Diego Gómez-Díaz

Dr. Diego Gómez-Díaz

University of Santiago de Compostela, Santiago de Compostela, Galicia, Spain
orcid

Research Focus & Metrics

Academic Career Length

27Years (2000-Present)

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

Representative Publications

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1 March 2003 in Journal of Food Engineering
Verified
Journal Article
Closed access
DGDiego Gómez-Díaz
Diego Gómez-Díaz
JNJosé M. Navaza
José M. Navaza

1 February 2009 in Chemical Engineering Journal
Verified
Journal Article
Closed access
JNJosé M. Navaza
José M. Navaza
DGDiego Gómez-Díaz
Diego Gómez-Díaz
La Rubia M.DoloresLa Rubia M.Dolores
La Rubia M.Dolores

6 September 2013 in Industrial & Engineering Chemistry Research
Verified
Journal Article
Closed access
AGAlicia García-Abuín
Alicia García-Abuín
DGDiego Gómez-Díaz
Diego Gómez-Díaz
AGAna Belén García
Ana Belén García
JNJosé M. Navaza
José M. Navaza
ARAntonio Rumbo
Antonio Rumbo



31 March 2023 in Biomass Conversion and Biorefinery
Verified
Journal Article
Open access
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CPCatarina Helena Pimentel
Catarina Helena Pimentel
MFM. Sonia Freire
M. Sonia Freire
DGDiego Gómez-Díaz
Diego Gómez-Díaz
Julia González-ÁlvarezJulia González-Álvarez
Julia González-Álvarez
: Wastewater containing dyes are released into water bodies generating serious problems in human health and marine life. To contribute to the solution of this problem, a novel activated carbon was prepared from untreated pine (Pinus radiata) sawdust by dry chemical activation with ZnCl2 and was used for wood dye adsorption. The carbon was characterized by point of zero charge, N2 and CO2 adsorption isotherms, SEM-EDX, and FTIR. N2 and CO2 surface areas were 471.4 and 319.5 m2 g−1, respectively, with 91% of micropores. Wood dye adsorption was studied in function of pH (2–12), adsorbent dose (0.1–4 g L−1), time (up to 48 h for blue and red and 12 h for black), and initial concentration (5–500 mg L−1). The equilibrium data for the blue and black dyes were satisfactorily fitted to the Freundlich model while those for the red dye to the Langmuir model. Kinetic data were explained by the pseudo-second order (chemisorption process) and intraparticle diffusion models. At 5 mg L−1, a 100% removal efficiency was achieved at all pH for the blue dye, whereas for the red and black, natural pH (5.1) and pH = 2, respectively, led to the best removal efficiencies, 96 and 56%. Increasing concentration above 25 mg L−1 significantly reduced adsorption efficiency for blue and red dyes. For the black dye increasing the dose to 1 g L−1, the adsorption efficiency reached 82% at 25 mg L−1. High removal efficiencies were achieved for all dyes at 25 mg L−1 and 4 g L−1.