[会议]
Chlorinated phenol removal from aqueous media by tea (Camellia sinensis) leaf waste tailored activated carbon
作者:
Joseph, C. G. 1;Anisuzzaman, S. M. 2;Daud, W. M. A. W. 3;Krishnaiah, D. 2;Ng, K. A. 1 1 Fac. of Sci. & Natural Resources, Univ. Malaysia Sabah, Kota Kinabalu, Universiti Malaysia Sabah, Faculty of Science & Natural Resources, Water Research Unit, Kota Kinabalu, 88400, Malaysia collin@ums.edu.my 2 Fac. of Eng., Univ. Malaysia Sabah, Kota Kinabalu, Universiti Malaysia Sabah, Faculty of Engineering, Kota Kinabalu, 88400, Malaysia 3 Dept. of Chem. Eng., Univ. of Malaya, Kuala Lumpur, University of Malaya, Department of Chemical Engineering, Kuala Lumpur, 50603, Malaysia
发表时间:
2017
会议集名/来源:
IOP Conference Series: Materials Science and Engineering
In this study, activated carbons (ACs) wereprepared from tea leaves by using a two-stage self-generated atmosphere method. The process was done by semi-carbonizing the precursor at 300 °C for 1 h, followed by the impregnation of the resulting char at 85 °C for 4 h and finally activation at 500 °C for 2 h. The semi-carbonised samples were impregnated with different ratios of zinc chloride (ZnCl2) and their physicochemical effect was studied. The prepared ACs underwent several aspects of both, chemical and physical characterizations, such as the percentage of yield, moisture content, ash content, pH, porosity, adsorption capacity of 2,4-dichlorophenol (2,4-DCP), surface area, porosity, morphology and surface chemistry studies. It was found that sample AC2, with an impregnation ratio of 2:1 was the best AC produced in this study. The maximum Brunauer, Emmett and Teller surface area of AC2 was found to be 695 m2/g. Langmuir, Freundlich and Temkin isotherm models were used to examine the experimental isotherms while the kinetic data was analyzed using the pseudo-first-order, pseudo-second-order and intraparticle diffusion kinetic models. The 2,4-DCP adsorption isotherm results complied well to the Langmuir isotherm for the equilibrium data while the adsorption kinetic data fitted well to the pseudo-second order model, indicating that chemisorption by valency forces via the sharing (covalent bond) or exchanging of electrons between the AC and the 2,4-DCP molecules were mainly responsible for the adsorption process. From these findings, it is concluded that tea leaves can be used as a low cost precursor for the removal of 2,4-DCP in aqueous medium. Swaminathan G and Ramanujam T K 1999 Bioprocess Eng.21 169 Nowicki P, Kazmierczak J and Robert P 2015 Powder Technol.269 312 Joseph C G, Bono A, Anisuzzaman S M and Krishnaiah D 2014 J. Appl. Sci.14 3182 Krishnaiah D, Anisuzzaman S M, Bono A and Sarbatly R 2013 J. King Saud Univ. Sci25 251 Anisuzzaman S M, Joseph C G, Daud W M A W, Krishnaiah D and Yee H S 2015 Int. J. Ind. Chem6 9 Anisuzzaman S M, Joseph C G, Krishnaiah D, Bono A and Ooi L C 2015 Parametric and adsorption kinetic studies of methylene blue removal from textile simulated sample using Durian (DuriozibethinusMurray) skin Manuscript accepted in the journal of Water Sci. Technol. Anisuzzaman S M, Joseph C G, Taufiq-Yap Y H, Krishnaiah D and Tay V V 2015 J. King Saud Univ. Sci. (in press) Daud W M A W and Houshamnd A H 2010 J. Nat. Gas. Chem.19 267 Alicia Peláez-Cid A. and Margarita Teutli-León M.M. 2012 ed Virginia Hernández Montoya Dr. (InTech) Lignocellulosic Precursors Used in the Elaboration of Activated Carbon, Lignocellulosic Precursors Used in the Synthesis of Activated Carbon - Characterization Techniques and Applications in the Wastewater Treatment Özhan A, Ömer S, Küçük M M and Cafer S 2014 Cellulose.21 2457 Virginia Hernández-Montoya and Adrian Bonilla-Petriciolet 2012, 1stCroatia Vol. 1 Joseph C G and Yii F 2008 J. Eng. Sci. Technol.3 234 Kim J W, Sohn M H, Kim D S, Sohn S M and Kwon Y S 2001 J. Hazard. Mater.85 301 Karen J S, Greisly D M and Puello J 2014 Chem.Eng. Transactions.37 721 Tan I A W, Ahmad A L and Hameed B H 2008 J. Hazard. Mater154 337-346 Bulut Y and Aydın H 2006 Desalination.194 259 Gupta V K, Agarwal S. and Saleh T.A. 2011 J. Hazard. Mater.185 17 Gupta V K and Nayak A 2012 Chem. Eng. J.180 81 Hameed B H and Ahmad A A 2009 J. Hazard. Mater.164 870 Hartono S B, Ismadji S, Sudaryanto Y and Irawaty W 2005 J. Ind. Eng. Chem.11 864 Mittal A, Kaur D, Malviya A, Mittal J and Gupta V K 2009 J. Colloid. Interf.Sci.337 345 Tham Y J, Latif P A, Abdullah A M, Shamala-Devi A and Taufiq-Yap Y H 2011 Bioresources Technol.102 724 Al-Qodah Z and Shawabkah R 2009 Braz. J. Chem. Eng.26 127 Gundogdu A, Duran C, Senturk H B, Soylak M, Ozdes D, Serencam H and Imamoglu M 2012 J. Chem. Eng. Data.57 2733 Ahmaruzzaman M and Laxmi G S 2010 J. Chem. Eng. Data.55 4614 Graham H N 1992 Prev.Med.21 334 Wankhade A A and Ganvir V N 2013 Int.Res. J. Environment Sci.2 53 Kennedy L J, Vijaya J J, Kayalvizhi K and Sekaran G 2007 Chem. Eng. J.132 279 Sahu J N, Acharya J and Meikap B C 2010 Bioresource Technol.101 1974
关键词:
activated carbon;adsorption;chemical engineering;industrial waste;organic compounds;surface chemistry;zinc compounds