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Synthesis and characterization of eco-friendly cellulose beads for copper (II) removal from aqueous solutions

  • Pollutant Removal and the Health Effects of Environmental Pollution
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Abstract

In this study, novel cellulose-bead-based biosorbents (CBBAS) were successfully synthesized from almond shell using a simple three-step process: (i) dissolution of bleached almond shell in ionic liquid (1-butyl-3-methylimidazolium chloride), (ii) coagulation of cellulose-ionic liquid solution in water and (iii) freeze-drying. Their morphological, structural and physicochemical properties were thoroughly characterized. These biomaterials exhibited a 3D-macroporous structure with interconnected pores, which provided a high number of adsorption sites. It should be noted that CBBAS biosorbents were efficiently employed for the removal of copper (II) ions from aqueous solutions, showing high adsorption capacity: 128.24 mg g−1. The biosorption equilibrium data obtained were successfully fitted to the Sips model and the kinetics were suitably described by the pseudo-second-order model. Besides, CBBAS biosorbents can be easily separated from the solution for their subsequent reuse, and thus, they represent a method for the removal of copper (II) from aqueous solutions that is not only eco-friendly but also economical.

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Abbreviations

aT :

Toth isotherm constant (mg L−1)

BET:

Brunauer–Emmett Teller

BJH:

Barrett–Joyner–Halenda

BTC:

Breakthrough curve

C :

Boundary layer thickness constant, (mg g−1)

C 0 :

Initial concentration, (mg L−1)

CBBAS:

Cellulose beads from bleached almond shell

Ce :

Equilibrium concentration, (mg L−1)

C t :

Heavy metal concentration at time t, (mg L−1)

DTG:

Derivative thermogravimetric analysis

E :

Mean free energy of adsorption for each molecule of the adsorbate, (kJ mol−1)

FTIR:

Fourier-transform infrared spectroscopy

I (020) :

Peak intensity of the crystalline part, dimensionless

I am :

Counter reading at a peak intensity of the amorphous material, dimensionless

ICP-MS:

Inductively coupled plasma mass spectrometer

k 1 :

Rate constant of the pseudo-first kinetic model, (min−1)

k 2 :

Rate constant of the pseudo-second kinetic model, (g mg−1 min−1)

K D-R :

Dubinin–Radushkevich constant related to the sorption energy, (mol2 kJ−2)

K F :

Freundlich constant, (mg g−1) (L mg−1)1/nF

K L :

Langmuir isotherm constant, (L g−1)

K p :

Intraparticle diffusion rate constant, (mg g−1 min−0.5)

K R :

Redlich–Peterson isotherm constant, (L mg−1)

K S :

Affinity constant of Sips model, (L mg−1)

K T :

Toth isotherm constant (L mg−1)

N :

Number of experimental data, dimensionless

n F :

Heterogeneity factor of Freundlich model, dimensionless

n S :

Sips parameter related to the heterogeneity of the adsorption system, dimensionless

n t :

Heterogeneity factor of Toth model, dimensionless

pHPZC :

Point zero charge, dimensionless

q cal :

Calculated value of metal adsorbed, (mg g−1)

q D-R :

Adsorption capacity in the Dubinin–Radushkevich model, (mg g−1)

q e :

Equilibrium adsorption capacity, (mg g−1)

q e,calc :

Calculated amount of adsorbed Cu(II) ion at equilibrium, (mg g−1)

q e,exp :

Experimental amount of adsorbed Cu(II) ion at equilibrium, (mg g−1)

q exp :

Experimental value of metal adsorbed, (mg g−1)

q m :

Maximum adsorption capacity in the Sips model, (mg g−1)

q max :

Maximum adsorption capacity of the adsorbent, (mg g−1)

q R,max :

Adsorption capacity of the regenerated adsorbents, (mg g−1)

q t :

Adsorbed amount of Cu(II) ions at a given time, t (mg g−1)

R:

Universal gas constant, (8.314 J mol−1 K−1)

R 2 :

Coefficient of determination, dimensionless

R E :

Removal efficiency, (%)

R L :

Type of Langmuir isotherm, dimensionless

S BET :

BET surface areas, (m2 g−1)

SEM:

Scanning electron microscopy

SR:

Swelling ratio, (%wt)

t :

Time, (min)

T :

Absolute temperature, (K)

TGA:

Thermogravimetric analysis

V :

Volume of the solution, (mL)

W 0 :

Mass of beads in the initial dried state, (g)

W S :

Mass of the beads in swollen state, (g)

χ 2 :

Reduced chi-square error, dimensionless

XRD:

X-ray diffraction

β :

Redlich–Peterson isotherm exponent, dimensionless

ε :

Dubinin−Radushkevich adsorption potential, (kJ mol−1)

ΔpH:

Difference between initial pH and final pH, dimensionless

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Acknowledgements

Technical assistance from the Scientific-Technical Services of the University of Oviedo is gratefully acknowledged.

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Authors

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Correspondence to Manuel Rendueles.

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Responsible editor: Tito Roberto Cadaval Jr

Highlights Novel cellulose beads (CBBAS), simply synthesized from bleached almond shell, are efficient materials for Cu ion adsorption, the capacity being 128.24 mg g−1

Electronic supplementary material

ESM 1

N2 adsorption–desorption isotherms of BAS and CBBAS is depicted in Fig. A1; determination of the pHPZC value of CBBAS adsorbent is presented in Fig. A2 and adsorption–desorption cycles of CBBAS adsorbent are shown in Fig. A3. (DOCX 115 kb)

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Maaloul, N., Oulego, P., Rendueles, M. et al. Synthesis and characterization of eco-friendly cellulose beads for copper (II) removal from aqueous solutions. Environ Sci Pollut Res 27, 23447–23463 (2020). https://doi.org/10.1007/s11356-018-3812-2

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  • DOI: https://doi.org/10.1007/s11356-018-3812-2

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