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Adsorption of phenol from aqueous solution by a hierarchical micro-nano porous carbon material 被引量:4

Adsorption of phenol from aqueous solution by a hierarchical micro-nano porous carbon material
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摘要 A hierarchical micro-nano porous carbon material (MNC) was prepared using expanded graphite (EG), sucrose, and phosphoric acid as raw materials, followed by sucrose-phosphoric acid solution impregnation, solidification, carbonization and activation. Nitrogen adsorption and mercury porosimetry show that mixed nanopores and micropores coexist in MNC with a high specific surface area of 1978 m2·g-1 and a total pore volume of 0.99 cm3·g-1. In addition, the MNC is found to consist of EG and activated carbon with the latter deposited on the interior and the exterior surfaces of the EG pores. The thickness of the activated carbon layer is calculated to be about one hundred nanometers and is further confirmed by scanning electron microscope (SEM) and transmission election microscope (TEM). A maximum static phenol adsorption of 241.2 mg·g-1 was obtained by using MNC, slightly higher than that of 220.4 mg·g-1 by using commercial activated carbon (CAC). The phenol adsorption kinetics were investigated and the data fitted well to a pseudo-second-order model. Also, an intra-particle diffusion mechanism was proposed. Furthermore, it is found that the dynamic adsorption capacity of MNC is nearly three times that of CAC. The results suggest that the MNC is a more efficient adsorbent than CAC for the removal of phenol from aqueous solution. A hierarchical micro-nano porous carbon material (MNC) was prepared using expanded graphite (EG), sucrose, and phosphoric acid as raw materials, followed by sucrose-phosphoric acid solution impregnation, solidification, carbonization and activation. Nitrogen adsorption and mercury porosimetry show that mixed nanopores and micropores coexist in MNC with a high specific surface area of 1978 m2·g-1 and a total pore volume of 0.99 cm3·g-1. In addition, the MNC is found to consist of EG and activated carbon with the latter deposited on the interior and the exterior surfaces of the EG pores. The thickness of the activated carbon layer is calculated to be about one hundred nanometers and is further confirmed by scanning electron microscope (SEM) and transmission election microscope (TEM). A maximum static phenol adsorption of 241.2 mg·g-1 was obtained by using MNC, slightly higher than that of 220.4 mg·g-1 by using commercial activated carbon (CAC). The phenol adsorption kinetics were investigated and the data fitted well to a pseudo-second-order model. Also, an intra-particle diffusion mechanism was proposed. Furthermore, it is found that the dynamic adsorption capacity of MNC is nearly three times that of CAC. The results suggest that the MNC is a more efficient adsorbent than CAC for the removal of phenol from aqueous solution.
出处 《Rare Metals》 SCIE EI CAS CSCD 2012年第6期582-589,共8页 稀有金属(英文版)
基金 financially supported by the Fundamental Research Funds for the National Natural Science Foundation of China(Nos.21071107,21277094,and21103119) Production and Research Collaborative Innovation Project of Jiangsu Province(No.BY2012123) Natural Science Foundation of Jiangsu Province(No.BK2012167) Scienceand Technology Pillar Program(Industry)of Jiangsu Province(No.BE2012101) Collegiate Natural Science Fund of Jiangsu Province(Nos.12KJA430005,09KJB30003,and11KJB430012) Key Laboratory for Environment Functional Materials of Suzhou(No.SZS201008) A Project Funded by the Priority Academic Program Development of Jiangsu Higher Education Institutions(PAPD),Applied Basic Research Project of Suzhou(No.SYG201242) Industrial Surport Project of Suzhou(No.SG201138) Jiangsu Key Laboratory of Material Tribology(No.Kjsmcx2011001) Jiangsu Key Laboratory for Photon Manufacturing(No.GZ201111) Jiangsu Provincial Key Laboratory for Interventional Medical Devices(No.Jr1210) Creative Project of Postgraduate of Jiangsu Province(No.CXZZ11_0954)
关键词 micro-nano porous carbon materials expanded graphite activated carbon phenol adsorption KINETICS micro-nano porous carbon materials expanded graphite activated carbon phenol adsorption kinetics
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  • 1XIONG Chunhua ZHU Shan YAO Caiping CHEN Qing.Adsorption behavior of Pd(Ⅱ) from aqueous solutions by D201 resin[J].Rare Metals,2011,30(5):470-476. 被引量:6
  • 2ZHOU Hualei,CHEN Yunfa.Effect of acidic surface functional groups on Cr(Ⅵ) removal by activated carbon from aqueous solution[J].Rare Metals,2010,29(3):333-338. 被引量:6
  • 3Chengbao Liu,Zhigang Chen,Xiangle Cheng,Zhenbang Wang,Xiaotao Duan.Preparation and structure analysis of expanded graphite-based composites made by phosphoric acid activation[J].Journal of Porous Materials.2010(4)
  • 4Rengaraj S,Seung-Hyeon M,Sivabalan R,et al.Agricultural solid waste for the removal of organics: adsorption of phenol from water and wastewater by palm seed coat activated carbon[].Waste Management.2002
  • 5Reddad Z,Gerente C,Andres Y,et al.Adsorption of several metal ions onto a low-cost biosorbent: kinetic and equilibrium studies[].Environmental Sciences.2002
  • 6Pan Bingcai,Xiong Ying,Li Aimin,et al.Adsorption of aromatic acids on an aminated hypercrosslinked macroporous polymer[].Reactive and Functional Polymers.2002
  • 7Ho YS,Mckay G.The kinetics of sorption of divalent metal ions onto sphagnum moss peat[].Water Research.2000
  • 8WJ.Jr. Weber,J.C. Morris.Kinetics of adsorption on carbon from solution[].J Sanit Engng Div Am Soc Civ Engrs.1963
  • 9G Vazquez,R Alonso,S Freire,J Gonzalez-Alvarez,G Antorrena.Uptake of phenol from aqueous solutions by adsorption in a Pinus pinaster bark packed bed[].Journal of Hazardous Materials.2006
  • 10Liu Chengbao.Preparation of Rxpanded Raphite and its Absorbing Properties for Oil in Waste Water[]..2007

二级参考文献24

  • 1Maiyalagan T. and Scott K., Performance of carbon nanofiber supported Pd-Ni catalysts for electro-oxidation of ethanol in alkaline medium, J. Power Sources, 2010, 195 (16): 5246.
  • 2Razi F., Iraji Z.A., and Rahimi F., Investigation of hydrogen sensing properties and aging effects of Schottky like Pd/porous Si, Sens. Actuators B, 2010, 146 (1): 53.
  • 3Poizot P., Jouikov V., and Simonet J., Glassy carbon modified by a silverpalladium alloy: cheap and convenient cathodes for the selective reductive homocoupling of alkyl iodides, Tetrahedron Lett., 2009, 50 (7): 822.
  • 4Rao C.R.M. and Reddi G.S., Platinum group metals (PGM) occurrence, use and recent trends in their determination, Trends Anal. Chem., 2000, 19 (9): 565.
  • 5Simonet J., Alkyl iodides as vectors for the facile coverage of electrified conductors by palladium nano-particles, Electrochem. Commun., 2009, 11 (1): 134.
  • 6Batten J.A., Ciner C., and Lucey B.M., The macroeconomic determinants of volatility in precious metals markets, Resour. Policy, 2010, 35 (2): 65.
  • 7Gaita R. and Al-Bazi J.S., An ion-exchange method for selective separation of palladium, platinum and rhodium from solutions obtained by leaching automotive catalytic-converters, Talanta, 1995, 42 (2): 249.
  • 8Lee J.Y., Raju B., Kurnar B.N., Kumar J.R., Park H.K., and Reddy B. R., Solvent extraction separation and recovery of palladium and platinum from chloride leach liquors of spent automobile catalyst, Sep. Purif. Technol., 2010, 73 (2): 213.
  • 9Barakat M.A., Mahmoud M.H.H., and Mahrous Y.S., Recovery and separation of palladium from spent catalyst, Appl. Catal. A, 2006, 301 (2): 182.
  • 10Dakshinamoorthy A., Dhami P.S., Naik P.W., Dudwadkar N.L., Munshi S.K., Dey P.K., and Venugopal V., Separation of palladium from high level liquid waste of PUREX origin by solvent extraction and precipitation methods using oximes, Desalination, 2008, 232 (1): 26.

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  • 1谢刚,毛宁,周林成,潘多,李彦锋.改进碳纳米管/聚氨酯复合材料吸附硝基苯[J].环境工程学报,2015,9(3):1117-1123. 被引量:5
  • 2冯欣欣,杜尔登,刘翔,郭迎庆,顾礼明,褚腾飞.碳基材料对污水厂尾水和太湖水体中CDOM的吸附特征[J].环境工程学报,2015,9(4):1534-1540. 被引量:10
  • 3吴勇民,李甫,黄咸雨,胡和兵.含酚废水处理新技术及其发展前景[J].环境科学与管理,2007,32(3):150-153. 被引量:61
  • 4Y.S Ho,G McKay.Pseudo-second order model for sorption processes[J]. Process Biochemistry . 1999 (5)
  • 5K.Y. Foo,B.H. Hameed.Insights into the modeling of adsorption isotherm systems[J]. Chemical Engineering Journal . 2009 (1)
  • 6Tsai W T, Chen H R. Adsorption kinetics of herbicide paraquat in aqueous solution onto a low-cost adsorbent, swine-manure- derived biochar [ J ]. International Journal of Environmental Science & Technology, 2013, 10(6) : 1349-1356.
  • 7Elan F, Sun B B, Song Z G, et al. Physicochemical properties of herb-residue biochar and its sorption to ionizable antibiotic sulfamethoxazole [ J ]. Chemical Engineering Journal, 2014, 248 : 128-134.
  • 8Ahmad M, Lee S S, Rajapaksha A U, et al. Trichloroethylene adsorption by pine needle biochars produced at various pyrolysis temperatures [ J ]. Bioresouree Technology, 2013, 143: 615- 622.
  • 9Tan X F, Liu Y G, Zeng G M, et al. Application of biochar for the removal of pollutants from aqueous solutions [ J ]. Chemosphere, 2015, 125: 70-85.
  • 10Chen Z M, Chen B L, Chiou C T. Fast and slow rates of naphthalene sorptinn to bioehars produced at different temperatures [ J]. Environmental Science & Technology, 2012, 46(20) : 11104-11111.

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