生物质类材料对酸性品红的吸附研究
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摘要
目前,印染废水排放量大,污染严重,直接威胁到人类的生产生活,因此印染废水的处理一直是环境科学与工程领域的研究重点。本研究选用花生壳、小麦秸秆、稻草秸秆以及玉米秸秆作为生物质类吸附剂材料,采用粉碎、碳化、改性和碳化并改性四类处理方式制备吸附剂,用于对溶液中酸性品红的吸附研究。在吸附单因子最优化条件下,结合模型初步分析吸附过程的吸附动力学、等温吸附特征以及吸附热力学,并对吸附过程机理进行了一定探讨。
     (1)生物质原材料对酸性品红的吸附研究
     论文中对四种生物质材料吸附酸性品红的单因子条件进行了系统研究,其最佳吸附条件为:花生壳、小麦秸秆、稻草秸秆和玉米秸秆的最佳pH分别为1,2,1,2,吸附时间分别为8h,8h,8h,12h,最佳投加量均为0.6g,在O.1-0.3mol/L的NaCl浓度范围,离子强度误差在12.33%-15.99%之间;对四种吸附剂对酸性品红的吸附过程进行分析,符合准一级动力学方程,拟合相关系数R2为0.990,0.974,0.869,0.925,吸附速率常数k1在0.176-0.339之间;研究该体系在283K、303K、323K温度下的吸附等温线,四种体系与Langmuir模型、Freundlich模型和Tempkin模型的拟合相关度均较好,相关系数均达到了0.900以上,根据Langmuir理论,常温(10℃)条件下,四种生物质材料的理论吸附量分别21.592mg/g,11.524mg/g,8.119mg/g,24.399mg/g;吸附热力学研究结果表明生物质材料对酸性品红的吸附为一自发、放热过程。
     (2)生物质碳化材料对酸性品红的吸附研究
     论文中对四种碳化材料吸附酸性品红的单因子进行了系统研究,其最佳吸附条件为:花生壳炭黑、小麦秸秆炭黑、稻草秸秆炭黑和玉米秸秆炭黑的最佳pH分别为1,1,2,2,吸附时间分别为10h,10h,8h,10h时可达吸附平衡,最佳投加量均为0.3g,碳化温度为750℃,在0.1-0.3mol/L的NaCl浓度范围,离子强度误差在6.78%-12.47%之间;四类碳化材料对酸性品红的吸附主要符合准二级动力学,拟合相关系数R2为0.993,0.995,0.974,0.956,吸附速率k2在0.013-0.046之间;等温吸附研究结果表明,四类碳化材料对酸性品红的吸附以多层吸附为主,等温吸附主要符合Freundlich方程和Tempkin方程;吸附热力学研究结果表明生物质碳化材料对酸性品红的吸附为一自发、吸热过程。
     (3)生物质改性材料对酸性品红的吸附研究
     氯化锌改性并微波活化制备改性材料。论文中对四种碳化材料吸附酸性品红的单因子进行了系统研究,其最佳吸附条件为:改性花生壳、改性小麦秸秆、改性稻草秸秆和改性玉米秸秆的最佳pH分别为1,1,1,2,吸附时间分别为12h,12h,10h,12h时可达吸附平衡,最佳投加量均为0.1g,在0.1-0.3mol/L的NaCl浓度范围,离子强度误差范围为8.48%-12.11%;吸附动力学研究表明,准一级动力学、准二级动力学一级颗粒内扩散模型均能很好的拟合改性小麦秸秆和改性稻草秸秆的吸附动力学过程,改性花生壳和改性玉米秸秆分别符合准二级动力学和准一级动力学方程;等温吸附研究结果表明,生物质类改性材料对酸性品红的吸附以多层吸附为主,等温吸附主要符合Freundlich方程和Tempkin方程;吸附热力学研究结果表明生物质碳化材料对酸性品红的吸附为一自发、放热过程。
     (4)生物质碳化改性材料对酸性品红的吸附研究
     lmol/L磷酸改性450℃碳化材料。论文中对四种碳化材料吸附酸性品红的单因子进行了系统研究,其最佳吸附条件为:改性花生壳炭黑、改性小麦秸秆炭黑、改性稻草秸秆炭黑以及改性玉米秸秆炭黑的最佳pH分别为1,1,1,1,吸附时间分别为6h,6h,8h,6h时可达吸附平衡,最佳投加量均为O.1g,在0.1-0.3mol/L的NaCl浓度范围,离子强度误差在7.26%-11.83%之间;吸附动力学研究表现出一致趋势,模型拟合分析均符合准二级动力学,拟合相关度均在0.972以上,吸附速率常数k2在0.017-0.030之间;等温吸附研究结果表明,生物质类碳化改性材料低温条件下吸附特征表现出极不规范的特点,在323K时对酸性品红的吸附以多层吸附为主,等温吸附主要符合Freundlich方程和Tempkin方程;吸附热力学研究结果表明生物质碳化材料对酸性品红的吸附为一自发、吸热过程。
At present, the dye wastewater had a serious pollution and it had a direct threat to the human production and life. So the dye wastewater treatment had been the focus research in the field of environmental science and engineering. In this paper, peanut shells, wheat straws, rice straws and corn straws were used as biomass raw materials to absorb acid fuchsin. There were four kinds of way (crushing, carbonization, modification, carbonization and modification) was used to deal with the raw materials. Under the condition of best single factors, combining with dynamics model, Isothermal adsorption model and thermodynamics model to analysis the adsorption mechanism.
     (1) Study on the adsorption of acidic with biomass
     Peanut shells, wheat straws, rice straws and corn straws adsorbing acid fuchsin balance when the pH were1,2,1,2and the time were8h,8h,8h,12h, The best dosing quantity was0.6g, In0.1to0.3mol/L NaCl concentration range, ionic strength error was between12.33%-15.99%; Under the best condition, the behavior of raw biomass materials adsorbing acid fuchsin meet first-order kinetics model, fitting correlation coefficient R2was0.990,0.974,0.869,0.925, and the adsorption rate constant k1were between0.176-0.339; Bring the test data into model, the results showed that the fitting correlation of Langmuir model, Freundlich model and Tempkin model were quit good when the temperature was283K、303K、323K in part, correlation coefficients were reached above0.900, according to the Langmuir theory, under the condition of normal temperature (10℃), the adsorption theory of four kinds of biomass material quantity were21.592mg/g, respectively,11.524mg/g and8.119mg/g and24.399mg/g; Adsorption thermodynamics study results showed that the biomass material of acid fuchsin adsorption was a spontaneous and exothermic process.
     (2) Study on the adsorption of acidic with carbonized materials
     Peanut shells carbon, wheat straws carbon, rice straws carbon and corn straws carbon adsorbing acid fuchsin balance when the pH were1,1,2,2and the time were10h,10h,8h,10h, The best dosing quantity was0.3g, In0.1to0.3mol/L NaCl concentration range, ionic strength error was between6.78%-12.47%;750℃carbonized materials adsorb acid fuchsin in the condition of best factors, four types of carbide material for adsorption of acid fuchsin was in line with the quasi secondary dynamics, the fitting correlation coefficient R2were0.993,0.995,0.974,0.956, and the adsorption rate k2was between0.013-0.046; Isothermal adsorption results indicated that, with the adsorption of acid fuchsin on four types of carbide material was given priority to with multilayer adsorption, isothermal adsorption mainly accorded with the Freundlich equation and Tempkin equation; Adsorption thermodynamics research results show that the biomass carbon materials of acid fuchsin adsorption was a spontaneous and endothermic process.
     (3) Study on the adsorption of acidic with modified materials
     The modified materials were perpetrated with using ZnCl2as modified agents, and microwave was used to activate the adsorbent. Modified peanut shells, modified wheat straws, modified rice straws and modified corn straws adsorbing acid fuchsin balance when the pH were1,1,1,2and the time were12h,12h,10h,12h, The best dosing quantity was0.1g, In0.1to0.3mol/L NaCl concentration range, ionic strength error was between8.48-12.11%; The results showed that a modified material was multilayer adsorption, and Isothermal adsorption main accord with Freundlich model and Tempkin model; the three dynamics models in this study all can describe the modified wheat and rice straws' adsorption behavior, modified peanut shells and modified corn straws meet both first-order and second-order kinetics equation, The dynamics parameters indicated that this modified way improved the adsorption ability of wheat straws and rice straws a lot. Adsorption thermodynamics study results showed that the biomass material of acid fuchsin adsorption was a spontaneous and exothermic process.
     (4) Study on the adsorption of acidic with modified carbonized materials
     The450℃biomass carbon was modified by1mol/L H3PO4, which were used as adsorbent to deal with acid fuchsin. Modified peanut shells carbon, modified wheat straws carbon, modified rice straws carbon and modified corn straws carbon adsorbing acid fuchsin balance when the pH were1,1,1,1and the time were6h,6h,8h,6h, The best dosing quantity was0.1g, in0.1to0.3mol/L NaCl concentration range, ionic strength error was between7.26%-11.83%; The dynamics showed a consistent trend, second-order kinetics equation was suitable, fitting correlation were above0.972, the adsorption rate constant k2was between0.017to0.030; The results showed that modified biomass carbon presented different adsorption characteristics in low temperature condition. When the temperature was323K, multilayer adsorption was the main adsorption behavior, Isothermal adsorption meet Freundlich model and Tempkin model; Adsorption thermodynamics research results showed that the biomass carbon materials of acid fuchsin adsorption are a spontaneous and endothermic process.
引文
[1]刘昌明.21世纪中国水资源若干问题的讨论[J].水利水电技术,2002,33(1):15-19
    [2]易怀昌.壳聚糖及其改性微球对酸性染料的吸附性能研究[D].中国海洋大学研究生学位论文,2009
    [3]刘昌明,曹英杰.我国水污染状况及其对人类健康的影响与主要对策[J].科学对社会的影响,2009,(2):16-22
    [4]Yuxing Wong, Jian Yu. Laccase-catalyzed depolarization of synthetic dyes[J]. Water Research, 1999,33:3512~3520
    [5]Yuzhu Fu, T Viraraghavan. Fungal depolarization of dye wastewaters:a review [J]. Bioresource Technology,2001,79:251-262
    [6]任海萍,吴柳明.纳米零价铁对酸性品红的脱除行为[J].中南大学学报(自然科学版),2008,39(2):307-310
    [7]岳钦艳,曹先艳,高宝玉等.改性粉煤灰及其处理废水的机理[J].环境污染与防治,2005,27(1):67-69
    [8]夏朝辉,张慧俐,张巍松等.紫外光Fenton试剂法处理染料废水研究[J].河南科学,2005,23(2):302-305
    [9]耿锋,戴海平.膜法染料废水处理及膜污染的防治[J].染整技术,2005,27(8):26-29
    [10]宋智,申泽星,王飞羽等.微电解催化处理染料废水研究[J].昆明理工大学学报:理工版,2007,33(2):83-85
    [11]高廷耀,顾国维.水污染控制工程下册[M].高等教育出版社,1999:226-227
    [12]Khattri S D. Colour removal from dye wastewater using sugar earle as all adsorbent [J]. Absorption Science Technology,2000,12(4):269~282
    [13]谭民强.轻工纺织化纤环境影响评价工程师职业资格登记培训教材[M].中国环境科学出版社,2005:225-234
    [14]Joanne B, Jason J P, Chris A E A.Treatment and decolorisation of dyes in ananaerobic baffled reactor [J]. Journal of Enviromental Engineering,2000,10(2):1026~1032
    [15]Vimonse V, Lei S, Jin B, Chow CWK, Saint C, Kinetc study and equilibrium isotherm analysis of Congo Red adsorption by clay materials. Chemical Engineering Journal,2009,148(2/3):354~ 364
    [16]龚正君,周文波,陈钰.花生壳活性炭对水中荧光素钠的吸附及动力学[J].环境工程学报,2013,7(1):221-225
    [17]彭晓文,杨迎新.膜分离技术在印染废水处理中的应用[J].江西化工,2003,(1):21-23
    [18]Vera Golob, Aleksandra Vinder. Efficiency of the coagulation/flocculation method for the treatment of dye bath effluents[J]. Dyes and Pigments,2005,67(2):93~97
    [19]Yong jun Wu, Li jun Zhang, Cong li Gao etal. Adsorption of Copper Ions and Methylene Blue in a Single and Binary System on Wheat Straw [J]. Journal of Chemical & Engineering Data,2009, 54:3229~3234
    [20]Ayyasamy Thevannan, Rubeena Mungroo, Catherine Hui Niu. Biosorption of nickel with barley straw [J]. Bioresource Technology 2010,101:1776~1780
    [21]N. V. Farinella, G. D. Matos, M. A. Z. Arruda. Grape bagasse as a potential biosorbent of metals in effluent treatments [J]. Bioresource Technology,2007,98:1940~1946
    [22]Anwar Ahmad, Rumana Ghufran, Wan Mohd. Faizal. Cd(Ⅱ), Pb(Ⅱ) and Zn(Ⅱ) Removal from Contaminated Water by Biosorption Using Activated Sludge Biomass [J]. Clean,2010,38:153~ 158
    [23]Chen Yu, Gong Zhengjun, Zhang Zhi-peng, et al. Adsorption of Cr(IV) from Aqueous Solution using Peanut Shell [J]. The 2nd Conference on Enivronmental Science and Information Application Technology,2010,33:530~533
    [24]黄川,刘元元,罗宇等.印染工业废水处理的研究现状[J].重庆大学学报(自然科学版),2001,24(6):139-142
    [25]龚铭祖.纺织工业废水治理[M].中国环境科学出版社,1990:150-156
    [26]Vilar V J P,Botelho C M S,Boaventura R A R,Influence of pH,ionic strength and temperature on lead biosorption by gelidium and agarextraction algal waste [J].Process Biochem.2005,40(10): 3267-3275
    [27]张晓敏,宗汉兴,汪德耀等.光催化氧化降解活性艳红X-3B模拟染料废水试验[J].水资源保护,2006,22(4):68-70
    [28]赵录庆,姜聚慧,郭强等.UV/Fenton试剂法处理酸性染料废水的研究[J].河南师范大学学报,2002,30(2):57-59
    [29]杨书铭,黄长盾.纺织印染工业废水治理技术[M].北京:化学工业出版社,2002:123-125
    [30]黄川,刘元元,罗宇等.印染工业废水处理的研究现状[J].重庆大学学报(自然科学版),2001,24(6):139-142
    [31]Emad N, Stephen J, Gavin M. etal. Adsorption of basic dyes from aqueous solution onto activated carbons[J]. Chemical Engineering Journal,2008,135:174-184
    [32]Yahya S, Musa I, Amjad H. etal. Effect of solution pH ionic strength and temperature on adsorption behavior of reactive dyes on activated carbon[J]. Dyes and Pigments,2008,77(1): 16-23
    [33]解建坤,岳钦艳,于慧等.污泥活性炭对活性艳红K-2BP染料的吸附特性研究[J].山东大学学报(理学版),2007,42(3):64-70
    [34]梁霞,王学江.活性炭改性方法及其在水处理中的应用[J].水处理技术,2011,37(8):1-5
    [35]Baskaralingam P, Pulikesi M, Elango D. etal. Adsorption for acid dye onto organobentonite[J]. Journal of Hazardous Materials,2006,128(2-3):138-144
    [36]叶玲,肖子敬,黄继泰等.改性膨润土在红色染液脱色处理中的应用[J].华侨大学学报(自然科学版),2000,21(4):366-370
    [37]冀静平,祝万鹏,孙欣等.膨润土的改性及对染料废水的处理研究[J].中国给水排水,1998,14(4):7-10
    [38]Wang C C, Juang L C, Hsu T C. etal. Adsorption of basic dyes onto montmorillonite[J]. Journal of Colloid and Interface Science,2004,273(1):80-86
    [39]弓晓峰,张文涛,崔秀丽等.海泡石在废水处理中的应用研究[J].环境污染治理技术与设备,2003,4(9):27-30
    [40]沈丽娜,完颜华,廖志成等.海绵铁对印染废水脱色研究[J].环境科学与技术,2004,27(6):18-20
    [41]李志平,欧阳玉祝,麻成金等.大孔树脂吸附法处理印染废水的研究[J].广西民族学院学报(自然科学版),2005,11(2):94-97
    [42]Yu Y, Zhuang Y Y, Wang Z H. etal. Adsorption of water~soluble dyes onto modified resin[J]. Chemosphere,2004,54(3):425-430
    [43]Mckay G, Blair H S, Gardner J. The adsorption of dyes in chitin Ⅰ. Equilibrium studies[J]. Journal of Applied Polymer Science,1982,27(1):3043-3057
    [44]Mckay G, Blair H S, Gardner J. The adsorption of dyes in chitin Ⅱ.External mass transfer processes[J]. Journal of Applied Polymer Science,1982,27(1):4251-4261
    [45]Mckay G, Blair H S, Gardner J. The adsorption of dyes in chitin ⅢIntraparticle diffusion processes[J]. Journal of Applied Polymer Science,1983,28(1):1767-1778
    [46]Wong Y C, Szeto Y S, Cheung W H, etal. Adsorption of acid dyes on chitosan-equilibrium isotherm analyses[J]. Process Biochemistry,2004,39(6):693-702
    [47]林静雯,索志强,王冠等.改性壳聚糖絮凝剂处理印染废水的研究[J].环境保护科学,2005,31(129):16-18
    [48]Annadurai G, Ling L Y, Lee J F. Adsorption of reactive dye from an aqueous solution by chitosan: isotherm, kinetic and thermodynamic analysis[J]. Journal of Hazardous Materials,2008,152(1): 337-346
    [49]朱启忠,赵亮云,赵宏等.壳聚糖对酸性染料的吸附性能[J].资源开发与市场,2006,22(2):101-102
    [50]Sud D., Mahajan G., Kaur M.P.Agricultural waste material as potential adsorbent for sequestering heavy metal ions from aqueous solution-A review[J]. Bioresour Technology,2008,99:6017~ 6027
    [51]田缓,张晓昱.生物质对染料废水的吸附脱色研究[J].环境与健康学术研讨会论文集,2007:325-327
    [52]王开峰,彭娜.非活体生物质对水中活性艳红X~3B的吸附研究[J].环境工程学报,2010,14(2):309-314
    [53]Ozer D, Dursu N G. Ozer A. methylene blue adsorption from aqueous solution by dehydtated peanut hull [J]. Journal of Hazardous Material,2007,144(1/2):171 ~ 179
    [54]李山,张丽娜,樊君等.环氧氯丙烷改性花生壳吸附水中次甲基蓝的研究[J].染料与染色,2008,45(2):49-51
    [55]程祥珍,肖加余,谢征芳等.活性炭纤维研究与应用进展[J]材料科学与工程,2003,21(2):283-288
    [56]尹炳奎,朱石清,朱南文等.生物质活性炭的制备及其染料废水中的应用[J].环境污染与防治,2006,28(8):608-610
    [57]吴成,张晓丽,李关宾等.黑碳制备的不同热解温度对其吸附菲的影响[J].中国环境科学,2007,27(1):125-128
    [58]俞力家,孙保帅,王天贵等.花生壳制备活性炭及其去除六价铬研究[J].化学工程师,2009,8:8-12
    [59]孙勇,李佐虎.利用黑液木质素制备活性炭的研究进展[J].中国纸业,2008,28(3):62-65
    [60]O'Connell D. W., Birkinshaw C, O'Dwyer T.F. Heavy metal adsorbents prepared from the modification of cellulose:Areview[J]. Bioresour Technology,2008,99:6709~6724
    [61]谭婷,李秀成.胺基稻草纤维的制备及对电镀废水中Fe3+、Ni2+、Cu2+、Zn2+的吸附[J].现代化工,2011,31(6):45-47
    [62]Vaughan T., Seo C. W., Marshall W. E. Removal of selected metal ions from aqueous solution using modified corncobs[J]. Bioresour Technology,2001,78:133 ~139
    [63]Navarro R.R., Sumi K., Fujii N., etal. Mercury removal from wastewater using porous cellulose carrier modified with polyethyleneimine[J]. Water Resarch,1996,30(10):2488~2494
    [64]Wang J, Pan Z J, Zhang Z H, etal. The investigation on ultrasonic degradation of acid fushine in the presence of ordinary and nanometer rutile TiO2 and the comparison of their sonocatalytic activities[J]. Dyes and Pigments,2007,74(3):525~530
    [65]赵玉翠,石建稳,郑经堂等.纳米TiO2的制备、表征及光催化降解酸性品红[J].应用化工,2007,6(10):993-997
    [66]徐蕾,宋如翠.H2O2与UV/TiO2协同体系光催化降解酸性品红的研究[J].吉林工程技术师范学院学报,2008,24(11):82-84
    [67]Hoffmann A J, Carrawy E R, Hoffmann M R. potocatalytic production of H2O2 organic peroxides on quantum-sized semiconductor colloid[J]. Environmental Science Technology,1994,28(5): 776-785
    [68]孙润录,肖寒,陈晓东等.电动降解处理酸性品红染料废水的研究[J].应用化工,2009,38(10):1488-1491
    [69]汤敏,任建敏.钠基膨润土吸附酸性品红的动力学与热力学[J].重庆工商大学学报(自然科学版),2010,27(4):373-376
    [70]Ayarif, Srasrae, Trabelsi Ayadim. Retention of lead from an aqueous solution by use of bentonite as adsorbent for reducing leachi ng from industrial effluents [J]. Desalination,2007,206:270~ 278
    [71]张志鹏,孙彩云,龚正君,陈钰,王东梅.新型吸附剂吸附重金属的研究进展[C].四川省第十一次环境监测学术交流会论文集,2010,180-182
    [72]Yuxing Wong, Jian Yu. Laccase-catalyzed depolarization of synthetic dyes[J]. Water Research, 1999,33:3512~3520
    [73]Yuzhu Fu, T Viraraghavan. Fungal depolarization of dye wastewaters:a review [J]. Bioresource Technology,2001,79:251~262
    [74]任海萍,吴柳明.纳米零价铁对酸性品红的脱除行为[J].中南大学学报(自然科学版),2008,39(2):307-310
    [75]岳钦艳,曹先艳,高宝玉等.改性粉煤灰及其处理废水的机理[J].环境污染与防治,2005,27(1):67-69.
    [76]夏朝辉,张慧俐,张巍松等.紫外光Fenton试剂法处理染料废水研究[J].河南科学,2005,23(2):302-305.
    [77]耿锋,戴海平.膜法染料废水处理及膜污染的防治[J].染整技术,2005,27(8):26-29.
    [78]宋智,申泽星,王飞羽等.微电解催化处理染料废水研究[J].昆明理工大学学报:理工版,2007,33(2):83-85
    [79]张小璇.染料废水的活性炭吸附及其热再生研究[D].厦门大学硕士学位论文,2005
    [80]刘江国,陈玉成,李杰霞等.改性玉米秸秆对Cu2+废水的吸附[J].工业水处理,2010,58(6):45-52
    [81]周丕严.H3PO4、KOH活化法桐壳基活性炭的制备及其吸附性能的研究[D].福建师范大学硕士学位论文,2009
    [82]Ho, Y.S, Ofomaja, A.E.. biosorption thermodynamics of cadmium on coconut coprameal as biosorbent[J]. Biochemical Engineering Journal,2006, (30):117~123
    [83]Selvaraj R, Younghun K, Cheol K, J. Removal of copper from aqueous solution by aminated and protonated mesoporous aluminas:kinetics and equilibrium[J]. Jouranl of Colloid and Interface Science,2004,273(1):14~21
    [84]Cheung C W, Porter J F, Mckay G.. Sorption kinetics for the removal of copper and zinc from effluents using bone char[J]. Separation and Purificaton Technology,2000,19(12):55~64
    [85]Ho, Y. S,Ng J C Y, McKayG. Kineties of Pollutant sorption by biosorbents:review[J]. Separation and Purification Methods,2000,29(2):189~232
    [86]Nathalie C, Richard G, Eric D. Adsorption of Cu(Ⅱ) and Pb(Ⅱ) onto a grafteds iliea:isotherms and kinetie models[J]. Water Researeh,2003,37(13):3079~3086
    [87]Akhtar M, Bhanger M, Iqbal S, Hasany MS. Sorption potential of rice husk for the removal of 2,4-diehlorophenol from aqueous solutions:Kinetic and thermodynamic investigations[J]. Journal of Hazardous Materials,2006,128(13):44~45
    [88]Febrianto J., Kosasih A.N., Sunarso J., etal. Equilibrium and kinetic studies in adsorption of heavy metals using biosorbent:a summary of recent studies[J]. Journal of Hazardous Materials, 2009,162:616-645
    [89]Gupta S., Babu B.V. Utilization of waste product(tamarind seeds)for the removal of Cr (Ⅵ)from aqueous solutions:Equilibrium,kinetics,and regeneration studies[J]. Journal of Environmental Management,2009,90:3013~3022
    [90]Aksu Z., Acikel U., Kutsal T, Investigation of simultaneous biosorption of copper(Ⅱ) and chromium(VI)on dried chlorella vulgaris from binary metal mixtures application of multicomponent adsorption isotherms[J]. Science Technology,1999,34:501 ~524
    [91]Li Q., Chai L.,Yang Z., etal. Kinetic,thermodynamics of Pb(II)adsorption onto modified spent grain from aqueous solution[J]. Applied Surface Science,2009,255(7):4298~4303
    [92]Huang PM. Soil mineral-organic matter-microorganism interactions:Fundamentals and impacts [J]. Advance in Agronomy,2004,82:391~472
    [93]Yu G, Saha UK, kozak LM, Huang PM. Kinetics of cadmium adsorption on aluminum precipitation products formed under the influence of ternate [J]. Geochimica et Cosmochimica Acta,2006,70(20):5134-5145
    [94]林玉锁Langmuir, Temkin和Freundlich方程应用于土壤吸附锌的比较.土壤,1994,26(5):269-272
    [95]Kinniburgh D G., General purpose adsorption isotherms [J]. Environmental Sicence Technology, 1986,20(9):895~904
    [96]龚正君,周文波,陈钰.活性炭纤维对水中酸性染料的吸附研究[J].工业水处理,2012,32(9):24-28
    [97]Kostura B, Kulveitova H, Juraj L. Blast furnace slaga as sorbents of phosphate from water solutions[J]. Water Resarch,2005,39:795~1802
    [98]Ozacar M. Equilibrium and kinetic modeling of adsorption of phosphorus on calcined alunite[J]. Adsorption,2003,9:25~132
    [99]赵桂瑜,周琪.页岩陶粒对水体中磷的吸附作用及动力学[J].环境污染与防治,2007,29(3):182-185
    [100]Kumar K V. Optimum sorption isotherm by linear and non-linear methods for malachite green onto lemon peels [J]. Dyes and Pigments,2007,74(3):595~597
    [101]Ho Y S. Selection of optimum sorption isotherm [J]. Carbon,2004,42(10):2115~2116
    [102]Vimonses V, Lei S, Jin B, Chow CWK, Saint C. Kinetic study and equilibrium isotherm analysis of Congo Red adsorption by clay materials[J]. Chemical Engineering Journal,2009,148(2/3): 354~364
    [103]KyriakoPoulosG, DouliaD, AnagnostoPoulosE.Adsorption of Pestieides on porous polymeric adsorbents [J].Chemieal Engineering Seienee.2005, (60):1177~1186
    [104]Longhinotti E, Pozza F, Furlan L. etal. Adsorption of Anionic Dyes on the Biopolymer Chitin [J]. Journal of the Chemical Society,1998,9:435~440
    [105]Yuh-Shan Ho. Second-order kinetic model for the sorption of cadmium onto tree fern:A comparison of linear and non-linear methods [J]. Water Resarch,2006,40:119~125
    [106]Wang Y, Gao B., Wen Y, etal. Preparation and utilization of wheat straw anionic sorbent for the removal of nitrate in aqueous solution[J]. Journal of Environmental Sciences,2007,19,1305~ 1310
    [107]赵辉,廖雄.改性农作废弃物对含铬重金属废水的吸附处理[J].应用化学,2011,40(10):1741-1744
    [108]Prasad S., Singh A,. Joshi H.C. Ehanol as an alterative fuel from agricultrial, industrial and urban residues[J]. Resources Conservation and Recycling,2007,50(1):1~39
    [109]易怀昌,孟范平,宫艳艳等.壳聚糖对酸性染料的吸附性能研究[J].化工环保,2009,29(2):114-118
    [110]Nunn T R, Howard J B, Longwell J P. Product compositions and kinetics in the rapid pyrolysis of sweet gum hardwood[J]. Engineering Chemistry Process,1985,24(3):836~844
    [111]Satoshi K, Hidetoshi S. Estimation of Point of zero charge for activated carbon treated with atlnospheric pressure non-thermal oxygen plasmas[J]. Thin Solid Films,2006,507(1):327~330
    [112]Chik A, Donghee P, Seung H W, etal. Removal of cationie heavy metal from aqueous solution by activated carbon impregnated with anionie surfactants[J]. Journal of Hazardous Materials,2009, 164(2-3):1130~1136
    [113]Ofomaja A.E., Ho Y. Effect of pH on cadmium biosorption by coconut copra meal[J]. Journal of Hazardous Materials,2007,139:356~362
    [114]Pino G.H., Mesquita L. M.S., Torem M. L. G. A. S. Pinto. Biosorption of cadmiu by green coconut shell powder[J]. Miner Enginerring,2006,19:380~387
    [115]Salem Z., Allia K. Cadmium biosorption on vegetal biomass[J]. International Journal Chemical Reactor Engineering,2008,6:1-9
    [116]Caturla F, Molina-Sabio M, Rodriguez-Noso F. Preparation of activated carbon by chemical activation with ZnCl2[J]. Carbon,1991,29(7):999~1007
    [117]Guo J L, Aik C G. Preparation of activated carbon from oil-palm-stone char by microwave-induced carbons dioxide activation [J]. Carbon,2000,38(4):1985-1993

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