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Mathematical modeling and interpretation of equilibrium isotherms of Pb (II) from aqueous media by Chlorella pyrenoidosa immobilized in Luffa cylindrica

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Abstract

New sorbent was prepared from unicellular green microalgal Chlorella pyrenoidosa (CP) immobilized in Luffa cylindrica (CP-LC) as a biosorbent for the removal of lead ions from aqueous media in a batch experiment mode. The prepared biosorbent was characterized by Fourier transform infrared spectroscopy (FTIR) and scanning electron microscopy (SEM). In the experimental design of the Pb (II) removal process, the equilibrium isotherms were studied and modeled. To select the best-fit isotherm model for this biological process, the experimental data were fitted in the eighteen different types of one-, two-, three-, four-, and five-parameter isotherm models. A comparison of non-linear models for selecting the optimum isotherm showed Fritz–Schlunder (V) model gives the most accurate fit to describe the experimental data, determined based on several error functions. Taking into account the outcome and in an attempt to optimize the equilibrium isotherms, the equation of Fritz-Schlünder (V) was modified to obtain more sophisticated model and more precision parameters values. As a consequence of such a developed model to existing mentioned ones, the mathematical model developed in this study is more suitable for predicting the equilibrium data. According to the results obtained, the evaluation of experimental data in terms of biosorption kinetics elucidated that the biosorption of Pb (II) by CP-LC well followed pseudo-second-order kinetics. The maximum biosorbent capacity of CP-LC was found to be 123 mg/g for 40 min at pH5. The calculated thermodynamic factors (∆G°, ∆H°, and ∆S°) indicated that the biosorption process was favorable, spontaneous, and exothermic at 298–318 K.

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Abbreviations

Ak (mg/g):

Koble-Carrigan isotherm constant

ae (-):

Activity of Pb (II) in solution at equilibrium

akh (–):

Constant in Khan isotherm

aR (L/g):

Constant in Redlich–Peterson isotherm

ARE:

average relative error

A T (L/g):

Equilibrium binding constant

as:

Activity of adsorbed Pb (II)

bo (L/g):

Constant in Baudu isotherm

Bk (L/g):

Koble-Carrigan isotherm constant

bKH (L/g):

Constant in Khan isotherm

bR (–):

Constant in Redlich–Peterson isotherm

BT (Kj/mol):

Temkin constant

b T (Kj/mol):

Adsorption energy

C (L/g):

Fritz-Schlünder (IV) constant

C0 (mg/L):

Initial Pb (II) ion concentration

Ce (mg/L):

Pb (II) ion concentration in solution at equilibrium

Cs (mg/g):

Pb (II) adsorbed on CP-LC

CP:

Chlorella pyrenoidosa

CP-LC:

Chlorella pyrenoidosa immobilized in luffa cylindrica

D (L/g):

Fritz-Schlünder (IV) constant

ERSQ (–):

Sum of the squares of the errors

GM:

Growth medium

HYBRID:

Hybrid fractional error function

IUPAC:

International union of pure and applied chemistry

K (–):

Henry’s isotherm model adsorption constant

K1 (1/min):

The rate constant of pseudo first-order model

K2 (g/mg/min):

the rate constant of pseudo second-order model

Kc (-):

The distribution constant

K K1 (L/g):

Kiselev equilibrium constant

K K2 (–):

Constant of complex formation between adsorbed molecules

KE (L/mg):

Elovich constant

K F (mg/g)(L/g)1/n :

Adsorption capacity

K FH (L/g):

Flory–Huggins equilibrium constant

K FG (L/g):

Fowler–Guggenheim equilibrium constant

KFS1 (L/g):

Fritz-Schlünder (v) equilibrium constant

kFS2 (L/g):

Fritz-Schlünder (v) equilibrium constant

K H (L/g):

Hill–de Boer constant

KL (L/mg):

Constant in Langmuir isotherm

K n (k/J/mol):

E nergetic constant of the interaction between adsorbed molecules

KR (L/g):

Constant in Redlich–Peterson isotherm

KRP (L/g):

Constant in Radke–Prausnitz isotherm

ks (L/g):

Constant in Sips isotherm

KT (L/g):

Constant in Toth isotherm

m (g/L):

Dose of free or immobilized cells

M1, M2 (–):

Constants in Fritz-Schlünder model

MPSD:

Marquardt’s percent standard deviation

N (–):

Number of observations in the experimental isotherm

n (–):

Constant in Freundlich isotherm

n FH (–):

Number of adsorbates occupying adsorption sites

nK (–):

Noefficient in Koble-Carrigan isotherm

nR (–):

Constant in Radke–Prausnitz isotherm

nS (–):

Coefficient in Sips isotherm

nT (–):

Constant in Toth isotherm

P (–):

Number of parameters in the regression model

qcal (mg/g):

Estimate from the isotherm for corresponding qexp

qe (mg/g):

Adsorption capacity

qexp (mg/g):

Observation from the batch experiment

q mKH (mg/g):

Maximum adsorbate uptake from Khan model

q m (mg/g):

Maximum adsorbate uptake from Radke–Prausnitz model

q mb (mg/g):

Maximum adsorbate uptake from Baudu model

q max (mg/g):

Maximum adsorbate uptake from Langmuir model

q mE (mg/g):

Maximum adsorbate uptake from elovich model

mFS (mg/g):

Fritz-Schlünder (v) maximum adsorption capacity.

q mk (mg/g):

Maximum adsorbate uptake from Toth model

q mS (mg/g):

Maximum adsorbate uptake from sips model

R (J/mol K):

Ideal gas constant

R2 (–):

Coefficient of determination

RL (-):

Separation factor

S2 :

Residual variance

SEM:

Scaninig electron microscopy

t (min):

Time

T (K):

Temperature

W (KJ/mol):

Interaction energy between adsorbed molecules

x, y (–):

Constants in Baudu isotherm

Ye (–):

Activity coefficient of Pb (II) in equilibrium solution

Ys (–):

Activity coefficient of adsorbed Pb (II)

∆H◦ (kJ/mol):

Enthalpy change

∆S◦ (J/mol K):

Entropy change

∆G◦(kJ/mol):

Gibbs free energy change (kJ/mol)

Ø (–):

Surface coverage of the adsorbent

α, ß (–):

Constant in modified Fritz-Schlunder (v)

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Acknowledgements

The authors (s) thank the anonymous reviewers for helping us to present this research in a more effective manner. The authors also are thankful to Mr. Ramzi Touchan, Research Professor at the Laboratory of Tree-Ring Research, University of Arizona, for his critical suggestions.

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Nouacer, I., Benalia, M., Henini, G. et al. Mathematical modeling and interpretation of equilibrium isotherms of Pb (II) from aqueous media by Chlorella pyrenoidosa immobilized in Luffa cylindrica. Biomass Conv. Bioref. 13, 7839–7858 (2023). https://doi.org/10.1007/s13399-021-01722-4

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