TY - JOUR
T1 - Phosphate removal by Ca(OH)2-treated natural minerals
T2 - experimental and modeling studies
AU - Mitrogiannis, Dimitris
AU - Psychoyou, Maria
AU - Baziotis, Ioannis
AU - Mavrogonatos, Constantinos
AU - Koukouzas, Nikolaos
AU - Anastopoulos, Ioannis
AU - Fyrillas, Marios
AU - Inglezakis, Vassilis J.
PY - 2023/3/5
Y1 - 2023/3/5
N2 - Adsorption of phosphate phosphorus (PO
4-P) from wastewater onto eco-friendly geosorbents has gained great attention aiming at recovering an essential nutrient for crop production. Notably, the literature on PO
4-P aqueous-phase adsorption kinetics is limited to the application of either empirical reaction-based models lacking a physical significance or over-simplified diffusion-based models frequently used outside their applicability area. In this study, equilibrium and kinetic experiments are presented under a wide range of phosphate concentrations (50–500 mg P/L) using sustainable and low-cost modified adsorbents. The kinetics of PO
4-P adsorption from aqueous solutions onto Ca(OH)
2-treated zeolite (CaT-Z) and bentonite (CaT-B) was analyzed by a dimensionless two-phase homogeneous surface diffusion model (TP-HSDM) assuming constant diffusivity coupled with the double selectivity isotherm equation (DSM). The TP-HSDM fit to the data at four initial P concentrations (50, 100, 200 and 300 mg/L) resulted in an average relative error of 14.6% and 17.4% from the experimental data for CaT-Z and CaT-B, respectively. The average surface diffusion coefficient (D
s) ranged from 2.5 × 10
-10 to 8.7 × 10
-10 cm
2/s for CaT-Z and from 1.6 × 10
-10 to 4.78 × 10
-9 cm
2/s for CaT-B. The external mass transfer coefficient (k
f) ranged from 2.72 × 10
-4 to 8.38 × 10
-4 cm/s for CaT-Z and from 5.63 × 10
-4 to 2.24 × 10
-3 cm/s for CaT-B. The dimensionless Biot (Bi) number exhibited values in the order of magnitude of 10
5 indicating that the intraparticle diffusion is the controlling mass transfer mechanism for both materials.
AB - Adsorption of phosphate phosphorus (PO
4-P) from wastewater onto eco-friendly geosorbents has gained great attention aiming at recovering an essential nutrient for crop production. Notably, the literature on PO
4-P aqueous-phase adsorption kinetics is limited to the application of either empirical reaction-based models lacking a physical significance or over-simplified diffusion-based models frequently used outside their applicability area. In this study, equilibrium and kinetic experiments are presented under a wide range of phosphate concentrations (50–500 mg P/L) using sustainable and low-cost modified adsorbents. The kinetics of PO
4-P adsorption from aqueous solutions onto Ca(OH)
2-treated zeolite (CaT-Z) and bentonite (CaT-B) was analyzed by a dimensionless two-phase homogeneous surface diffusion model (TP-HSDM) assuming constant diffusivity coupled with the double selectivity isotherm equation (DSM). The TP-HSDM fit to the data at four initial P concentrations (50, 100, 200 and 300 mg/L) resulted in an average relative error of 14.6% and 17.4% from the experimental data for CaT-Z and CaT-B, respectively. The average surface diffusion coefficient (D
s) ranged from 2.5 × 10
-10 to 8.7 × 10
-10 cm
2/s for CaT-Z and from 1.6 × 10
-10 to 4.78 × 10
-9 cm
2/s for CaT-B. The external mass transfer coefficient (k
f) ranged from 2.72 × 10
-4 to 8.38 × 10
-4 cm/s for CaT-Z and from 5.63 × 10
-4 to 2.24 × 10
-3 cm/s for CaT-B. The dimensionless Biot (Bi) number exhibited values in the order of magnitude of 10
5 indicating that the intraparticle diffusion is the controlling mass transfer mechanism for both materials.
KW - phosphate
KW - bentonite
KW - zeolite
KW - surface diffusion
KW - mass transfer
KW - modeling
U2 - 10.1016/j.colsurfa.2022.130805
DO - 10.1016/j.colsurfa.2022.130805
M3 - Article
SN - 0927-7757
VL - 660
JO - Colloids and Surfaces A: Physicochemical and Engineering Aspects
JF - Colloids and Surfaces A: Physicochemical and Engineering Aspects
M1 - 130805
ER -