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
- 푞mFS (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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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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DOI: https://doi.org/10.1007/s13399-021-01722-4