RELATIONAL DESCRIPTION OF AN ADSORPTION SYSTEM BASED ON ISOTHERM, ADSORPTION DENSITY, ADSORPTION POTENTIAL, HOPPING NUMBER AND SURFACE COVERAGE

RELATIONAL DESCRIPTION OF AN ADSORPTION SYSTEM BASED ON ISOTHERM, ADSORPTION DENSITY, ADSORPTION POTENTIAL, HOPPING NUMBER AND SURFACE COVERAGE

Gossweilerdendron balsamiferum (Tola wood) dust, as a precursor was used for the production of acid-activated carbon (TDAC) employed in the adsorptive removal of Cu2+ and Pb2+ ions. The relational adsorptive behaviour of TDAC, equilibrium studies and statistical evaluation of the data prediction performance of the respective models were conducted. The adsorbent was characterized using scanning electron microscopy (SEM) and Fourier transform infrared spectroscopy. Removal efficiencies of 75.66 % (for Cu-loaded TDAC) and 72.22 % (for Pb-loaded TDAC) were recorded at optimum pH (pH 6.0). The values of adsorption density, adsorption potential, hopping number and surface coverage were 7.256E-13 mol/L; -4920.78 J/mol; 8.44; 0.86 and 9.623E-13 mol/L; -5648.6 J/mol; 8.53; 0.86, for Cu- and Pb-loaded TDAC, respectively. Modified Langmuir model emerged as the best fit model for both adsorption system, as it depicted the lowest average error values of 1.8E-11 (for Cu-loaded TDAC) and 1.43E-12 (for Pb-loaded TDAC). Furthermore, model prediction performance showed that 5-parameter equation with t- and p-values of -0.862; 0.439 (for Cu-loaded TDAC) and -0.804; 0.466 (for Pb-loaded TDAC), was the least predictive among the isotherm models. The study demonstrated the effective application of TDAC in Cu2+ and Pb2+ adsorption, with the Cu-loaded TDAC being more efficient.

___

  • [1] Aniagor, C.O., Menkiti M.C, Kinetics and mechanistic description of adsorptive uptake of crystal violet dye by lignified elephant grass complexed isolate. Journal of Environmental Chemical Engineering. 2018; 6: 2105–2118. https://doi.org/10.1016/j.jece.2018.01.070
  • [2] Roger, M.R, Removal of metal ions from contaminated water using agricultural residues. ECO WOOD—2nd International conference on environmentally compatible forest products, 2006; 241–250.
  • [3] Renge, V.C., Khedkar, S.V., Pande, S.V., Removal of heavy metals from wastewater using low-cost adsorbents: a review. Sci. Rev. Chem. Commun., 2012; 2(4): 580–584.
  • [4] WHO (World Health Organization). Trace Elements in Human Nutrition and Health, 1996; Geneva, Switzerland.
  • [5] Menkiti, M.C., Ani, J.U., Onukwuli, O.D., Coagulation flocculation performance of snail shell biomass for wastewater purification. New York Sci. J., 2011; 4(2): 81–90
  • [6] Menkiti, M.C., Ejimofor, M.I., Ezemagu, I.G., Uddameri, V., Turbid-metric approach on the study of the adsorptive component of paint effluent coagulation using snail shell extract. Arab J. Sci. Eng., 2016; 41: 2527. DOI:10.1007/s13369-015-2013-2
  • [7] Giri, A.K., Patel, R., Mandal, S, Removal of Cr (VI) from aqueous solution by Eichhornia crassipes root biomass-derived activated carbon. Chem. Eng. J., 2012; 34, 185–186
  • [8] Nethaji, S., Sivasaoyyy, A., Mandal, S, Preparation and characterization of corn cob activated carbon coated with nano-sized magnetite particles for the removal of Cr (VI) Bioresour. Technol., 2013; 134: 94–100.
  • [9] Saha, B., Orvig, C, Adsorbent for hexavalent chromium elimination from industrial and municipal effluents. Coord. Chem. Rev., 2010; 254: 2959–2972
  • [10] Albadarin, A.B., Mangwandi, C., Al-Muhtaseb, A.A.H., Walker, G.M. Allen, S.J., Ahmad, M.N.M, Kinetics and thermodynamics of chromium ions adsorption onto low-cost dolomite adsorbent. Chem. Eng. J., 2012; 179: 193–202
  • [11] Wa Mulange, D.M., Garbers-Craig, A.M, Stabilization of Cr (VI) from fine ferrochrome dust using exfoliated vermiculite. J. Hazard. Mater., 2012; 12: 223–224.
  • [12] Menkiti M. C., Aniagor C. O, Parametric studies on descriptive isotherms for the uptake of crystal violet dye from aqueous solution onto lignin-rich adsorbent, Arabian Journal of Science and Engineering, 2017; 3(3): 205–220. DOI: 10.1007/s13369-017-2789-3
  • [13] Yan, H., Yang, H., Li, A.M., Cheng, R.S, pH-tunable surface charge of chitosan/graphene oxide composite adsorbent for efficient removal of multiple pollutants from water. Chem. Eng. J., 2016; 284:1397–1405.
  • [14] Crini, G., Badot, P.M, Application of Chitosan, a natural Aminopolysaccharide, for dye removal from aqueous solutions by adsorption processes using batch studies: a review of recent literature. Prog. Polym Sci., 2008; 33: 399-447. http://dx.doi.org/10.1016/j.progpolymsci.2007.11.001
  • [15] Gupta, V.K., Suhas, Application of Low-Cost Adsorbents for Dye Removal—A Review. Journal of Environmental Management, 2009; 90: 2313-2342.
  • [16] Nyiszli, M, Auschwitz: A Doctor's Eyewitness Account. New York: Arcade Publishing, 2011; 34.
  • [17] Green, H, Wood: Craft, Culture, History Penguin Books, New York, 2006.
  • [18] Larous, S.1., Meniai, A.H, Removal of copper (II) from aqueous solution by agricultural by-products sawdust. Energy Procedia, 2012; 18: 915 – 923
  • [19] Aniagor, C.O, Adsorption of copper (II) and lead (II) metal ions from aqueous solution using Tola (wood) dust activated carbon. Unpublished thesis, Nnamdi Azikiwe University, Awka, 2012.
  • [20] Horsfall, M., Spiff, A.L, Effects of temperature on the sorption of Pb2+ and Cd2+ from aqueous solution by Caladium bicolor (Wild Cocoyam) biomass. Electronic Journal of Biotechnology, 2005; 8: 2.
  • [21] Menkiti, M.C., Aneke, M.C., Ejikeme, P.M., Onukwuli, O.D., Menkiti, N.U, Adsorptive treatment of brewery effluent using activated Chrysophyllum albidium seed shell carbon. Springerplus, 2014; 3: 213.
  • [22] Soares, M.A.R., Quina, M.M.J., Gando–Ferreira, L., Quinta–Ferreira, R.M, Removal of Pb (II) from aqueous solutions using eggshell composting products, Second International Conference on Sustainable Solid and Waste Management, Athens, 2014.
  • [23] Galindo, L.S.G., De, A.F., Neto, A, Removal of cadmium (II) and lead(II) Ions from the aqueous phase on sodic bentonite, Mat. Res., 2013; 16: 515–527.
  • [24] Menkiti M.C., Aniagor C.O., Agu C.M., Ugonabo V.I, Effective adsorption of crystal violet dye from an aqueous solution using lignin-rich isolate from elephant grass. Water Conservation Science and Engineering, 2018; 3(1): 33 – 46. https://doi.org/10.1007/s41101-017-0040-4
  • [25] Padmesh, T.V.N., Vijayaraghavan, K., Sekaran, G., Velan, M, Application of two – and three-parameter isotherm models: biosorption of acid red 88 onto Azolla microphylla, Biorem. J., 2006; 10: 37–44.
  • [26] Piccin, J.S., Gomes, C. S., Féris, L.A., Mariliz. G, Kinetics, and isotherms of leather dye adsorption by tannery solid waste. Chemical Engineering Journal, 2012; 183: 30 –38. DOI: 10.1016/j.cej.2011.12.013
  • [27] Azizian, S., Eris, S., Wilson, L.D, Re-evaluation of the century-old Langmuir isotherm for modeling adsorption phenomena in solution. Chemical physics, 2018; 513: 99-104.
  • [28] Shafique, U., Ijaz, A., Salman, M., Zaman, W.U., Jamil, N., Rehman, R., Javaid, A, Removal of arsenic from water using pine leaves, J. Taiwan Inst. Chem. E., 2012; 43: 256–263.
  • [29] Temkin, M.J., Pyzhev V, Kinetics of ammonia synthesis on promoted iron catalysts, Acta Physiochim. URSS, 1940; 12: 217–222.
  • [30] Foo, K. Y., Hameed, B. H, Insights into the modeling of adsorption isotherm systems, Chemical Engineering Journal, 2010; 156(1): 2–10.
  • [31] Jovanovic, D.S, Physical sorption of gases: Isotherms for monolayer and multilayer sorption, Colloid Polym. Sci., 1969; 235:1203–1214.
  • [32] Ng, J.C.Y., Cheung, W.H., McKay, G, Equilibrium studies of the sorption of Cu (II) ions onto chitosan, J. Colloid Interface Sci., 2002; 255: 64–74.
  • [33] Sips, R, Combined form of Langmuir and Freundlich equations, J. Chem. Phys., 1948; 16: 490 – 495.
  • [34] Toth, J, State equations of the solid-gas interface layer, Acta Chem. Acad. Hung., 1971; 69: 311 – 317.
  • [35] Brouers, F., Sotolongo, O., Marquez, F., Pirard, J.P, Microporous and heterogeneous surface adsorption isotherms arising from Levy distributions, Physica A, 2005; 349: 271–282.
  • [36] Vieth, W.R., Sladek, K.J, A model for diffusion in a glassy polymer, J. Colloid Sci., 1965; 20: 1014–1033.
  • [37] Hamidpour, M., Kalbasi, M., Afyuni, M., Shariatmadar, H, Kinetic and isothermal studies of cadmium sorption onto bentonite and zeolite, Int. Agrophys., 2010; 24: 253–259.
  • [38] Khan, A.R., Ataullah, R., Al–Haddad, A, Equilibrium adsorption studies of some aromatic pollutants from dilute aqueous solutions on activated carbon at different temperatures, J. Colloid Interface Sci., 1997; 194: 154–165.
  • [39] Ringot, D., Lerzy, B., Chaplain, K., Bonhoure, J.P., Auclair, E., Larondelle, Y, In vitro biosorption of ochratoxin A on the yeast industry by-products: comparison of isotherm models, Bioresource Technol., 2007; 98: 1812–1821.
  • [40] Hadi, M., McKay, G., Samarghandi, M. R., Maleki, A., Aminabad, M.S, Prediction of optimum adsorption isotherm: comparison of chi–square and log–likelihood statistics. Desalination Water Treat., 2012; 49: 81–94.
  • [41] Fritz, W., Schlunder, E.U, Simultaneous adsorption equilibria of organic solutes in dilute aqueous solution on activated carbon, Chem. Eng. Sci., 1974; 29: 1279–1282.
  • [42] Shahbeig, H., Bagheri, N., Ghorbanian, S.A., Hallajisani, A., Poorkarimi, S, A new adsorption isotherm model of aqueous solutions on granular activated carbon, WJMS, 2013; 9: 243–254.
  • [43] Markovski, J.S., Dokic, V., Milosavljevic´, M., Mitric´, M., Peric´–Grujic´, A.A., Onjia, A.E., Marinkovic, A.D, Ultrasonic assisted arsenate adsorption on solvothermal synthesized calcite modified by goethite, α–MnO2 and goethite/α–MnO2, Ultrason. Sonochem., 2014; 21: 790–801.
  • [44] Parker, G.R, Optimum isotherm equation and thermodynamic interpretation for aqueous 1, 1, 2–trichloroethene adsorption isotherms on three adsorbents, Adsorption, 1995; 1: 113–132.
  • [45] Baudu, M, Etude des interactions solute–fibers de charbon actif. Application et regeneration, Ph.D. diss., Universite de Rennes I, 1990.
  • [46] Auta, M., Hameed, B.H, Optimized waste tea activated carbon for adsorption of methylene blue and acid blue 29 dyes using response surface methodology. Chem. Eng. J., 2011; 175: 233–243.
  • [47] Cerozi, B., Fitzsimmons, K. The effect of pH on phosphorus availability and speciation in an aquaponics nutrient solution. Bioresource Technology, 2016; 219: 778–781. 10.1016/j.biortech.2016.08.079.
  • [48] Delle Site, A. Factors affecting sorption of organic compounds in natural sorbent/ water systems and sorption coefficients for selected pollutants. A review, J. Phys. Chem. Ref. Data, 2001; 30: 187–439.
  • [49] Jossens, L., Prausnitz, J.M., Fritz, W., Schlünder, E.U., Myers, A.L. Thermodynamics of multi–solute adsorption from dilute aqueous solutions, Chem. Eng. Sci., 1978; 33: 1097–1106.
  • [50] Quin˜ones, I., Guiochon, G. Derivation and application of a Jovanovic–Freundlich isotherm model for single-component adsorption on heterogeneous surfaces, J. Colloid. Interf. Sci., 1996; 183: 57–67.
  • [51] El-Khaiary, M.I., Malash, G.F. Common data analysis errors in batch adsorption studies. Hydrometallurgy, 2011; 105(3-4):314–320. https://doi.org/10.1016/j.hydromet.2010.11.005
  • [52] Mario, F. T. Elementary Statistics, 11TH Ed. Pearson Education Inc. Boston, USA, 2012.
  • [53] Greenbank, M., Manes, M. Application of the Polanyi Adsorption Potential Theory to Adsorption from Solution on Activated Carbon. J. Phys. Chem., 1981; 85: 3050-3059. Doi: 0022-3654/81/2085-3050$01.25/0
  • [54] Shannon, R. D. Revised effective ionic radii and systematic studies of interatomic distances in halides and chalcogenides. Acta Crystallogr. A., 1976; 2: 751–767.
  • [55] McNaught, A. D., Wilkinson, A. IUPAC Compendium of Chemical Terminology, 2nd ed. Blackwell Scientific Publications, Oxford, U.K, 1997.