Daniele Vital Vital Vich

Prof. Daniele Vital Vital Vich


Research Focus & Metrics

Academic Career Length

23Years (2004-Present)

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

Representative Publications

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26 May 2012 in BioEnergy Research
Verified
Journal Article
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INIracema Andrade Nascimento
Iracema Andrade Nascimento
SMSheyla Santa Izabel Marques
Sheyla Santa Izabel Marques
ICIago Teles Dominguez Cabanelas
Iago Teles Dominguez Cabanelas
SPSolange Andrade Pereira
Solange Andrade Pereira
JDJanice Isabel Druzian
Janice Isabel Druzian
MNMaurício Andrade Nascimento
Maurício Andrade Nascimento

1 July 2010 in Bioresource Technology
Verified
Journal Article
Closed access
LOLorena Lima de Oliveira
Lorena Lima de Oliveira
RCRachel Biancalana Costa
Rachel Biancalana Costa
DODagoberto Yukio Okada
Dagoberto Yukio Okada
DVDaniele Vital Vital Vich
Daniele Vital Vital Vich
IDIolanda Cristina Silveira Duarte
Iolanda Cristina Silveira Duarte
MVMaria Bernadete Amâncio Varesche
Maria Bernadete Amâncio Varesche

1 August 2012 in International Journal of Hydrogen Energy
Verified
Journal Article
Closed access
CLCarolina Zampol Lazaro
Carolina Zampol Lazaro
DVDaniele Vital Vital Vich
Daniele Vital Vital Vich
JHJulia Sumiko Hirasawa
Julia Sumiko Hirasawa
MVMaria Bernadete Amâncio Varesche
Maria Bernadete Amâncio Varesche

6 November 2021 in Journal of Chemical Technology & Biotechnology
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Journal Article
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ASAmanda L. M. dos Santos
Amanda L. M. dos Santos
ACAna Luiza S. Castro
Ana Luiza S. Castro
KSKarina R. Salonon
Karina R. Salonon
TSTheo S. O. de Souza
Theo S. O. de Souza
DVDaniele Vital Vital Vich
Daniele Vital Vital Vich

24 April 2019 in International Journal of Phytoremediation
Verified
Journal Article
Closed access
VCVitor Cano
Vitor Cano
DVDaniele Vital Vital Vich
Daniele Vital Vital Vich
DRDiederik P. L. Rousseau
Diederik P. L. Rousseau
PLPiet Nicolaas Luc Lens
Piet Nicolaas Luc Lens
MNMarcelo Nolasco
Marcelo Nolasco
Treatment of landfill leachate is a challenge due to its complex chemical composition and high recalcitrance and because of high costs for conventional wastewater treatment. In our study, leachate from the Quitaúna Landfill, Sao Paulo Metropolitan Region, Brazil, was treated at a laboratory scale with a horizontal subsurface flow constructed treatment wetland (HF-CTW) operating under a recirculation regime. Two units planted with Heliconia psittacorum (HP) and Cyperus papyrus (CP), and one unplanted control unit were assessed. With a recirculation regime over 21 days, the planted units removed 40% of chemical oxygen demand (COD) while the control unit removed only 29%. True color removal efficiencies were 2, 22, and 23% for the control, HP, and CP HF-CTWs, respectively. The ammonium nitrogen removal efficiencies for a 21-day hydraulic retention time (HRT) were 63–81% for planted units and 72% for the control. The increase of the HRT from 7 to 21 days led to the enhancement of ammonium nitrogen removal but did not affect the COD and total nitrogen removals. This phenomenon is a consequence of leachate’s low biodegradability. The present study shows the importance of the HRT and plant presence for landfill leachate treatment using HF-CTWs.

18 December 2015 in Journal of Water and Health
Verified
Journal Article
Open access
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RRRenata Piacentini Rodriguez
Renata Piacentini Rodriguez
DVDaniele Vital Vital Vich
Daniele Vital Vital Vich
MGM. L. Garcia
M. L. Garcia
MVMaria Bernadete Amâncio Varesche
Maria Bernadete Amâncio Varesche
Marcelo ZaiatMarcelo Zaiat
Marcelo Zaiat
The production of low-pH effluent with sulfate and metals is one of the biggest environmental concerns in the mining industry. The biological process for sulfate reduction has the potential to become a low-cost solution that enables the recovery of interesting compounds. The present study analyzed such a process in a horizontal-flow anaerobic immobilized biomass (HAIB) reactor, employing ethanol as the carbon and energy source. Results showed that a maximal efficiency in the removal of sulfate and ethanol could only be obtained by reducing the applied sulfate load (225.1 ± 38 g m−3 d−1). This strategy led to over 75% of chemical oxygen demand (COD) and sulfate removal. Among the COD/SO42− studied ratios, 0.67 showed the most promising performance. The effluent's pH has naturally remained between 6.8 and 7.0 and the complete oxidation of the organic matter has been observed. Corrections of the influent pH or effluent recirculation did not show any significant effect on the COD and sulfate removal efficiency. Species closely related to strains of Clostridium sp. and species of Acidaminobacter hydrogenomorfans and Fusibacter paucivorans that can be related to the process of sulfate reduction were found in the HAIB reactors when the initial pH was 5 and the COD/SO42− ratio increased to 1.0.