Lead poison and lead in drinking water sources are common reports nowadays. This paper presents a report on removal of lead ion from aqueous solution using a household waste (used batteries). Spent batteries were collected, sectioned; carbon rods were removed and ground into powder. Powdered Carbon Rods (PCR) were sieved into different particle sizes. Adsorption properties of the adsorbent were studied using synthetic lead solutions and typical wastewaters with a particular attention to kinetics models and cost analysis. The study revealed that kinetic models can be grouped into two based on the values of correlation coef cient (R2) as adsorption kinetics models with R2 less than 0.96 and adsorption kinetics models with R2 greater than 0.96. The adsorption kinetic of Pb2+ onto PCR at different pH were 0.250 (l h-1), 0.375 (mg g-1) with R2 = 0.855 and 0.095(l h-1), 0.169(mg g-1) with R2= 0.992 at initial pH of 7.2 and 3.2 respectively for Pseudo rst-order. Applicability of the process to typical wastewaters and raw water samples showed that PCR can be used as an adsorbent for Pb2+ removal from aqueous solutions. The study concluded that the mechanism of adsorption of Pb2+ onto PCR as an adsorbent followed two-steps intra-particle and pore diffusion transport. The average costs of producing a kilogram of powdered carbon rods were found to be 0.875USD and 1.018 USD for public and generator electricity sources respectively. The cost producing PCR is dearer compared to the cost of producing empty fruit bunches (0.50USD kg-1), 0.068 USD kg-1 of powdered corn cob, cheaper compared to the cost of producing pencon shell based activated carbon (2.72 USD kg-1) and sugar cane based granular activated carbon by steam (3.12 USD kg-1).
Alam, Z.M.D., Muyibi, S.A., Mansor, M.F and Wahid, R., 2007. Activated carbons derived from oil palm empty fruit bunches: Application to environmental problems. Journal of Environmental Sciences, 19(1):103-108.
Almeida, M. F., Xará, S. M., Delgado, J and Costa, C. A., 2009. Laboratory study on the behaviour of spent AA household alkaline batteries in incineration. Waste Management, 29:342– 349.
APHA,. 1998. Standard method for the examination of water and wastewater, 20th edn, America Water Works Association and Water Pollution Control Federation, Washington DC.
Boyd, G.E., Adamson, A.W and Myers, L.S., 1947. The exchange adsorption of ions from aqueous solutions by organic zeolites, J. Am. Chem. Soc. 69:2836– 2848.
Crombie-Quilty, M.B and McLoughin, A. J., 1983. The adsorption of bovine serum albumin by activated sludge. Water Research, 17:39-45.
Ho, Y.S., 2007. Bibliometric analysis of adsorption technology in environmental science. Journal of Environmental Protection Science, 1:1-11.
Ho,Y.S and G. McKay., 1998a. A comparison of chemisorption kinetic models applied to pollutant removal on various sorbents, Process. Saf. Environ. Protect,76 (B4): 332–340.
Ismail, A., D.B, Adie., I. A., Oke., J.A Otun., N.O. Olarinoye., Lukman, S and C.A. Okuofu., 2009. Adsorption kinetics of cadmium ions onto powdered corn cobs. Canadian Journal of Chemical Engineering, 87: 896 – 906.
Johannes, H and Johan, O., 2002. Granular activated carbon performance at three south africa water treatment plants. Water SA Special edition. 36-42.
Michele, C and Johannes, H., 2004. Practical experiences with granular activated carbon at the rietvel water treatment plant. Water SA. 30: 88-96.
Oke, I. A, Umoru, L.E and Ogedengbe, M.O., 2007a. Properties and stability of a carbon-resin electrode. Journal of Materials and Design. 28(7):2251-2254.
Oke, I. A., Olarinoye, N.O and Adewusi, S.R.A., 2008. Adsorption kinetics for arsenic removal by untreated powdered eggshell from aqueous solutions. Journal of Adsorption Society,14(1): 85-92.
Oke, I. A., Umoru, L.E and Ogedengbe, M.O., 2007b. 2k factorial experiments on factors that in uence stability of carbon resin electrodes. FUTAJEET, 5(2):135-141.
Otun, J.A., Oke, I.A., Olarinoye, N.O., Adie, D.B and Okuofu, C.A., 2006a. Factors that in uence adsorption using 2k factorial experiment. Journal of Applied Sciences, 6 (11): 2432- 2437.
Otun, J.A; Oke, I.A; Olarinoye, N.O; Adie, D.B and Okuofu, C.A., 2006b. Adsorption isotherms of Pb(II), Ni(II) and Cd (II) onto PES. Journal of Applied Sciences, 6(11): 2368- 2376.
Ryu, Y.K; S.J. Lee; J.W. Kim and C.H. Lee., 2001. Adsorption equilibrium and Kinetics of H2O on Zeolite 13 X. Korean J.. Chem. Eng, 18(4):525-530.
Ulmanu, M., Anyer I., Maran-Muson, E., Peliez; C. C., Teadorescu, T. and Moreh, E., 2003. Single and competitive separation of copper and cadmium from aqueous solution on adsorbent materials. J. of Env.iron. Prot. and Eco., 4(1): 179-186.
Yasmin, K.; K. Mody; S. Basha, S and Jha. B., 2009. Kinetics, equilibrium and thermodynamic studies on biosorption of hexavalent chromium by dead fungal biomass of marine Aspergillus niger. Chemical Engineering Journal, 145:489– 495.
Zand, A.D and Abduli, M.A., 2008. Current situation of used household batteries in Iran and appropriate management policies. Waste Management. 28: 2085–2090.
Atık Pilleri Kullanarak Sıvı Çözeltilerden Kaldırılan Pb2+’nin Adsorbsiyon Kinetiği
İçme su kaynaklarındaki kurşun ve kurşun zehri günümüzde yaygın olarak ifade edilmektedir. Bu
çalışma evsel bir atık (kullanılmış pil) kullanarak, sıvı çözeltiden kurşun iyonlarının kaldırılması üzerine bir bilgi
sunmaktadır. Kullanılmış piller toplanılıp kesitlerine ayrıldıktan sonra, karbon çubukları çıkarıldı ve öğütüldü.
Adsorbentlerin adsorpsiyon özellikleri kinetic modeller ve maliyet anazlileri dikkate alınarak, tipik kirleticiler
ve sentetik kurşun çözücüler kullanılarak çalışıldı. Korelasyon katsayısı değerlerine göre mevcut çalışma kinetic
modellerin iki şekilde gruplandırılabileceğini ortaya koydu. Farklı pH değerlerinde (7.2 and 3.2) PCR üzerine
Pb2’nin adsorpsiyon kinetiği, sırasıyla R2 = 0.855 de 0.250 (l/h), 0.375 (mg/g) ve R2 = 0.992 de 0.095(l/h),
0.169(mg/g) idi. Tipik kirleticiler ve ham su örnekleri, PCR’nin sulu çözeltilerden Pb2+’nin kaldırılması için bir
adsorbent olarak kullanılabileceğini gösterdi. Maliyet analizleri ortlama 1 kg karbon çubukları üretmenin ortak
ve ortak olmayan elektrik kaynakları için sırasıyla 0.875USD ve 1018 USD mal olacağını gösterdi. Çalışma, bir
adsorbent olarak PCR üzerine Pb2+ adsorbsiyon mekanizmasının iki adımda gerçekleştiği ortaya çıktı.
Alam, Z.M.D., Muyibi, S.A., Mansor, M.F and Wahid, R., 2007. Activated carbons derived from oil palm empty fruit bunches: Application to environmental problems. Journal of Environmental Sciences, 19(1):103-108.
Almeida, M. F., Xará, S. M., Delgado, J and Costa, C. A., 2009. Laboratory study on the behaviour of spent AA household alkaline batteries in incineration. Waste Management, 29:342– 349.
APHA,. 1998. Standard method for the examination of water and wastewater, 20th edn, America Water Works Association and Water Pollution Control Federation, Washington DC.
Boyd, G.E., Adamson, A.W and Myers, L.S., 1947. The exchange adsorption of ions from aqueous solutions by organic zeolites, J. Am. Chem. Soc. 69:2836– 2848.
Crombie-Quilty, M.B and McLoughin, A. J., 1983. The adsorption of bovine serum albumin by activated sludge. Water Research, 17:39-45.
Ho, Y.S., 2007. Bibliometric analysis of adsorption technology in environmental science. Journal of Environmental Protection Science, 1:1-11.
Ho,Y.S and G. McKay., 1998a. A comparison of chemisorption kinetic models applied to pollutant removal on various sorbents, Process. Saf. Environ. Protect,76 (B4): 332–340.
Ismail, A., D.B, Adie., I. A., Oke., J.A Otun., N.O. Olarinoye., Lukman, S and C.A. Okuofu., 2009. Adsorption kinetics of cadmium ions onto powdered corn cobs. Canadian Journal of Chemical Engineering, 87: 896 – 906.
Johannes, H and Johan, O., 2002. Granular activated carbon performance at three south africa water treatment plants. Water SA Special edition. 36-42.
Michele, C and Johannes, H., 2004. Practical experiences with granular activated carbon at the rietvel water treatment plant. Water SA. 30: 88-96.
Oke, I. A, Umoru, L.E and Ogedengbe, M.O., 2007a. Properties and stability of a carbon-resin electrode. Journal of Materials and Design. 28(7):2251-2254.
Oke, I. A., Olarinoye, N.O and Adewusi, S.R.A., 2008. Adsorption kinetics for arsenic removal by untreated powdered eggshell from aqueous solutions. Journal of Adsorption Society,14(1): 85-92.
Oke, I. A., Umoru, L.E and Ogedengbe, M.O., 2007b. 2k factorial experiments on factors that in uence stability of carbon resin electrodes. FUTAJEET, 5(2):135-141.
Otun, J.A., Oke, I.A., Olarinoye, N.O., Adie, D.B and Okuofu, C.A., 2006a. Factors that in uence adsorption using 2k factorial experiment. Journal of Applied Sciences, 6 (11): 2432- 2437.
Otun, J.A; Oke, I.A; Olarinoye, N.O; Adie, D.B and Okuofu, C.A., 2006b. Adsorption isotherms of Pb(II), Ni(II) and Cd (II) onto PES. Journal of Applied Sciences, 6(11): 2368- 2376.
Ryu, Y.K; S.J. Lee; J.W. Kim and C.H. Lee., 2001. Adsorption equilibrium and Kinetics of H2O on Zeolite 13 X. Korean J.. Chem. Eng, 18(4):525-530.
Ulmanu, M., Anyer I., Maran-Muson, E., Peliez; C. C., Teadorescu, T. and Moreh, E., 2003. Single and competitive separation of copper and cadmium from aqueous solution on adsorbent materials. J. of Env.iron. Prot. and Eco., 4(1): 179-186.
Yasmin, K.; K. Mody; S. Basha, S and Jha. B., 2009. Kinetics, equilibrium and thermodynamic studies on biosorption of hexavalent chromium by dead fungal biomass of marine Aspergillus niger. Chemical Engineering Journal, 145:489– 495.
Zand, A.D and Abduli, M.A., 2008. Current situation of used household batteries in Iran and appropriate management policies. Waste Management. 28: 2085–2090.
Oke, İ. A. (2014). Adsorption Kinetics of Pb2+ Removal from Aqueous Solutions Using Spent Batteries. Journal of the Institute of Science and Technology, 4(1), 49-54.
AMA
Oke İA. Adsorption Kinetics of Pb2+ Removal from Aqueous Solutions Using Spent Batteries. Iğdır Üniv. Fen Bil Enst. Der. Mart 2014;4(1):49-54.
Chicago
Oke, İsaiah Adesola. “Adsorption Kinetics of Pb2+ Removal from Aqueous Solutions Using Spent Batteries”. Journal of the Institute of Science and Technology 4, sy. 1 (Mart 2014): 49-54.
EndNote
Oke İA (01 Mart 2014) Adsorption Kinetics of Pb2+ Removal from Aqueous Solutions Using Spent Batteries. Journal of the Institute of Science and Technology 4 1 49–54.
IEEE
İ. A. Oke, “Adsorption Kinetics of Pb2+ Removal from Aqueous Solutions Using Spent Batteries”, Iğdır Üniv. Fen Bil Enst. Der., c. 4, sy. 1, ss. 49–54, 2014.
ISNAD
Oke, İsaiah Adesola. “Adsorption Kinetics of Pb2+ Removal from Aqueous Solutions Using Spent Batteries”. Journal of the Institute of Science and Technology 4/1 (Mart 2014), 49-54.
JAMA
Oke İA. Adsorption Kinetics of Pb2+ Removal from Aqueous Solutions Using Spent Batteries. Iğdır Üniv. Fen Bil Enst. Der. 2014;4:49–54.
MLA
Oke, İsaiah Adesola. “Adsorption Kinetics of Pb2+ Removal from Aqueous Solutions Using Spent Batteries”. Journal of the Institute of Science and Technology, c. 4, sy. 1, 2014, ss. 49-54.
Vancouver
Oke İA. Adsorption Kinetics of Pb2+ Removal from Aqueous Solutions Using Spent Batteries. Iğdır Üniv. Fen Bil Enst. Der. 2014;4(1):49-54.