改性核桃壳炭基吸附材料对Cu2+的吸附性能研究

何荔枝1, 王美城1, 姚思聪1, 邹宏菁2, 左小利2, 陈尧1*

化工新型材料 ›› 2020, Vol. 48 ›› Issue (2) : 173 -178.

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化工新型材料 ›› 2020, Vol. 48 ›› Issue (2) : 173-178.
科学研究

改性核桃壳炭基吸附材料对Cu2+的吸附性能研究

    何荔枝1, 王美城1, 姚思聪1, 邹宏菁2, 左小利2, 陈尧1*
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Removal of Cu2+ from aqueous solution using walnut shell-based activated carbon with pyrolusite modification

  • He Lizhi1, Wang Meicheng1, Yao Sicong1, Zou Hongjing2, Zuo Xiaoli2, Chen Yao1
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摘要

利用核桃壳作为原料制备出普通核桃壳活性炭 (WS)和软锰矿改性核桃壳活性炭 (WSMn),探讨了WSMn中改性剂软锰矿的最佳添加量,并对2种活性炭进行了表面特性分析,研究了2种活性炭对溶液中Cu2+的吸附特性。结果表明:当软锰矿添加量为1% (质量分数)时,WSMn的孔隙结构更加发达,以微孔和中孔为主,比表面积为1433.13m2/g,总孔容为0.9083cm3/g,比表面积比未添加软锰矿的核桃壳活性炭提高了27.16%。室温下,当活性炭投加量为6g/L,Cu2+溶液质量浓度为200mg/L,溶液初始pH=4.3,吸附平衡时间为1h时,WSMn和WS对溶液中Cu2+的去除率分别为95.5%和73.67%。准二级动力学方程和Langmuir吸附等温方程能准确地描述2种活性炭对Cu2+的吸附过程。

Abstract

Unmodified (WS) and pyrolusite modified activated carbons (WSMn) were developed from walnut shell.The optimized addition of pyrolusite in the activated carbons production was also discussed.Analysis of surface characteristics and Cu2+ adsorption performance in the solution for both activated carbons were carried out.The BET surface area and pore volume of WSMn was up to 1433.13m2/g and 0.9083cm3/g,the BET surface area was 27.16% higher than WS's.Compared with WS,the pore structure of WSMn was more developed with mesopores and micropores.At room temperature,with the 200mg/L Cu2+,pH=4.3,6g/L adsorbent and 60min reaction,the maximum removal rate of Cu2+ could be 95.5% and 73.67% for WSMn and WS,respectively.For both activated carbons the adsorption kinetics was fitted well with the pseudo-second order model and the adsorption isotherm followed Langmuir model.

关键词

核桃壳 / 活性炭 / 改性 / 重金属离子吸附

Key words

walnut shell / activated carbon / modification / heavy metal ion-adsorption

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改性核桃壳炭基吸附材料对Cu2+的吸附性能研究[J]. 化工新型材料, 2020, 48(2): 173-178 DOI:

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参考文献

[1] 余琼粉,李明,宁平,等.核桃壳活性炭的制备及其在环境保护中的应用[J].化学工业与工程,2011,28 (6):63-67.
[2] Hamissa A M B,Lodi A,Seffen M,et al.Sorption of Cd (Ⅱ) and Pb (Ⅱ) from aqueous solutions onto agave Americana fibers[J].Chemical Engineering Journal,2010,159 (1):67-74.
[3] Girodsa P,Dufoura A,Fierrob V,et al.Activated carbons prepared from wood particleboard wastes:characterisation and phenol adsorption capacities[J].Journal of Hazardous Materials,2009,166 (1):491-501.
[4] 赖波,周岳溪,杨平.生物活性炭法处理ABS树脂生产废水[J].中国环境科学,2012,32 (2):254-259.
[5] Zaini M A A,Okayama R,Machida M.Adsorption of aqueous metal ions on cattle-manure-compost based activated carbons[J].Journal of Hazardous Materials,2009,170 (2/3):1119-1124.
[6] 高翔,鲁安怀,郑辙,等.锰的氧化物和氢氧化物在污染水体净化中的应用研究现状[J].矿物岩石,2002,22 (1):77-81.
[7] 蒋文勇.软锰矿在环境污染治理中的应用[J].四川化工,2008,11 (4):48-51.
[8] 刘琛,蒋文举,王娟,等.软锰矿-污泥基活性炭对活性艳红X-3B的吸附特性研究[J].林产化学与工业,2009,29 (4):37-40.
[9] 张望,蒋文举,刘琛,等.微波法制备软锰矿-污泥基活性炭的工艺条件及吸附性能研究[J].四川化工,2009,12 (1):41-45.
[10] 陈维芳,程明涛,张道方,等.有机酸-铁改性活性炭去除饮用水中的砷[J].中国环境科学,2011,31 (6):910-915.
[11] Dimit rova S V.Metal sorption on blust-furnance slag[J].Water Res,1996,30:228-332.
[12] Vaghetti J C P,Lima E C,Royer B,et al.Pecan nutshell as biosorbent to remove Cu (Ⅱ),Mn (Ⅱ) and Pb (Ⅱ) from aqueous solutions[J].Journal of Hazardous Materials,2009,162 (1):270-280.
[13] Basci N,Kocadagistan E,Kocadagistan B.Biosorption of Cu (Ⅱ) from aqueous solutions by wheat shells[J].Desalination,2003,164 (2):135-140.
[14] Khan M N,Wahab M F.Characterization of chemically modified corncobs and its application in the removal of metal ions from aqueous solution[J].Journal of Hazardous Materials,2007,141 (1):237-244.
[15] 李雪英,李坤权,乔小朵,等.活化因素对蔗渣基生物质炭中孔结构的影响[J].环境化学,2015,34 (11):2017-2024.
[16] Raposo F,De La Rubia M A,Borja R.Methylene blue number as useful indicator to evaluate the adsorptive capacity of granular activated carbon in batch mode:influence of adsorbate/adsorbent mass ratio and particle size[J].Journal of Hazardous Materials,2009,165 (1/2/3):291-299.
[17] Esposito A,Pagnanelli F,Veglio F.PH-rated equilibria models for biosorption in single metal systems[J].Chemical Engineering Science,2002,57 (3):307-313.
[18] 汪莉,陈尧,蒋文举,等.软锰矿改性污泥活性炭对Cu2+吸附特性的研究[J].环境科学与技术,2011,34 (11):118-121.
[19] Monser L,Adhoum N.Modified activated carbon for the removal of copper,zinc,chromium and cyanide from wastewater[J].Separation and Purification Technology,2002,26 (2):137-146.
[20] Juang R S.Adsorption behavior of reactive dyes from aqueous solution on chitosan[J].Chemical Technology and Biotechnology,1997,70 (4):391-399.
[21] Namasivayam C,Senthilkumar S.Removal of arsenic from aqueous solution using industrial solid waste:adsorption rates and equilibrium studies[J].Ind Eng Chem Research,1998,37 (23):4816-4822.
[22] Ho Y S,MeKay G.Pseudo-second order model for sorption proeesses[J].Process Bioehem,1999,34 (5):451-465.
[23] Ozacar M,SengilⅠA.A kinetic study of metal complex dye sorption onto pine sawdust[J].Proeess Bioehem,2005,40 (2):565-572.
[24] Yang X,AI-Duri B.Kinetic modeling of liquid-phase adsorption of reactive dyes on aetivated carbon[J].Colloid Interface Sei,2005,287 (1):25-34.
[25] Bulut Y,Aydm H.A kinetics and thermodynamics study of methylene blue adsorption on wheat shells[J].Desalination,2006,194 (1/2/3):259-267.
[26] Kannan N,Sundaram M M.Knetics and mechanism of removal of methylene blue by adsorption on various carbons-a comparative study[J].Dyes Pigments,2001,51 (1):25-40.
[27] Ho Y S,McKay G.Kinetic model for lead (Ⅱ) sorption on to peat[J].Adsorpt Sci Technol,1998,16 (4):243-255.
[28] Seredych M,Bandosz T J.Removal of copper on composite sewage sludge/industrial sludge-based adsorbents:the role of surface chemistry[J].Journal of Colloid and Interface Science,2006,302 (2):379-388.
[29] Sharma Y C,Prasad G,Rupainwar D C.Removal of Ni (Ⅱ) from aqueous solutions by sorption[J].International Journal of Environmental Studies,1991,37 (3):183-191.

基金资助

国家青年自然科学基金项目(51208323)

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