天祝褐煤腐植酸对Ni2+离子吸附性能研究

通过FTIR、FR分析了天祝腐植酸吸附重金属Ni2+离子前后的红外光谱、荧光强度的变化,对重金属离子Ni2+进行了吸附性能及机理研究.结果表明:在室温条件下(20℃～ 25℃),吸附最佳pH=6,吸附平衡时间约为5h.符合Freundlich吸附模型,相关系数R=0.9998,特性常数n为2.49.腐植酸对Ni2+有较好的吸附性能,其吸附过程可用Ho准二级反应动力学模型描述.     

H3PO4改性PS-EDTA树脂对水相中Cu2+、Zn2+和Cd2+的吸附性能研究

大孔氯甲基化聚苯乙烯小球先后与乙二胺、2-氯乙酸反应得EDTA型螯合树脂(PS-EDTA),再用磷酸在室温处理得PS-EDTA/P树脂。PS-EDTA/P树脂被用于水相中Cu2+、Zn2+和Cd2+的吸附净化处理,探讨了溶液的pH值、初始金属离子浓度、时间、温度等因素对吸附性能的影响,并研究了其对重金属离子的吸附动力学和热力学。结果表明,PS-EDTA/P树脂对Cu2+和Zn2+的吸附符合Langmuir等温式、对Cd2+的吸附符合Freundlich等温式,准二级吸附动力学方程能够很好地描述3种金属离子在树脂上的吸附动力学行为。同时,PS-EDTA/P树脂对重金属吸附的热力学参数表明,PS-EDTA/P树脂对Cu2+、Zn2+和Cd2+的吸附是一个自发的、吸热的过程。已吸附Cu2+、Zn2+和Cd2+的树脂可以用0.1mol/L HCl解吸,解吸后的树脂对Cu2+、Zn2+和Cd2+仍具有较高的吸附量。     

弱酸性氨基二硫代甲酸酯功能化聚氯乙烯树脂对Hg2+的吸附与脱附性能

以聚氯乙烯为原料依次与四乙烯五胺、CS2和ClCH2COONa反应合成了一种含氮、氧、硫的弱酸性氨基二硫代甲酸酯功能化的聚氯乙烯螯合树脂,树脂的结构经红外分析和元素分析表征。探讨了在不同pH值、Hg2+初始浓度、吸附温度和时间等条件下合成树脂对Hg2+的吸附性能。结果表明,螯合树脂对Hg2+有较快的吸附速率,pH=2.0左右时树脂对Hg2+的吸附效果最好,随着温度的升高吸附量逐渐增大,35 ℃时Hg2+起始浓度为0.01766 mol/L时,树脂对Hg2+的吸附量可达3.330 mmol/g。树脂对Hg2+的吸附符合Langmuir和Freundlich等温式。用0.2 mol/L硝酸-10%硫脲对吸附后的树脂进行洗脱,脱附率达99.2%。     

巯基功能化膨润土吸附Pb2+的动力学和热力学研究

研究了自制巯基功能化膨润土(TFB)对Pb2+的吸附行为,考察了溶液的pH值、离子强度、吸附时间和温度对吸附平衡的影响,并对吸附过程进行了动力学与热力学研究.结果表明,常温下,吸附时间为60min、0.1mol/L的KNO3、pH=6.0、5.0g/L TFB对200mg/L的Pb2+的吸附率达到85.4％以上,TFB对Pb2+的吸附动力学符合准二级动力学方程;TFB对Pb2+的吸附热力学符合Langmuir等温线方程和Dubinin-Radushkevich (D-R)等温线方程,表明吸附主要发生在TFB表面的活性区域,属于单分子层吸附,其吸附平均活化能E在8-16kJ/mol范围内,表明该吸附过程为化学吸附,不同温度下的吸附热力学的吉布斯自由能以及熵变和焓变表明该吸附过程为自发放热反应.     

水稻秸秆的改性及其对重金属Cu2+的吸附

重金属Cu2+可直接或间接危害人体,作为天然吸附剂的农业废弃物因价廉易得、来源广泛、吸附高效等优点备受青睐。本文选用水稻秸秆（RS）为吸附原料,分别经酸、碱改性后得到H2SO4-RS和NaOH-RS,通过FT-IR、SEM和BET对改性前后吸附材料的表面官能团、表观形貌和结构等理化性质进行分析,考察投加量、吸附时间、初始Cu2+浓度和离子强度对吸附效果的影响,并结合吸附动力学、吸附等温线和热力学模型对吸附过程进行探讨。结果表明：改性水稻秸秆对Cu2+达到吸附平衡所需的投加量和时间较之未改性RS大大减少,去除率由42.0%分别提升至85.9%（H2SO4-RS）和90.0%（NaOH-RS）;随初始Cu2+浓度和离子强度的增大,RS的吸附性能显著降低,H2SO4-RS有所降低,而NaOH-RS只是稍有下降,NaOH-RS对150 mg/L含Cu2+溶液的去除率仍达到84.2%,离子强度cNaCl = 0.1 mol/L时去除率维持在86.1%。吸附动力学和吸附等温实验表明水稻秸秆对Cu2+的吸附符合准二级动力学模型和Langmuir吸附等温模型;热力学分析显示,相同温度下RS、H2SO4-RS和NaOH-RS吸附Cu2+过程的ΔG逐渐减小,且改性后两种吸附剂的ΔG均小于0,ΔH由改性前的正值转变为负值,说明水稻秸秆改性后吸附Cu2+的自发性更强,为自发的放热过程。     

乙二胺硅胶复合材料对Zn2+的吸附特性

以γ-氯丙基三氯硅烷为偶联剂,将乙二胺偶合接枝在硅胶表面,合成对锌离子具有吸附作用的乙二胺硅胶复合材料（EDA/SiO2）,考察了Zn2+溶液pH值、初始浓度、吸附温度和吸附时间等因素对复合材料吸附性能的影响。 结果表明,在研究的溶液浓度及温度范围内,Zn2+溶液pH值对EDA/SiO2的吸附量影响显著,吸附的最佳pH值范围在3.0~5.5;Zn2+的吸附平衡数据符合Langmuir吸附模型,热力学数据显示,EDA/SiO2对Zn2+的吸附行为为一吸热且自发进行的过程,升高温度有利于吸附,并对此吸附行为作了解释;吸附动力学数据可用拟二级吸附动力学方程描述,得到的吸附速率常数与溶液初始浓度有关。     

8-羟基喹啉接枝PGMA的合成及对Cd~(2+)的吸附性能

合成了一种带8-羟基喹啉功能基的交联聚甲基丙烯酸缩水甘油酯树脂(HQPGMA),采用红外光谱和热重分析对合成树脂进行了表征。探讨了该合成树脂对Cd2+的静态吸附性能。考察了在不同的温度、Cd2+离子浓度、吸附时间及p H值等条件下,HQPGMA树脂对Cd2+的吸附情况。结果表明,HQPGMA树脂对Cd2+具有良好的吸附作用。当p H值约为4.5时,吸附效果最佳,当Cd2+初始浓度为0.01888mol/L时,其最大吸附量为0.861mmol/g;树脂对Cd2+的吸附过程符合Langmuir和Freundlich等温吸附方程;其吸附动力学与准二级动力学方程拟合的更好;吸附为自发的吸热过程;0.2mol/L HNO3对树脂上吸附的Cd2+的脱附率可达85.7%。     

氨基功能化离子印迹硅胶对Cd2 的吸附行为及机理

研究了氨基功能化离子印迹硅胶对Cd2+的吸附行为及机理,进行了等温吸附模型和吸附动力学的测定和吸附热力学计算。结果表明,饱和吸附量的实验值为30.7mg/g;20min即可达到吸附平衡;等温吸附曲线符合Langmuir等温吸附模型,吸附过程以单层吸附为主;Cd2+的吸附动力学数据均符合准二级反应动力学模型;反应的吉布斯自由能为负值,焓变为23.01k J/mol,熵变为104.1J/mol·K,说明吸附是一个吸热的自发进行的过程。     

邻-氨基酚修饰吸附树脂对2-氨基吡啶的静态吸附热力学及动力学特征

合成了两种邻-氨基酚修饰超高交联吸附树脂(MOAR-1、MOAR-2),并用该树脂对水溶液中2-氨基吡啶的静态吸附热力学和动力学特征进行研究。热力学研究结果表明,Freundlich吸附等温方程能够对静态吸附等温线进行很好地拟合。吸附焓变ΔH<0,其绝对值小于60kJ/mol,表明以物理吸附为主以及该吸附剂容易脱附的特征;ΔG<0,说明吸附是自发行为;ΔS<0,表明吸附质分子在树脂表面上的运动受到了限制。两种树脂对2-氨基吡啶的吸附量随着温度的升高而降低,适当降低温度有利于吸附。动力学研究的结果表明:吸附符合一级动力学方程,吸附速率随温度升高而增大。表观活化能Ea<4.0kJ/mol,说明吸附较容易进行。     

ZrO2负载碳纳米管吸附去除水中氟的研究

以ZrO2负载多壁碳纳米管(ZrO2-MWCT)为吸附剂,系统研究了其对水中F-的吸附、脱附性能。结果表明,F-在ZrO2-MWCT吸附剂上的吸附等温线可以用Freundlich方程模拟,吸附动力学符合拟二级动力学方程,吸附速率随着F-初始浓度的提高而减低。当pH为4~5时,F-在ZrO2-MWCT吸附剂上的吸附量最大。水中阴离子的存在降低ZrO2-MWCT对F-的吸附量,不同阴离子对F-影响的大小顺序为:CO32->SO42->Cl->NO3-。吸附饱和的ZrO2-MWCT可用0.1mol/L的NaOH脱附再生,经4次再生后,其吸附量仍为14.55mg/g。     

Thermodynamics of Pb2+ and Ni2+ adsorption onto natural bentonite from aqueous solutions

Removal of Pb2+ and Ni2+ from aqueous solutions by sorption onto natural bentonite was investigated. Experiments were carried out as a function of particle size, the amount of bentonite, pH, concentration of metals, contact time, and temperature. The adsorption patterns of metal ions onto followed the Langmuir, Freundlich, and Dubinin-Radushkevich isotherms. This included adsorption isotherms of single-metal solutions at 303 K by batch experiments. The thermodynamic parameters (DeltaH,DeltaS,DeltaG) for Pb2+ and Ni2+ sorption onto bentonite were also determined from the temperature dependence. The adsorptions were endothermic reactions. The results suggested that natural bentonite is suitable as a sorbent material for recovery and adsorption of metal ions from aqueous solutions.     

Competitive adsorption of Pb2+, Cu2+, and Cd2+ ions on microporous titanosilicate ETS-10

In the present study, the competitive adsorption characteristics of binary and ternary heavy metal ions Pb2+, Cu2+, and Cd2+ on microporous titanosilicate ETS-10 were investigated in batch systems. Pure microporous titanosilicate ETS-10 was synthesized with P25 as the Ti source and characterized by the techniques of X-ray diffraction (XRD), field emission-scanning electron microscope (FESEM), nitrogen adsorption, and zeta-potential. Equilibrium and kinetic adsorption data showed that ETS-10 displays a high selectivity toward one metal in a two-component or a three-component system with an affinity order of Pb2+ > Cd2+ > Cu2+. The equilibrium behaviors of heavy metals species with stronger affinity toward ETS-10 can be described by the Langmuir equation while the adsorption kinetics of the metals can be well fitted to a pseudo-second-order (PSO) model.     

Removal of cadmium(II) and zinc(II) metal ions from binary aqueous solution by rice husk ash

The present study reports the competitive adsorptive removal of cadmium (Cd(II)) and zinc (Zn(II)) ions from binary systems using rice husk ash (RHA), a waste obtained from the rice husk-fired furnaces, as an adsorbent. The initial pH (pH₀) affects significantly the capacity of RHA for adsorbing the metallic ions in the aqueous solution. The pH₀ ≈ 6.0 is found to be the optimum for the removal of Cd(II) and Zn(II) ions by RHA. The single ion equilibrium adsorption from the binary solution is better represented by the non-competitive Redlich–Peterson (R–P) and the Freundlich models than by Langmuir model in the initial metal concentration range of 10–100 mg/l. The adsorption of Zn(II) ion is more than that of Cd(II) ion, and this trend is in agreement with the single-component adsorption data. The equilibrium metal removal decreases with increasing concentrations of the other metal ion and the combined effect of Cd(II) and Zn(II) ions on RHA is generally found to be antagonistic. Non-modified Langmuir, modified Langmuir, extended-Langmuir, extended-Freundlich, Sheindorf–Rebuhn–Sheintuch (SRS), non-modified R–P and modified R–P adsorption models were tested to find the most appropriate competitive adsorption isotherm for the binary adsorption of Cd(II) and Zn(II) ions onto RHA by minimizing the Marquardt's percent standard deviation (MPSD) error function. The extended-Freundlich model satisfactorily represents the adsorption equilibrium data of Cd(II) and Zn(II) ions onto RHA.     

A New Organophosphorus Insecticides Removal Process Using Fly ASH

Abstract

Fly ash and soil mixtures with a range of fly ash content from 1 to 100% were used to study adsorption and desorption of four organophosphorus insecticides, ethyl parathion, methyl parathion, fenitrothion and fenthion, in batch experiments. The object of the study was to develop a treatment process using fly ash as sorbent material to isolate/immobilize organic contaminants from aqueous solutions. The adsorption isotherms fit the Freundlich equation x/m=K_dC^1/n. The K_d values increase with the increase of the fly ash content. The isotherms seem to fit the S type, in mixtures of soil with a fly ash content from 0 to 10%, which implies that adsorption becomes easier as the concentration in the liquid phase increases. In mixtures of soil with a fly ash content from 25 to 50% the isotherms become L type and correspond to a decrease of site availability as the solution concentration increases. Finally in mixtures of soil with a fly ash content over 50%, C type adsorption was observed which correspond to a constant partition of the insecticides between the bulk solution and the adsorbent. Mass balance estimations show that the mean percent amounts of insecticides for a range of concentration 0.5–15 mg/l, removed by adsorption in the soil sample are 81.56 % for ethyl parathion, 48.97 % for methyl parathion, 67.06 % for fenitrothion and 86.65 % for fenthion. The adsorption increases as the fly ash content increased and reach the 100% in the “pure” fly ash. The adsorbed amounts of insecticides in mixtures of soils with >50% fly ash content, are up to 99%. In contrast, the amounts of desorption in water decrease as the fly ash content increase.

The results of this research demonstrate that the fly ash shows a significant capacity for adsorption of organophosphorus compounds from aqueous solution and can be used for pesticide removal process.     

Kinetics and equilibrium adsorption of Cu(II), Cd(II), and Ni(II) ions by chitosan functionalized with 2[-bis-(pyridylmethyl)aminomethyl]-4-methyl-6-formylphenol

Chitosan biopolymer chemically modified with the complexation agent 2[-bis-(pyridylmethyl)aminomethyl]-4-methyl-6-formylphenol (BPMAMF) was employed to study the kinetics and the equilibrium adsorption of Cu(II), Cd(II), and Ni(II) metal ions as functions of the pH solution. The maximum adsorption of Cu(II) was found at pH 6.0, while the Cd(II) and Ni(II) maximum adsorption occurred in acidic media, at pH 2.0 and 3.0, respectively. The kinetics was evaluated utilizing the pseudo-first-order and pseudo-second-order equation models and the equilibrium data were analyzed by Langmuir and Freundlich isotherms models. The adsorption kinetics follows the mechanism of the pseudo-second-order equation for all studied systems and this mechanism suggests that the adsorption rate of metal ions by CHS-BPMAMF depends on the number of ions on the adsorbent surface, as well as on their number at equilibrium. The best interpretation for the equilibrium data was given by the Langmuir isotherm and the maximum adsorption capacities were 109 mg g-1 for Cu(II), 38.5 mg g-1 for Cd(II), and 9.6 mg g-1 for Ni(II). The obtained results show that chitosan modified with BPMAMF ligand presented higher adsorption capacity for Cu(II) in all studied pH ranges.     

巯基树脂对金属离子的吸附性能(Ⅱ)

研究了自合成的巯基树脂对重金属离子Ag 、Hg2 、Cr3 的吸附容量、吸附动力学、等温吸附过程等静态吸附性能,影响吸附的因素和吸附机理.结果表明,该树脂对上述3种离子吸附能力强,吸附量分别达6.56mmol/g、3.25mmol/g、2.10mmol/g.树脂对各重金属离子等温吸附在实验浓度范围内符合Langmuir或Freundlich方程.吸附机理研究表明,巯基与金属离子发生了离子交换和配位反应,化学吸附起支配作用;另外树脂对Ag 、Hg2 吸附过程中存在一定的氧化还原现象.     

Adsorptive Removal of Cd,Cu, Ni and Mn from Environmental Samples Using Fe3O4-Zro2@APS Nanocomposite: Kinetic and Equilibrium Isotherm Studies

In this study, Fe₃O₄-ZrO₂ functionalized with 3-aminopropyltriethoxysilane (Fe₃O₄-ZrO₂@APS) nanocomposite was investigated as a nanoadsorbent for the removal of Cd(II), Cu(II), Mn (II) and Ni(II) ions from aqueous solution and real samples in batch mode systems. The prepared magnetic nanomaterials were characterized using X-ray powder diffraction (XRD), scanning electron microscopy/energy dispersion x-ray (SEM/EDX) Fourier transform infrared spectroscopy (FTIR) and transmission electron microscopy (TEM). Factors (such as adsorbent dose and sample pH) affecting the adsorption behavior of the removal process were studied using the response surface methodology. Under optimized condition, equilibrium data obtained were fitted into the Langmuir and Freundlich isotherms and the data fitted well with Langmuir isotherms. Langmuir adsorption capacities (mg/g) were found to be 113, 111, 128, and 123 mg/g for Cd, Cu, Ni and Mn, respectively. In addition, the adsorption kinetics was analyzed using five kinetic models, pseudo-first order, pseudo-second order, intraparticle diffusion and Boyd models. The adsorbent was successfully applied for removal of Cd(II), Cu(II), Mn (II) and Ni(II) ions in wastewater samples.     

Preparation of a novel chelating resin for the removal of Ni2+ from water

A new chelating resin DVB-MA-HDA modified with hydroxamic acid groups was prepared for the fast removal of Ni2＋ from water. SEM, BET, elemental analysis, FT-IR spectroscopy and XPS were used to characterize this new adsorbent. Batch adsorption experiment indicated that the equilibrium adsorption capacity of DVB-MA-HD for Ni2＋ was more than 130mg/g, and the adsorption isotherm can be well fitted by the Langmuir model. The adsorption kinetic curve indicates that more than 60% of the adsorption amount of Ni2＋ at equilibrium occurred within the initial 20 rain. 0.1 mol/L EDTA solution could desorb Ni2＋ from DVB-MA-HDA effectively.