h−1 m−2) and minimize membrane fouling, ensuring less than 14.7% flux drop and up to 90% feed recovery. Under these conditions, irreversible fouling below 0.08 L h−2 m−2 bar−1 helped increase the longevity of the membrane and reduce the costs of the treatment. For 10 m3 day−1 OMW-2 on average, 47.4 m2 required membrane area and 0.87 € m−3 total costs for the RO process were estimated.
Collections
  • DIQ - Artículos

My Account

LoginRegister

Browse

All of DIGIBUGCommunities and CollectionsBy Issue DateAuthorsTitlesSubjectFinanciaciónThis CollectionBy Issue DateAuthorsTitlesSubjectFinanciación

Statistics

View Usage Statistics

Servicios

Pasos para autoarchivoAyudaLicencias Creative CommonsSHERPA/RoMEODulcinea Biblioteca UniversitariaNos puedes encontrar a través de

Contact Us | Send Feedback