柱撑粘土吸附去除水中重金属离子的实验研究

运用十二烷基磺酸钠和聚羟基硅铝对蒙脱石进行改性后的柱撑蒙脱石,分别研究了溶液的pH值,初始浓度和反应时间对Cu2 ,Cr3 和Cd2 三种重金属离子的吸附性能、平衡模型和动力学过程。结果表明:十二烷基磺酸钠柱撑蒙脱石对三种重金属离子都具有很强的吸附能力,聚羟基硅铝柱撑粘土次之;柱撑后的蒙脱石对单组分的重金属离子的吸附平衡方程符合Langmuir模型;吸附行为的动力学符合假一级动力学方程。柱撑粘土吸附去除水中重金属离子的实验研究@刘云$华南理工大学环境科学与工程学院!广州,510640 @吴平霄$华南理工大学环境科学与工程学院!广州,5…     

二连盆地脑木根凹陷铀成矿水文地质特征浅析

为取得二连盆地脑木根凹陷铀成矿水文地质条件,运用地下水动力学、水文地球化学、铀水文地球化学等知识,通过调查取样,分析数据,整理资料等进行研究。结果表明:该地区地下水水动力特征为从北西部、南东部的补给区向中部的排泄区径流;地下水水化学类型以Cl·HCO_3-Na、Cl-Na型水为主,矿化度最高106.50 g/L,平均3.50 g/L;该地区地下水水中铀含量较高,平均值为120μg/L,最高值可达910μg/L,自然底数为56.00μg/L,水中氡浓度平均值为100 Bq/L,最高值可达14 985 Bq/L,自然底数为95 Bq/L。研究结果表明该地区地下水环境特征有以利于铀成矿、富集。     

改性石墨烯海绵材料对铀的吸附研究

通过氧化石墨和氨基三亚甲基膦酸反应制得一种石墨烯海绵材料ATMP-GS,将制备的材料进行对铀的吸附实验,考察了溶液pH、温度、ATMP-GS用量、吸附时间和铀溶液初始浓度对吸附效果的影响。实验结果发现,在pH为5.0时ATMP-GS吸附铀的效果最好,吸附在3 h内即可达到平衡,最大吸附容量为96 mg/g,温度对其吸附铀的能力影响不大。ATMP-GS吸附铀的动力学过程符合准二级动力学模型,Langmuir和Freundlich吸附等温模型均可较好地用来描述ATMP-GS对铀的吸附。对该材料进行了SEM、XRD表征,结果表明该材料有较多地孔径分布,这将有利于铀的吸附进行。     

污染场地六价铬迁移转化机制与数值模拟研究

随着全球工业化迅猛发展,土壤和地下水六价铬污染日益严重。基于某铁合金厂铬渣场地现场调查与采样分析,开展铬渣场地土样吸附、渗透和弥散试验,研究六价铬在粉质黏土土样中的吸附特性和迁移规律,建立考虑对流-弥散-吸附的六价铬迁移三维动力学模型,结合数值软件获取污染源位于场地上、下游时地下水中六价铬迁移分布特征,并揭示弥散度?和分配系数 对六价铬时空分布的影响。试验结果表明,粉质黏土对六价铬吸附符合Langmuir等温吸附模型,最大吸附量为466.6 mg/kg;蒸馏水和160 mg/L 六价铬溶液入渗下粉质黏土渗透系数约为6.5×10–7～6.7×10–7 cm/s,1 000 mg/L六价铬溶液的渗透系数增大至4.4×10–6 cm/s;粉质黏土水动力弥散系数D为1.4×10–4 m2/d,计算得到阻滞因子 为4.2～10。数值模拟结果表明,场地下游受到六价铬污染时,即使不考虑分子扩散作用,上游仍有被污染的风险,污染程度取决于含水层的弥散度;考虑含水层对六价铬吸附时,土体分配系数越大,六价铬污染羽分布范围越小,在预测地下水中六价铬浓度分布时应重点考虑六价铬吸附等转化过程。     

基于透钙磷石向磷灰石转化的除氟过程及其机理

磷灰石的沉淀可以影响矿物相-水相之间氟化物的分配,在饮用水除氟以及延缓土壤中氟的迁移过程中扮演着重要角色。本研究通过共沉淀法制备了磷灰石的前驱体矿物透钙磷石,并将其转化为溶解度更低的磷灰石,以研究其转化过程中矿物相的演变及对氟的固定能力,并探讨了氟的固定机理。结果表明,溶液中的氟伴随着磷灰石的沉淀由液相转移至固相中,此过程对氟的固定量高达21.8 mg/g,是羟基磷灰石对氟吸附量的2.2倍。透钙磷石转化为磷灰石的过程为溶解-沉淀过程,氟在磷灰石的生长过程中进入磷灰石的结构中。此外,透钙磷石向磷灰石的转化过程对氟的去除具有高度选择性,溶液中共存的Cl^-、CO₃^2-、NO₃^-和SO₄^2-等阴离子几乎不影响其氟去除能力。研究结果表明,通过透钙磷石-磷灰石的转化可以将氟固定到磷灰石中,从而降低氟的可迁移性和渗入地下水造成的环境风险。     

北京地热开采中的尾水氟处理方法

釆用猪骨灰型羟基磷灰石、蜂窝煤灰和赤铁矿进行吸附除氟实验,猪骨灰型羟基磷灰石效果较好,蜂窝煤灰有一定的效果。猪骨灰型羟基磷灰石的氟吸附量最高可达1.28mg/g,蜂窝煤灰可达1.00mg/g。猪骨灰型羟基磷灰石出水含氟量的最低值为0.39mg/L,氟去除率达94.3%。蜂窝煤灰除氟的最低含氟量为4.25mg/L,接近北京市三级排放标准。不同pH值条件下的除氟实验表明,酸性条件下蜂窝煤灰对氟的吸附量大大增加,出水含氟量明显降低,为1.44mg/L,pH值的变化对猪骨灰型羟基磷灰石的除氟效果影响不大。蜂窝煤灰和猪骨灰型羟基磷灰石的平衡吸附曲线表明,吸附作用为多层分子吸附,利用蜂窝煤灰和猪骨灰型羟基磷灰石对氟的吸附量和出水含氟量数据,估算了平衡吸附曲线表达式的系数。     

腐植酸改性强化磁铁矿吸附水体中铅镉的实验研究

磁铁矿是一种绿色廉价的矿物材料,对水体中重金属离子具有良好的吸附性,但吸附容量低,选择性差,易团聚,通过改性可以克服该缺点并提高其吸附性能。本文以腐植酸为改性剂,采用常温水相反应制备了腐植酸改性磁铁矿吸附材料。通过傅里叶红外光谱(FTIR)、扫描电镜(SEM)和X射线光电子能谱(XPS)表征研究其表面形貌和微观结构。采用静态平衡实验考察了pH、吸附时间等因素对铅、镉吸附性能的影响,探讨了吸附动力学规律,拟合了吸附等温线。结果表明:腐植酸上的羧基、羟基被成功地接枝到了磁铁矿表面。在室温下,溶液初始pH对Pb~(2+)的吸附率几乎无影响,对Cd~(2+)的影响较大,当pH=7时,Pb~(2+)和Cd~(2+)吸附率均达到了95%。对初始质量浓度为10mg/L的Pb~(2+)、Cd~(2+)最佳吸附平衡时间为360min,吸附过程符合准二级动力学方程。吸附等温线实验得到的竞争吸附顺序为Pb~(2+)Cd~(2+),由Langmuir等温吸附模型得到Pb~(2+)、Cd~(2+)饱和吸附容量分别为39.27mg/g、28.95mg/g,显著大于磁铁矿的饱和吸附容量,表明磁铁矿经腐植酸改性后增强了对水中铅镉的吸附能力。     

磷灰石固定水溶性铅离子研究进展

羟基磷灰石与天然磷灰石均能有效地固定水溶性铅离子,１ｇ羟基磷灰石或改性活性天然磷灰石除去水溶液中的铅离子量可以高达８００ｍｇ;其反应机理以磷灰石的溶解与铅的磷酸盐矿物的沉淀为主,伴有表面吸附作用。羟基磷灰石和改性活化天然磷灰石可用于含铅废水的处理,而性能良好的天然磷灰石在对铅污染水体、土壤及废弃物进行原地改良方面具有广阔的前景。     

溶液中Pb~(2+),Cd~(2+)和Cu~(2+)离子对羟基磷灰石吸附Zn~(2+)行为的影响

本文研究了在Pb~(2+),Cd~(2+)和Cu~(2+)等离子共存的条件下,羟基磷灰石对溶液中Zn~(2+)离子的吸附行为,讨论了Pb~(2+),Cd~(2+)和Cu~(2+)离子对Zn~(2+)吸附行为的影响;比较了羟基磷灰石对上述离子的吸附能力。实验结果表明:随着Cd~(2+)离子浓度增大,对Zn~(2+)的去除率逐渐增高,羟基磷灰石对Cd~(2+)和Zn~(2+)离子无吸附选择性。而随着Cu~(2+)离子浓度增大,对Zn~(2+)的去除率急剧下降,表现出明显的吸附选择性。另一方面,对Zn~(2+)的去除率几乎不随Pb~(2+)离子浓度的变化而改变,这是由于羟基磷灰石对这两种离子的吸附行为与机理不同。上…     

羟基磷灰石对水溶性Fe~(3+)的去除机理

利用天然磷矿粉为原料制备的羟基磷灰石(HAP)研究其去除水溶性Fe3+作用机理。结果表明:HAP对水溶液中Fe3+离子的去除过程是一个复杂的非均相固-液反应,分为两个阶段:初期阶段(t≤20 min)反应速度快,动力学过程复杂;后期阶段(t20min)反应速度较慢,符合一级反应动力学方程。HAP去除水溶性Fe3+离子的主要作用机理是溶解-沉淀和表面吸附作用。     

Dynamic fuzzy neural network for simulating the fixed-bed adsorption of cadmium,nickel, and zinc on bone char

This study introduces the application of a dynamic fuzzy neural network for fitting and simulating the adsorption of nickel, cadmium, and zinc ions in mono- and bi-metallic solutions (nickel–cadmium, nickel–zinc, and cadmium–zinc) using packed-bed columns with bone char. This neural network model has shown a flexible and self-adaptive architecture with a faster learning speed than that of traditional artificial neural approaches. Results showed that this neural network model was reliable for representing the high asymmetry behavior of concentration profiles in both mono- and bi-metallic breakthrough curves where its accuracy was quite reasonable. Breakthrough parameters for mono-component and binary systems of tested heavy metals were calculated and compared. This analysis showed that the removal of these heavy metal ions in binary systems was a strong competitive adsorption process where the presence of co-ions reduced the removal performance of bone char at fixed-bed adsorbers. Results of surface characterization of adsorbent samples with X-ray photoelectron and infrared spectroscopy supported a removal mechanism based on an ion exchange between calcium from hydroxyapatite of bone char and heavy metal ions in the solution forming new metal–phosphate interactions in the adsorbent surface.     

季胺盐阳离子插层蒙脱土对铀吸附性能的研究

通过十六烷基三甲基溴化铵（CTMAB）与钠基蒙脱土离子交换制备出季胺盐阳离子插层蒙脱土（CTMA’-M）,采用小角X射线衍射仪、傅里叶变换红外光谱仪和高分辨透射电镜表征微观结构,研究CTMA’的插层量、溶液的初始pH值、初始浓度和其他共存离子对吸附铀性能的影响,考察了CTMA’-M处理铀矿水）台废水的应用性能。结果表明：CTMA’插层后蒙脱土的层间距由1．21nm增加到4．09nm,但仍保持钠基蒙脱土原有的晶体结构。随CTMAB用量的增加,插层到蒙脱土层间的CTMA’量增加,对铀离子的吸附容量逐渐增大,当CTMAB的用量超过阳离子交换容量的1．4倍时,铀吸附容量基本保持不变。溶液pH和接触时间对铀离子吸附性能影响较大．CTMA’-M最佳吸附pH值为6．0,平衡吸附时间为80min,CTMA’插层能够改善蒙脱土对铀离子的选择性吸附。在1L含有15mg／L铀的废水中加入1．5gCTMA’-M时,铀的去除率达到98％以上。     

Effects of Pb^2＋, Cd^2＋ and Cu^2＋ on the Aqueous Zn^2＋ Sorption by Hydroxyapatite

In this paper, the behaviors of aqueous zinc sorption by hydroxyapatite in the co-existence of Pb^2＋, Cd^2＋ and Cu^2＋ are investigated, the effects of Pb^2＋, Cd^2＋ and Cu^2＋ on the sorption of Zn^2＋ are discussed, and the hydroxyapatite sorption capabilities for Pb^2＋, Cd^2＋, Cu^2＋ and Zn^2＋ are compared. The experimental results show that the Zn^2＋ removal efficiency decreases gradually with the increase of the Cd^2＋ concentration of the solution, and there is no sorption preference between Cd^2＋ and Zn^2＋. On the other hand, the Zn^2＋ removal efficiency rapidly decreases rapidly with the increase of the Cu^2＋ concentration of the solution, and there is a clear sorption preference between Cu^2＋ and Zn^2＋. It is noticed that the Zn^2＋ removal efficiency is hardly changed with the variance of Pb^2＋ concentration because the removal mechanisms for these two ions are totally different. It is concluded that the adsorption affinities of the heavy metals for the hydroxyapatite follows this sequence： pb^2＋〉 Cu^2＋〉 Cd^2＋〉 Zn^2＋.     

Biosorption of Cd(II) from synthetic wastewater using dry biofilms from biotrickling filters

Biofilms wasted from biotrickling filters was dried and used as biosorbent for Cd(II) removal from aqueous solutions. The adsorption condition and effect, adsorption isotherms and kinetics of Cd(II) removal were investigated, and the effects of competitive metal ions on Cd(II) removal were also examined. Results showed that the dry waste biofilms reached the maximum adsorption capacity of 42 mg/g of Cd(II) at 25 °C for 120 min when the initial concentration of Cd(II) and their pH were 50 mg/L and 6.0, respectively. Under these conditions, the removal efficiency of Cd(II) reached to 89.3% when the biosorbent dosage was 2.0 g/L. The Langmuir isotherm model correlated with the isotherm data better than the Freundlich isotherm model, and the pseudo-second-order model fitted the kinetic data better than the pseudo-first-order model. These results indicated that the adsorption was monolayer accompanied with chemical adsorption. In the presence of other metal ions, divalent metal ions of Ca and Zn inhibited the performance of Cd(II) biosorption significantly, while Na(I), K(I) and Fe(III) which had a higher or lower valence than Ca(II) affected slightly when containing 50 mg/L Cd(II), 0.5 g/L adsorbent dosage and pH 6.0. The analyses of scanning electron microscopy and Fourier transform infrared spectroscopy illuminated that the biosorbent had porous structures and the amide group was the majorly responsible for Cd(II) removal. Dry biofilms were novel sorbents for effective removal Cd(II), and it could be reused and recycled if necessary.     

Kinetic and equilibrium study of Ni(II) sorption from aqueous solutions onto Peganum harmala-L

In this study, the adsorption behavior of Ni(II) in an aqueous solution system using natural adsorbent Peganum harmala-L was measured via batch mode. The prepared sorbent was characterized by scanning electron microscope, Fourier transform infrared spectroscopy, N₂ adsorption–desorption and pH_zpc. Adsorption experiments were carried out by varying several conditions such as contact time, metal ion concentration and pH to assess kinetic and equilibrium parameters. The equilibrium data were analyzed based on the Langmuir, Freundlich, Temkin and Dubinin–Radushkevich isotherms. Kinetic data were analyzed using the pseudo-first-order, pseudo-second-order and intra-particular diffusion models. Experimental data showed that at contact time 60 min, metal ion concentration 50 mg/L and pH 6, a maximum amount of Ni(II) ions can be removed. The experimental data were best described by the Langmuir isotherm model as is evident from the high R ² value of 0.988. The adsorption capacity (q _m) obtained was 68.02 mg/g at an initial pH of 6 and a temperature of 25 °C. Kinetic studies of the adsorption showed that equilibrium was reached within 60 min of contact and the adsorption process followed the pseudo-first-order model. The obtained results show that P. harmala-L can be used as an effective and a natural low-cost adsorbent for the removal of Ni(II) from aqueous solutions.     

Adsorption kinetics of herbicide paraquat in aqueous solution onto a low-cost adsorbent, swine-manure-derived biochar

Biochars have received increasing attention in recent years because of their significant properties such as carbon sequestration, soil fertility, and contaminant immobilization. In this work, the adsorptive removal of paraquat (1,1′-dimethyl-4,4′-dipyridinium chloride, one of the most widely used herbicides) from aqueous solution onto the swine-manure-derived biochar has been studied at 25 °C in a batch adsorption system. The adsorption rate has been investigated under the controlled process parameters including initial pH (i.e., 4.5, 6.0, 7.5, and 9.0), paraquat concentration (i.e., 0.5, 1.0, 2.0, 4.0, and 6.0 mg/L), and biochar dosage (i.e., 0.10, 0.15, 0.20, 0.25, and 0.30 g/L). Based on the adsorption affinity between cationic paraquat and carbon-like adsorbent, a pseudo-second order model has been developed using experimental data to predict the adsorption kinetic constant and equilibrium adsorption capacity. The results showed that the adsorption process could be satisfactorily described with the reaction model and were reasonably explained by assuming an adsorption mechanism in the ion exchange process. Overall, the results from this study demonstrated that the biomass-derived char can be used as a low-cost adsorbent for the removal of environmental cationic organic pollutants from the water environment.     

Studies on the recovery of uranium from nuclear industrial effluent using nanoporous silica adsorbent

In this paper, the sorption of uranium onto nanoporous silica adsorbent in the presence of nitrate, sulfate, chloride, fluoride and phosphate was studied. The effect of contact time between the nanoporous sorbent and aqueous solution, pH and initial concentration of uranium was also investigated. Uranium sorption onto nanoporous silica adsorbent is a very fast process as sorption rate increases with pH increment. Optimum pH for uranium sorption was 4?C8. Experimental sorption isotherm is successfully described by Langmuir and Freundlich models. The results obtained by batch experiments showed that the presence of high concentration of nitrate, sulfate, chloride and phosphate anions alone had no interference with uranium recovery. However, the presence of fluoride ions (>250?mg/L) decreases uranium sorption by about 55?%. The results also showed that the presence of phosphate ions (about 300?mg/L) in solution could remove fluoride interference completely. Finally, the efficiency of the nanoporous silica adsorbent for uranium recovery from wastewater of the uranium conversion facility was investigated.     

Adsorption of lead using a new green material obtained from Portulaca plant

In the present study the potential of a new green material obtained from Portulaca oleracea plant was investigated. The material was used without any chemical treatment to study the adsorption behavior of lead ions from aqueous solution. Various batch experiments were carried out using different experimental conditions such as pH, contact time, adsorbent concentration, and metal ion concentration to identify the optimum conditions. The influence of these parameters on the adsorption capacity was studied. Results showed the optimum initial pH for adsorption as 6. Adsorption equilibrium was reached in 120?min. The adsorption data were modeled using both the Langmuir and Freundlich classical adsorption isotherms. Results show ~78% removal of lead from aqueous solution. The kinetic data corresponded well with pseudo second-order equation. From the initial results, the green material obtained from the waste of Portulaca seems to be a potential low-cost adsorbent for removal of lead ions from water.     

ZH型重金属螯合纤维对水溶液中Sr2+的吸附行为

研究了ZH型重金属螯合纤维对水溶液中Sr~(2+)的吸附行为,考察了pH值、纤维加入量、Sr~(2+)初始浓度、作用时间等对吸附行为的影响,并采用SEM、EDS和FTIR等现代分析测试手段探讨了ZH型重金属螯合纤维对Sr~(2+)的吸附机制。结果表明,在pH值为7.0、纤维加入量为2.0 g/L、Sr~(2+)初始质量浓度为50 mg/L的条件下,纤维对Sr~(2+)的吸附在4 h左右基本达到平衡。实验条件下ZH型重金属螯合纤维对Sr~(2+)的最大吸附量可达26.22 mg/g。等温吸附拟合结果表明,ZH型重金属螯合纤维对Sr~(2+)的吸附可能是以单分子层为主的单分子层和多分子层吸附共同作用的结果。纤维对Sr~(2+)的动力学吸附过程符合准二级动力学模型。红外光谱分析表明Sr~(2+)与纤维上—NH_2和—COOH等基团进行配位络合从而吸附在纤维表面,—CH_2—和C=CH_2等基团参与此吸附过程。能谱分析表明Sr~(2+)与纤维上Na~+和Ca~(2+)还存在着离子交换作用。     

Evaluating the effectiveness of a hybrid sorbent resin in removing fluoride from water

In some regions of the world, the concentration of fluoride in groundwater is high. To reduce the amount of fluoride to acceptable drinking water standard, it is highly recommended to treat the water. Fluoride adsorption in aqueous solution by a hybrid resin was studied in this research because of its functional groups likeness with goethite. Kinetic data showed that F adsorption was rapid in the beginning and maximum uptake occurred in within 10 min and equilibrium reached within 100 min. The experimental results showed that fluoride adsorption was influenced by pH of solution and optimum operating pH was in the range of 3 to 5.5. Langmuir model was applicable to the present study and F ions were exchanged with hydroxide ions in nano-scaled structure on the surface of sorbent. This adsorbent with 61 % efficiency is suitable for the regions where F concentration is less than 4 mg/L.