Joana Beigbeder

Dr. Joana Beigbeder


Research Focus & Metrics

Academic Career Length

14Years (2013-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 September 2013 in Resources, Conservation and Recycling
Verified
Journal Article
Closed access
JBJoana Beigbeder
Joana Beigbeder
DPDidier Perrin
Didier Perrin
JMJean-François Mascaro
Jean-François Mascaro
JLJosé-Marie Lopez-Cuesta
José-Marie Lopez-Cuesta

1 January 2019 in Waste Management
Verified
Journal Article
Closed access
JBJoana Beigbeder
Joana Beigbeder
LSLata Soccalingame
Lata Soccalingame
Didier PERRINDidier PERRIN
Didier PERRIN
JBJean-Charles Bénézet
Jean-Charles Bénézet
ABAnne Bergeret
Anne Bergeret

1 February 2018 in Polymer Degradation and Stability
Verified
Journal Article
Closed access
CBCélia Badji
Célia Badji
JBJoana Beigbeder
Joana Beigbeder
HGHélène Garay
Hélène Garay
ABAnne BERGERET
Anne BERGERET
JBJean-Charles Bénézet
Jean-Charles Bénézet
VDValérie Desauziers
Valérie Desauziers

1 June 2017 in Integrated Environmental Assessment and Management
Verified
Journal Article
Open access
PDF file
ECErwan Carré
Erwan Carré
JBJoana Beigbeder
Joana Beigbeder
VJVincent Jauzein
Vincent Jauzein
GJGuillaume Junqua
Guillaume Junqua
Miguel Lopez-FerberMiguel Lopez-Ferber
Miguel Lopez-Ferber
Tertiary treatment process (including filtration and/or disinfection) is necessary to obtain a water quality suited for high‐quality reuse from wastewater treatment. Industrial pilots representing small real‐size treatment units were set up downstream of a conventional secondary treatment of a wastewater treatment plant in the South of France and their performance followed for 2 y. Life cycle assessment (LCA) methodology is used to compare the environmental impacts of different treatment processes. Five tertiary treatment trains were studied: 1) sand filtration (SF) + storage followed by ultraviolet (UV) dynamic reactor disinfection (SF‐UVD), 2) sand filtration + UV batch reactor disinfection (SF‐UVB), 3) ultrafiltration (UF), 4) ultrafiltration and UV batch reactor disinfection (UF‐UVB), and 5) microfiltration (MF) and storage followed by dynamic UV disinfection (MF‐UVD). The chosen functional unit is “To supply 1 m3 of water with a quality in compliance with the highest standard of the French reuse regulations.” The combination of SF with UV disinfection or the use of UF alone was found to be equivalent in terms of environmental impact for most of the midpoint indicators chosen. Combination of UF with UV disinfection was significantly more impacting because the electricity consumption was nearly doubled. This study was conducted on an industrial pilot; it may thus be representative of industrial facilities implemented to treat higher water flows. Integr Environ Assess Manag 2017;13:1113–1121. © 2017 SETAC

1 February 2018 in Polymer Degradation and Stability
Verified
Journal Article
Closed access
CBCélia Badji
Célia Badji
JBJoana Beigbeder
Joana Beigbeder
HGHélène Garay
Hélène Garay
ABAnne BERGERET
Anne BERGERET
JBJean-Charles Bénézet
Jean-Charles Bénézet
VDValérie Desauziers
Valérie Desauziers

1 October 2018 in Composites Science and Technology
Verified
Journal Article
Closed access
CBCélia Badji
Célia Badji
JBJoana Beigbeder
Joana Beigbeder
HGHélène Garay
Hélène Garay
ABAnne BERGERET
Anne BERGERET
JBJean-Charles Bénézet
Jean-Charles Bénézet
VDValérie Desauziers
Valérie Desauziers