Biosorption of diazinon by a pre-treated alimentary industrial waste: equilibrium and kinetic modeling

Abstract This study explores the feasibility of pre-treated coffee waste (PCW) as biosorbent for the removal of diazinon. The effect of the pesticide concentration (6–20 mg L−1), contact time, adsorbent dose (0.2–1.2 g L−1), solution pH (3–11.5), temperature (15–40 °C) and co-existing inorganic ions...

תיאור מלא

מידע ביבליוגרפי
Main Authors: N. Yeddou Mezenner, H. Lagha, H. Kais, M. Trari
פורמט: Article
שפה:English
יצא לאור: SpringerOpen 2017-04-01
סדרה:Applied Water Science
נושאים:
גישה מקוונת:http://link.springer.com/article/10.1007/s13201-017-0563-z
_version_ 1828431516611379200
author N. Yeddou Mezenner
H. Lagha
H. Kais
M. Trari
author_facet N. Yeddou Mezenner
H. Lagha
H. Kais
M. Trari
author_sort N. Yeddou Mezenner
collection DOAJ
description Abstract This study explores the feasibility of pre-treated coffee waste (PCW) as biosorbent for the removal of diazinon. The effect of the pesticide concentration (6–20 mg L−1), contact time, adsorbent dose (0.2–1.2 g L−1), solution pH (3–11.5), temperature (15–40 °C) and co-existing inorganic ions (H2PO4 −, NO3 −) on the diazinon biosorption over PCW is investigated. The experimental results indicate an optimal pH of 7.3 for the diazinon elimination on PCW (1 g L−1). The Langmuir model describes well the isotherm data with a high regression coefficient (R 2 > 0.990) and a maximum monolayer biosorption capacity of 18.52 mg g−1 at 15 °C. It is also observed that the intra-particle diffusion is not the rate-controlling step. A comparison is evaluated between the pseudo-second-order and intra-particle diffusion kinetic models; the experimental data are well fitted by the pseudo-second-order kinetic model. The biosorption capacity decreases with increasing temperature for a diazinon concentration of 10 mg L−1. The negative enthalpy ΔH° (−63.57 kJ/mol) indicates that the diazinon biosorption onto PCW is exothermic. Under optimal conditions, the biosorption reaches 95% after 90 min. The removal efficiency decreases from 95 to 65.67 and 48.9% for the diazinon alone and in the presence of NO3 − and H2PO4 − (100 mg L−1), respectively.
first_indexed 2024-12-10T18:04:25Z
format Article
id doaj.art-cbd554f8b8b1479c9511afb1c595d521
institution Directory Open Access Journal
issn 2190-5487
2190-5495
language English
last_indexed 2024-12-10T18:04:25Z
publishDate 2017-04-01
publisher SpringerOpen
record_format Article
series Applied Water Science
spelling doaj.art-cbd554f8b8b1479c9511afb1c595d5212022-12-22T01:38:39ZengSpringerOpenApplied Water Science2190-54872190-54952017-04-01774067407610.1007/s13201-017-0563-zBiosorption of diazinon by a pre-treated alimentary industrial waste: equilibrium and kinetic modelingN. Yeddou Mezenner0H. Lagha1H. Kais2M. Trari3Laboratory of Chemical Engineering, Faculty of Mechanical and Chemical Engineering, USTHBLaboratory of Chemical Engineering, Faculty of Mechanical and Chemical Engineering, USTHBLaboratory of Storage and Valorization of Renewable Energies, Faculty of Chemistry, USTHBLaboratory of Storage and Valorization of Renewable Energies, Faculty of Chemistry, USTHBAbstract This study explores the feasibility of pre-treated coffee waste (PCW) as biosorbent for the removal of diazinon. The effect of the pesticide concentration (6–20 mg L−1), contact time, adsorbent dose (0.2–1.2 g L−1), solution pH (3–11.5), temperature (15–40 °C) and co-existing inorganic ions (H2PO4 −, NO3 −) on the diazinon biosorption over PCW is investigated. The experimental results indicate an optimal pH of 7.3 for the diazinon elimination on PCW (1 g L−1). The Langmuir model describes well the isotherm data with a high regression coefficient (R 2 > 0.990) and a maximum monolayer biosorption capacity of 18.52 mg g−1 at 15 °C. It is also observed that the intra-particle diffusion is not the rate-controlling step. A comparison is evaluated between the pseudo-second-order and intra-particle diffusion kinetic models; the experimental data are well fitted by the pseudo-second-order kinetic model. The biosorption capacity decreases with increasing temperature for a diazinon concentration of 10 mg L−1. The negative enthalpy ΔH° (−63.57 kJ/mol) indicates that the diazinon biosorption onto PCW is exothermic. Under optimal conditions, the biosorption reaches 95% after 90 min. The removal efficiency decreases from 95 to 65.67 and 48.9% for the diazinon alone and in the presence of NO3 − and H2PO4 − (100 mg L−1), respectively.http://link.springer.com/article/10.1007/s13201-017-0563-zBiosorptionDiazinonPesticidePre-treated coffee waste
spellingShingle N. Yeddou Mezenner
H. Lagha
H. Kais
M. Trari
Biosorption of diazinon by a pre-treated alimentary industrial waste: equilibrium and kinetic modeling
Applied Water Science
Biosorption
Diazinon
Pesticide
Pre-treated coffee waste
title Biosorption of diazinon by a pre-treated alimentary industrial waste: equilibrium and kinetic modeling
title_full Biosorption of diazinon by a pre-treated alimentary industrial waste: equilibrium and kinetic modeling
title_fullStr Biosorption of diazinon by a pre-treated alimentary industrial waste: equilibrium and kinetic modeling
title_full_unstemmed Biosorption of diazinon by a pre-treated alimentary industrial waste: equilibrium and kinetic modeling
title_short Biosorption of diazinon by a pre-treated alimentary industrial waste: equilibrium and kinetic modeling
title_sort biosorption of diazinon by a pre treated alimentary industrial waste equilibrium and kinetic modeling
topic Biosorption
Diazinon
Pesticide
Pre-treated coffee waste
url http://link.springer.com/article/10.1007/s13201-017-0563-z
work_keys_str_mv AT nyeddoumezenner biosorptionofdiazinonbyapretreatedalimentaryindustrialwasteequilibriumandkineticmodeling
AT hlagha biosorptionofdiazinonbyapretreatedalimentaryindustrialwasteequilibriumandkineticmodeling
AT hkais biosorptionofdiazinonbyapretreatedalimentaryindustrialwasteequilibriumandkineticmodeling
AT mtrari biosorptionofdiazinonbyapretreatedalimentaryindustrialwasteequilibriumandkineticmodeling