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Received November 10, 2016
Accepted March 16, 2017
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Removal of methylene blue dye from aqueous solutions by a new chitosan/zeolite composite from shrimp waste: Kinetic and equilibrium study
Mohammad Hadi Dehghani1 2†
Aliakbar Dehghan1†
Hossein Alidadi3
Maryam Dolatabadi3
Marjan Mehrabpour3
Attilio Converti4
1Tehran University of Medical Sciences, School of Public Health, Department of Environmental Health Engineering, Tehran, Islamic Republic of Iran 2Institute for Environmental Research, Center for Solid Waste Research, Tehran, Islamic Republic of Iran 3Health Sciences Research Center, Department of Environmental Health Engineering, School of Health, Mashhad University of Medical Sciences, Mashhad, Islamic Republic of Iran 4Department of Civil, Chemical and Environmental Engineering, Chemical Engineering Pole, Genoa University, Via Opera Pia 15, I-16145 Genoa, Italy
hdehghani@tums.ac.ir
Korean Journal of Chemical Engineering, June 2017, 34(6), 1699-1707(9), 10.1007/s11814-017-0077-2
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Abstract
The adsorption of methylene blue dye (MBD) from aqueous solutions was investigated using a new composite made up of shrimp waste chitosan and zeolite as adsorbent. Response surface methodology (RSM) was used to optimize the effects of process variables, such as contact time, pH, adsorbent dose and initial MBD concentration on dye removal. The results showed that optimum conditions for removal of MBD were adsorbent dose of 2.5 g/L and pH of 9.0, and initial MBD concentration of 43.75mg/L and contact time of 138.65 min. The initial concentration of dye had the greatest influence on MBD adsorption among other variables. The experimental data were well fitted by the pseudo-second order kinetic model, while the Freundlich isotherm model indicated a good ability for describing equilibrium data. Acc ording to this isotherm model, maximum adsorption capacity of the composite was 24.5mg/g.Desorption studies showed that the desorption process is favored at low pH under acidic conditions.
Keywords
References
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Ghaedi M, Kokhdan SN, Spectrochim. Acta A., 136, 141 (2015)
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Mahmoodi NM, Hayati B, Arami M, Lan C, Desalination, 268(1-3), 117 (2011)
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Geethakarthi A, Phanikumar BR, Int. J. Environ. Sci. Technol., 8, 561 (2011)
Cao JS, Lin JX, Fang F, Zhang MT, Hu ZR, Bioresour. Technol., 163, 199 (2014)
Alver E, Metin AU, Chem. Eng. J., 200-202, 59 (2012)
Geethakarthi A, Phanikumar B, Environ. Sci. Pollut. Res., 19, 656 (2012)
Prola LDT, Acayanka E, Lima EC, Umpierres CS, Vaghetti JCP, Santos WO, Laminsi S, Djifon T, Ind. Crop. Prod., 46, 328 (2013)
Li Q, Zhao Y, Wang L, Aiqin W, Korean J. Chem. Eng., 8, 28 (2011)
Celekli A, Celekli F, Cicek E, Bozkurt H, Environ. Sci. Pollut. Res., 21, 5086 (2014)
Saeed M, Nadeem R, Yousaf M, Int. J. Environ. Sci. Technol., 12, 1223 (2015)
Song Y, Ding S, Chen S, Xu H, Mei Y, Ren J, Korean J. Chem. Eng., 12, 32 (2015)
Dehghani MH, Naghizadeh A, Rashidi A, Derakhshani E, Desalin. Water Treat, 51(40-42), 7655 (2013)
Janaki V, Vijayaraghavan K, Oh BT, Lee KJ, Muthuchelian K, Ramasamy AK, Kannan SK, Carbohydr. Polym., 90, 1437 (2012)
Xie K, Zhao W, He X, Carbohydr. Polym., 83, 1516 (2011)
Ribas MC, Adebayo MA, Prola LDT, Lima EC, Cataluna R, Feris LA, Puchana-Rosero MJ, Machado FM, Pavan FA, Calvete T, Chem. Eng. J., 248, 315 (2014)
Cardoso NF, Lima EC, Royer B, Bach MV, Dotto GL, Pinto LAA, Calvete T, J. Hazard. Mater., 241, 146 (2012)
Kumar PS, Ramalingam S, Sathishkumar K, Korean J. Chem. Eng., 28(1), 149 (2011)
Brillas E, Huitle AM, Appl. Catal. B: Environ., 166 (2015)
Verma AK, Dash RR, Bhunia P, J. Environ. Manage., 93(1), 154 (2012)
Rondon H, El-Cheikh W, Boluarte IAR, Chang CY, Bagshaw S, Farago L, Jegatheesan V, Shu L, Bioresour. Technol., 183, 78 (2015)
Greluk M, Hubicki Z, Desalination, 278(1-3), 219 (2011)
Wijannarong S, Aroonsrimorakot S, Thavipoke P, Kumsopa C, Sangjan S, APCBEE Procedia, 5, 279 (2013)
Dehghani MH, Mahdavi P, Desalin. Water Treat., 54(12), 3464 (2014)
Anbia M, Hariri SA, Ashrafizadeh SN, Appl. Surf. Sci., 256(10), 3228 (2010)
Zhang W, Yang H, Dong L, Yan H, Li H, Jiang Z, Kan X, Li A, Cheng R, Carbohydr. Polym., 90, 887 (2012)
Zhong QQ, Yue QY, Li QA, Xu X, Gao BY, Desalination, 267(2-3), 193 (2011)
Ngah WSW, Teong LC, Hanafiah MAKM, Carbohydr. Polym., 83(4), 1446 (2011)
Lin JW, Zhan YH, Chem. Eng. J., 200, 202 (2012)
Hou HJ, Zhou RH, Wu P, Wu L, Chem. Eng. J., 211, 336 (2012)
Wan MW, Kan CC, Rogel BD, Dalida MLP, Carbohydr. Polym., 80, 891 (2010)
Liu Q, Yang B, Zhang L, Huang R, Int. J. Biol. Macromol., 72, 1129 (2015)
Wang L, Zhang JP, Wang AQ, Desalination, 266(1-3), 33 (2011)
Chang MY, Juang RS, J. Colloid Interface Sci., 278(1), 18 (2004)
Nesic AR, Velickovic SJ, Antonovic DG, J. Hazard. Mater., 209-210, 256 (2012)
Swayampakula K, Boddu VM, Nadavala SK, Abburi K, J. Hazard. Mater., 170(2-3), 680 (2009)
Hydari S, Sharififard H, Nabavinia M, Parvizi MR, Chem. Eng. J., 193-194, 276 (2012)
Travlou NA, Kyzas GZ, Lazaridis NK, Deliyanni EA, Chem. Eng. J., 217, 256 (2013)
Dutta S, Bhattacharyya A, Ganguly A, Gupta S, Basu S, Desalination, 275(1-3), 26 (2011)
Nesic AR, Velickovic SJ, Antonovic DG, Composites Part B: Eng., 53, 145 (2013)
Sagheer FAA, Sughayer MAA, Muslim S, Elsabee MZ, Carbohydr. Polym., 77, 410 (2009)
Mohanasrinivasan V, Mishra M, Paliwal JS, Singh SK, Selvarajan E, Suganthi V, Devi CS, 3 Biotech., 4, 167 (2014)
Ghaedi M, Khafri HZ, Asfaram A, Spectrochim. Acta A., 152, 233 (2016)
Lagergren S, Vetenskapsakademiens KS, Handlingar., 24(4), 1 (1898)
Ho YS, McKay G, Chem. Eng. J., 70(2), 115 (1998)
Weber W, Morris J, J. Sanit. Eng. Div., 89, 31 (1963)
Ngah WSW, Teong LC, Wong CS, Hanafiah MAKM, J. Appl. Polym. Sci., 3, 125 (2012)
Ghaedi M, Kokhdan SN, Spectrochim. Acta A., 136, 141 (2015)
Su CSH, Teng TT, Alkarkhi AFM, Low LW, Water. Air. Soil. Poll., 5, 225 (2014)