Abstract
In this study, a generalized, comprehensive and feasible mathematical model was developed for the description of the adsorption of multicomponent system in a fixed bed containing solid adsorbent. It took into cognizance of all the factors considered negligible in the literature, which included intraparticle, interparticle and interphase diffusional resistances, conditions of non-equilibrium and non-linear binary adsorption of butan-2-ol and 2-methylbutan-2-ol onto the adsorbent Filtrasorb 400 (granular activated carbon). The resulting 4N hyperbolic and parabolic differential equations were numerically solved using orthogonal collocation on finite element method. Excellent agreements were achieved between the experimental data and the simulated results of breakthrough times and concentrations of the solutes in fixed beds of 0.41, 0.82 and 1.23 m. Equally, the observed chromatographic tops of the less strongly adsorbed component (butan-2-ol) and the effects of adsorber length on times of breakthrough of the components and height of peaks were precisely simulated. The results of this study are of beneficial use in the design and analysis of fixed beds employed for the treatment of multicomponent aqueous wastewater effluents from industry.
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Abbreviations
- ARD:
-
Average relative deviation
- EABS:
-
Sum of the absolute errors
- ERRSQ:
-
Sum of the squares of the errors
- HYBRID:
-
Composite fractional error function
- MAE:
-
Ean absolute error
- MAPE:
-
Mean absolute percentage error
- MPE:
-
Mean percentage error
- MPSD:
-
Marquardt’s percent standard deviation
- OCFEM:
-
Orthogonal collocation on finite element method
- RMSE:
-
Root mean square error
- SPE:
-
Standard prediction error
- \(a_{ij}\) :
-
Fritz-Schlüender model constant (L/mg)
- \(a_{i0}\) :
-
Fritz-Schlüender model constant (L/mg)
- \(b_{ij}\) :
-
Fritz- Schlüender model exponent
- \(b_{i0}\) :
-
Fritz- Schlüender model exponent
- \(\overline{c}_{e}\) :
-
Mean value of experimental breakthrough data (kg/m3)
- \(\overline{c}_{i}\) :
-
Dimensionless concentration of solute i in fluid phase of the column
- \(c_{i}\) :
-
Concentration of solute i in fluid phase of the column (kg/m3)
- \(\overline{c}_{i,\,e}\) :
-
Experimental breakthrough concentrations of solute for run i (kg/m3)
- \(\left( {c_{i} } \right)_{0}\) :
-
Inlet concentration of solute i in the column (kg/m3)
- \(\overline{c}_{i,\,p}\) :
-
Simulated (or predicted) breakthrough concentrations of solute for run i (kg/m3)
- \(c_{si}\) :
-
Amount of solute i adsorbed per unit volume of the particle (kg/m3) at equilibrium with a liquid phase concentration, \(X_{i}\), in a solution containing N solutes
- \(C_{i}\) :
-
Constant in Eq. (1) (dimensionless)
- \(D_{Li}\) :
-
Axial diffusivity for component i in the fluid phase (m2/s)
- \(D_{pi}\) :
-
Diffusivity for component i, in the fluid phase within the pore of an adsorbent (m2/s)
- \(D_{si}\) :
-
Diffusion coefficient for the diffusion of component i through the solid phase of an adsorbent (m2/s)
- \(k_{f}\) :
-
Freundlich isotherm constant (kg/m3)1−n
- \(K_{fi}\) :
-
Film mass transfer coefficient of solute i (m/s)
- \(n\) :
-
Degree of heterogeneity (dimensionless)
- N:
-
Number of solutes in solution (dimensionless)
- \(N_{e}\) :
-
Number of experimental runs (dimensionless)
- \(Pe_{i}\) :
-
Peclet number of component i (dimensionless)
- \(q_{i}^{*}\) :
-
Concentration of solute i in the solid (or adsorbed) phase (kg/m3)
- \(\left( {q_{i}^{*} } \right)_{0}\) :
-
Concentration of solute i in the solid (or adsorbed) phase (kg/m3)
- \(Q_{i}^{*}\) :
-
Dimensionless concentration of solute i in the solid (or adsorbed) phase
- r:
-
Radial distance in particle, i.e., radius of the adsorbent pellet as measured from center of pellet (m)
- R:
-
External radius of the adsorbent (m)
- \(R^{2}\) :
-
Coefficient of determination (or regression coefficient) (dimensionless)
- \(Sh_{i}\) :
-
Sherwood number of component i (dimensionless).
- t:
-
Time from start of sorption process (h)
- \(U_{f}\) :
-
Linear velocity in the positive direction of z (m/s)
- \(X_{i}\) :
-
Concentration of solute i in pore fluid phase (kg/m3)
- \(\overline{X}_{i}\) :
-
Dimensionless concentration of solute i in pore fluid phase
- z:
-
Axial distance in column (m)
- \(z_{T}\) :
-
Length of column (m)
- Z:
-
Dimensionless axial distance
- \(\alpha\) :
-
Geometry of the adsorbent (dimensionless)
- \(\in_{b}\) :
-
Void fraction in the bed, i.e., volume of voids per unit volume of bed (dimensionless)
- \(\in_{p}\) :
-
Void fraction in particles, i.e., volume of pores in the pellet per unit volume of pellet (dimensionless)
- \(\sigma\) :
-
Dimensionless radius
- \(\tau\) :
-
Dimensionless time
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Conceptualization: OAO; Methodology: KOA and AJA; Formal analysis and investigation: OAO; KOA, KFKO and AJA; Writing—original draft preparation: KOA and AJA; Writing—review and editing: OAO; KOA; KFKO and AJA; Resources: OAO and AJA; Supervision: OAO and KFKO.
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Olafadehan, O.A., Amoo, K.O., Oyedeko, K.F.K. et al. Dynamic Studies of Binary Adsorption System in Fixed Beds using Orthogonal Collocation on Finite Element Method. Int. J. Appl. Comput. Math 10, 108 (2024). https://doi.org/10.1007/s40819-024-01688-7
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DOI: https://doi.org/10.1007/s40819-024-01688-7