改性桑枝粉及沸石对水中高氯酸盐的吸附研究

以十六烷基三甲基溴化铵为改性剂制备改性桑枝粉和改性沸石，采用红外光谱和扫描电镜对改性产物的结构进行表征，并对吸附剂的Zeta电位进行分析，以探讨高氯酸盐的吸附机理。考察pH值、吸附剂投加量和高氯酸盐初始浓度对改性产物吸附水中高氯酸根的影响。结果表明，改性产物表面的季铵阳离子基团能较好地吸附废水中的高氯酸根；去除率随吸附...     

硫酸钛混凝去除无机砷(Ⅲ)的效能

使用硫酸钛作为混凝剂,研究了混凝去除As(Ⅲ)过程中溶液pH值、混凝剂投加量、砷的初始浓度以及阴离子对除砷效果的影响.硫酸钛的水解沉淀物颗粒等电点为pH =5;当pH =6时,水解沉淀物的粒径最大.在pH =5 ～8范围内,As(Ⅲ)的去除率高且基本稳定;而沉淀物颗粒Zeta电位降低较大.说明水解沉淀物Zeta电位对As(Ⅲ)的去除影响不大.混凝剂投加量为2.5 ～10 mg/L时,As (Ⅲ)的去除率随投加量的增加而显著增加;混凝剂投加量大于15 mg/L时,As(Ⅲ)去除率随混凝剂投加量的增加变化趋于平缓.水中阴离子(硅酸根和磷酸根离子)的存在会降低混凝对As (Ⅲ)的去除效率.     

负载TiO_2的活性炭纤维改性电极电吸附除氟

采用溶胶-凝胶法制备TiO2凝胶,将TiO2凝胶涂覆在活性炭纤维表面并进行热处理制备改性电极（TiO2/ACF）,利用扫描电子显微镜（SEM）、X射线衍射光谱仪（XRD）、比表面和孔隙度分析仪对负载前后电极的表面特性进行表征,并探讨了其对NaF溶液的电吸附效果。结果表明,电极负载TiO2后表面变得粗糙,比表面积和总孔体积减小,而介孔体积和平均孔径增大。此外,表面的TiO2同时以金红石和锐钛矿的晶型存在。电吸附实验结果显示,加电可以提高吸附容量,而且电压、pH和初始氟离子浓度均对电吸附容量产生影响：电压增大,吸附容量增加,当施加电压为2 V时,电吸附容量为1.03 mg/g,比开路电位时提高40%;pH可以通过影响氟离子在溶液中的存在形态和TiO2/ACF电极表面的羟基基团对电吸附容量产生影响;初始氟离子浓度升高,电极吸附容量增大,但是去除率降低。在处理初始氟离子浓度为4 mg/L的NaF溶液时,在2 V电压、中性pH和12 h的吸附时间下,改性ACF为电极的吸附量为1.32 mg/g。     

负载TiO2的活性炭纤维改性电极电吸附除氟

采用溶胶-凝胶法制备TiO2凝胶,将TiO2凝胶涂覆在活性炭纤维表面并进行热处理制备改性电极(TiO2/ACF),利用扫描电子显微镜(SEM)、X射线衍射光谱仪(XRD)、比表面和孔隙度分析仪对负载前后电极的表面特性进行表征,并探讨了其对NaF溶液的电吸附效果。结果表明,电极负载TiO2后表面变得粗糙,比表面积和总孔体积减小,而介孔体积和平均孔径增大。此外,表面的TiO2同时以金红石和锐钛矿的晶型存在。电吸附实验结果显示,加电可以提高吸附容量,而且电压、pH和初始氟离子浓度均对电吸附容量产生影响:电压增大,吸附容量增加,当施加电压为2 V时,电吸附容量为1.03 mg/g,比开路电位时提高40%;pH可以通过影响氟离子在溶液中的存在形态和TiO2/ACF电极表面的羟基基团对电吸附容量产生影响;初始氟离子浓度升高,电极吸附容量增大,但是去除率降低。在处理初始氟离子浓度为4 mg/L的NaF溶液时,在2 V电压、中性pH和12 h的吸附时间下,改性ACF为电极的吸附量为1.32 mg/g。     

饮用水除砷材料吸附特性及影响因素分析

采用活性氧化铝、零价铁粉和载铁沸石作为吸附剂,通过静态吸附实验,研究3种饮用水除砷材料的吸附特性及影响因素。结果表明,在pH值为6.5,砷浓度为1 mg/L,投加量为2 g/L,25℃恒温的条件下,活性氧化铝、零价铁粉和载铁沸石分别在90 min、150 min和90 min达到吸附平衡状态,均较好符合langmuir等温吸附模型,对砷的最大吸附容量依次为7.3、3.3和3.9 mg/g。pH值和竞争性阴离子对砷的去除均有显著影响。降低溶液pH值能明显提高3种材料的除砷效率;水中磷酸根离子的存在,能够明显降低活性氧化铝和零价铁粉的除砷效率;水中硅酸根离子的存在,能够明显降低零价铁粉和载铁沸石的除砷效率。     

天然锰砂去除水中的砷

天然锰砂是一种廉价、高效的水处理用材料,但尚未用于水中砷的去除。实验研究了反应时间、砷形态、初始砷浓度、温度、溶液初始pH对吸附过程的影响。结果表明,天然锰砂对As(Ⅲ)的吸附能力大于As(Ⅴ)。25℃时,固液比为10 g/L的条件下,天然锰砂对初始浓度为5.0 mg/L的砷溶液吸附过程经72 h基本达到平衡,平衡时对As(Ⅲ)和As(Ⅴ)的去除率分别达到94.5%和85.9%。吸附过程符合Lagergren准一级反应动力学模型和假二级反应动力学模型。相比之下,假二级动力学模型拟合程度更高。对As(Ⅲ)和As(Ⅴ),45℃时的吸附量均大于25℃时。不同温度下,天然锰砂对As(Ⅲ)和As(Ⅴ)的吸附过程更符合Freundlich等温吸附模型。在溶液初始pH为3～10范围内,锰砂对砷的吸附能力受pH的影响较小。实验结果表明,天然锰砂是一种具有实际应用潜力的除砷材料。     

固定化改性蒙脱土对苯酚吸附性能的研究

利用十六烷基三甲基溴化铵对天然蒙脱土进行改性,并用聚乙烯醇对改性蒙脱土进行固定化处理,然后进行柱状吸附和振荡条件的吸附试验。研究结果表明,HDTMA改性蒙脱土固定化后能有效吸附苯酚,不同环境条件对苯酚的柱状吸附能力产生不同的影响。在pH4~8的范围内,固定化改性蒙脱土对苯酚的吸附效果无显著性差异,pH在10以上,其吸附能力明显下降;温度对吸附效果影响不大;进水苯酚浓度越高,改性蒙脱土对苯酚的吸附量越大,但出水苯酚浓度也高;苯酚的流速越小,吸附容量越高,吸附效果越好。     

5种铁氧化物去除As(V)性能的比较研究

为了从铁氧化物中筛选得到潜在经济有效的除砷材料,对5种铁氧化物去除As(V)的性能进行了比较研究。吸附实验结果表明,其吸附容量依次为施氏矿物四方纤铁矿水铁矿赤铁矿针铁矿,其吸附过程均符合准二级动力学,约24 h时吸附达到平衡。其中,pH=5时,施氏矿物的吸附容量达到83 mg/g。分别投加500 mg/L和300 mg/L的施氏矿物,可将含砷1.484 mg/L和0.850 mg/L、高TOC含量和高pH特征的模拟配水砷浓度降至0.01 mg/L以下。鉴于施氏矿物良好的吸附除砷性能,进一步通过SEM、FTIR和电位滴定对其表面特性进行了深入研究,结果显示,本研究中制备的施氏矿物存在结构性或表面吸附的SO42-,其(质子)表面位密度约为4.32个/nm2,表面质子化常数pK1为4.60,pK2为-8.98。     

固定化改性蒙脱土对苯酚吸附性能的研究

利用十六烷基三甲基溴化铵对天然蒙脱土进行改性，并用聚乙烯醇对改性蒙脱土进行固定化处理，然后进行柱状吸附和振荡条件的吸附试验。研究结果表明，HDTMA改性蒙脱土固定化后能有效吸附苯酚，不同环境条件对苯酚的柱状吸附能力产生不同的影响。在pH4～8的范围内，固定化改性蒙脱土对苯酚的吸附效果无显著性差异，pH在10以上．其吸附能力明显下降；温度对吸附效果影响不大；进水苯酚浓度越高，改性蒙脱土对苯酚的吸附量越大，但出水苯酚浓度也高；苯酚的流速越小，吸附容量越高，吸附效果越好。     

三维电极电吸附动态反应器的除氟特征研究

采用自制的单极性复合型三维阳极作为第三维电极对含氟水进行动态电促吸附实验,通过研究不同填充床高度、阴阳极板间距、隔膜材料对电促吸附除氟效果的影响,确定反应器的最佳结构参数为:填充床高度20 cm、阴阳极板间距4 cm、隔膜为nafion117膜。工作电压、进水pH、进水流速、共存物质对氟离子去除效果的影响结果表明:在一定范围内增大工作电压,降低进水pH或进水流速均可提高除氟效果。相应的最佳操作条件为:工作电压7 V、进水流速4 mL/min、酸性pH;腐殖酸和碳酸根离子的存在会对氟离子去除产生较强抑制作用,低浓度的氯离子可促进氟离子的电促吸附。扫描电镜(SEM)-电子能谱(EDX)的表征结果显示三维颗粒电极的表面及孔隙内部均可吸附氟离子,且电吸附后并未出现电极腐蚀现象。     

Pteris multifida Poir., a new arsenic hyperaccumulator: characteristics and potential

This paper reports a new arsenic hyperaccumulator, Pteris multifida Poir, a fern that grows widely in the southeast of China. The results show that the average arsenic content in the fronds was 1144.78 mg/kg, with a highest value of 2061 mg/kg. The average arsenic content in the roots was 692.7 mg/kg, and the average bioconcentration factor was 1.2, with a highest value of 1.78. The average translocation factor was 1.77, with a highest value of 3.13. The arsenic content in fronds was significantly correlated with the pH and the phosphorus available in the soil, but less correlated with the arsenic concentration in the soil. P.multifida Poir might accumulate the maximum arsenic in fronds when the soil-available phosphorus was 55 mg/kg and the soil pH was 8.34.     

电吸附法去除水中刚果红的研究

以一种典型的联苯胺类直接偶氮染料刚果红为模型物,利用自制活性炭电极,研究各种因素(扫描电压、溶液初始浓度、电解质浓度、pH、电极活性炭用量等)对电吸附效果的影响.结果表明,在-1.0～1.0V的扫描电压下,刚果红没有氧化还原反应发生,电吸附是一稳定而又可逆的过程；扫描电压负极化使刚果红的吸附率降低,而正极化能明显提高吸附率,在0.9V扫描电压下的吸附率比开路(扫描电压为零)时提高了18.6百分点;刚果红溶液的初始浓度越高,吸附平衡时的吸附容量越高,但吸附率反而降低,刚果红溶液的初始质量浓度为40 mg/l时的吸附容量是10 mg/L时的4.87倍,而吸附率降低了21.4％；随着电解质Na2SO4的加入,加快了刚果红在溶液中的运动速率,但刚果红的最终去除率有所降低,并且在一定范围内Na2SO4加入的越多,刚果红的最终吸附效果越差；pH为7(未调节)时,活性炭电极对刚果红的吸附率最高,pH为2、11时,吸附率均有所降低;随着电极活性炭用量的增加,刚果红的吸附容量逐渐降低,吸附率则逐渐提高,达到吸附平衡所需时间相应也延长.     

As(V) retention on soils and forest by-products and other waste materials

As(V) retention capacity is determined by means of adsorption/desorption trials performed for coarse and fine ground mussel shell, forest and vineyard soils with or without fine shell, pine wood ash, oak wood ash, pine sawdust and slate-processing fines. Pine ash shows the highest arsenic retention potential (with >97 % adsorption and ≤1 % desorption), followed by shell-amended forest soil (adsorption between 96 and 92 %), by un-amended forest soil (adsorption between 98 and 86 %) and by the amended vineyard soil (adsorption between 92 and 75 %). Sawdust is the material with the lowest arsenic retention capacity in most cases, with un-amended vineyard soil also showing poor results. In the case of oak ash, As(V) percentage adsorption becomes higher with increasing added arsenic concentrations, while this increase in added arsenic causes lower percentage adsorption in the case of slate fines. Regarding adsorption ability, As(V) adsorption data were fitted to Freundlich and Langmuir models, showing good fitting, with pine ash and shell-amended forest soil having the highest K _F values. In view of that, mussel shell amendment would be useful to increase arsenic retention on forest and vineyard soils, while pine ash could be used to retain arsenic even from wastewaters.     

Removal of arsenic(V) from aqueous solutions using iron-oxide-coated modified activated carbon.

Removal of arsenic(V) from aqueous solutions was evaluated with the following three different sorption materials: coal-based activated carbon 12 x 40 (activated carbon), iron(II) oxide (FeO)/activated carbon-H, and iron oxide. The apparent characteristics and physical chemistry performances of these adsorbents were investigated by X-ray diffraction, nitrogen adsorption, and scanning electronic microscope. Also, batch experiments for arsenic removal were performed, and the effects of pH value on arsenic(V) removal were studied. The results suggest that the main phases of the iron oxide surface are magnetite, maghemite, hematite, and goethite; fine and uniform iron oxide particles can cover activated carbon surfaces and affect the surface area or pore structures of activated carbon; adsorption kinetics obey a pseudo-first-order rate equation; and adsorption capacities of adsorbents are affected by the values of pH. The optimum value of pH for iron oxide lies in a narrow range between 4.0 and 5.5, and arsenic(V) removal by FeO/activated carbon-H is ideal and stable in the pH range 3 to 7, while activated carbon has the lowest adsorption capacity in the entire pH range. Also, the adsorption characteristics of FeO/activated carbon-H composites and virgin activated carbon match well the Langmuir adsorption model, while those of iron oxide fit well the Freundlich adsorption model.     

模拟酸雨对氧化锰吸附砷(Ⅲ)的解吸行为研究

以合成的氧化锰为吸附剂研究了酸雨pH值、酸雨离子强度、解吸时间和解吸次数等因素对模拟酸雨解吸砷(Ⅲ)的影响。实验结果表明:氧化锰对砷(Ⅲ)吸附容量较大,等温平衡吸附量为:48.38 mg/g。模拟酸雨的pH值与离子强度对砷(Ⅲ)的解吸影响不大;解吸反应在90 min后基本达到平衡,平衡解吸量为2.69×10-2mg/g;随解吸次数的增加解吸量变化不大。氧化锰对砷(Ⅲ)的吸附主要是专性的配位吸附,吸附砷(Ⅲ)后难以被模拟酸雨解吸。     

Sorption and leaching of flucetosulfuron in soil

Abstract

The adsorption–desorption and leaching of flucetosulfuron, a sulfonylurea herbicide, was investigated in three Indian soils. Freundlich adsorption isotherm described the sorption mechanism of herbicide with adsorption coefficients (K_f) ranging from 17.13 to 27.99 and followed the order: Clayey loam?>?Loam?>?Sandy loam. The K_f showed positive correlation with organic carbon (OC) (r?=?0.910) and clay content (r?=?0.746); but, negative correlation with soil pH (r = ?0.635). The adsorption isotherms were S-type suggesting that herbicide adsorption was concentration dependent and increased with increase in concentration. Desorption followed the sequence: sandy loam?>?clayey loam?>?loam . Hysteresis (H) was observed in all the three soils with H?<?1. Leaching of flucetosulfuron correlated positively with the soil pH; but, negatively with the OC content. Sandy loam soil (OC- 0.40%, pH ?7.25) registered lowest adsorption and highest leaching of flucetosulfuron while lowest leaching was found in the loam soil (pH ? 7.89, OC ? 0.65%). The leaching losses of herbicide increased with increase in the rainfall intensity. This study suggested that the soil OC content, pH and clay content played important roles in deciding the adsorption–desorption and leaching behavior of flucetosulfuron in soils.     

Characterizing As(III,V) adsorption by soils surrounding ash disposal facilities

Leachate derived from unlined coal ash disposal facilities is a potential anthropogenic source of arsenic to the environment. To establish a theoretical framework for predicting attenuation of arsenic by soils subject to ash landfill leachate, which is typically enriched in calcium and sulfate, the adsorption of As(V) and As(III) was characterized from 1 mM CaSO₄ for 18 soils obtained down-gradient from three ash landfill sites and representing a wide range in soil properties. As(V) consistently exhibited an order of magnitude greater adsorption than As(III). As(V) adsorption was best described by coupling pH with 15 s DCB-Fe (R² = 0.851,  = 0.001), although pH coupled to clay, DCB-Fe, or DCB-Al also generated strong correlations. For As(III), pH coupled to Ox–Fe (R² = 0.725,  = 0.001) or Ox–Fe/Al (R² = 0.771,  = 0.001) provided the best predictive relationships. Ca²⁺ induced increases in As(V) adsorption whereas sulfate suppressed both As(V) and As(III) adsorption. Attenuation of arsenic from ash leachate agreed well with adsorption measured from 1 mM CaSO₄ suggesting that the use of 1 mM CaSO₄ in laboratory adsorption tests is a reasonable approach for estimating arsenic behavior in soils surrounding ash landfills. We also showed that the impact of leachate-induced changes in soil pH over time may not be significant for As(V) adsorption at pH < 7; however, As(III) adsorption may be impacted over a wider pH range especially if phyllosilicate clays contribute significantly to adsorption. The benefits and limitations of predicting arsenic mobility using linearized adsorption coefficients estimated from nonlinear adsorption isotherms or from the relationships generated in this study are also discussed.     

Effect of biosolid incorporation on arsenic distribution in Mollisol soils in central Chile

The effect of biosolid incorporation on arsenic distribution in Mollisol soils in central Chile was studied. Two soils were sequentially extracted for arsenic with a five-step method that accounts for the following arsenic forms: non-specifically adsorbed (F1), specifically adsorbed (F2), amorphous and poorly crystallized Fe and Al oxides (F3), well-crystallized Fe and Al oxides (F4) and residual (F5). The arsenic residual fraction was predominant in Pintué soil, whereas in Graneros soil, arsenic was mostly associated to amorphous Fe and Al oxides. Graneros soil exhibited a higher As(V) adsorbing capacity than Pintué soil, which relates to the higher clay and iron and aluminum oxides contents, confirming that these components participation is essential for the adsorption of this metalloid. Biosolid application at a rate of 100Mg ha(-1) caused an increase in arsenic bound to amorphous Fe and Al oxides and in the residual fraction, in Pintué soil. When Pintué soil was spiked with arsenic, aged for two months, and treated with biosolid (100Mg ha(-1)), the content of arsenic in the most labile fractions decreased, thus showing a favorable effect in its application to soils with few specific sites for arsenic adsorption. Arsenic speciation was carried out in the first two fractions of the sequential extraction procedure. As(V) was the main form in both fractions. Biosolid incorporation at a rate of 100Mg ha(-1) caused a significant increase in organic arsenic forms.     

Evaluating of arsenic(V) removal from water by weak-base anion exchange adsorbents

Arsenic contamination of groundwater has been called the largest mass poisoning calamity in human history and creates severe health problems. The effective adsorbents are imperative in response to the widespread removal of toxic arsenic exposure through drinking water. Evaluation of arsenic(V) removal from water by weak-base anion exchange adsorbents was studied in this paper, aiming at the determination of the effects of pH, competing anions, and feed flow rates to improvement on remediation. Two types of weak-base adsorbents were used to evaluate arsenic(V) removal efficiency both in batch and column approaches. Anion selectivity was determined by both adsorbents in batch method as equilibrium As(V) adsorption capacities. Column studies were performed in fixed-bed experiments using both adsorbent packed columns, and kinetic performance was dependent on the feed flow rate and competing anions. The weak-base adsorbents clarified that these are selective to arsenic(V) over competition of chloride, nitrate, and sulfate anions. The solution pH played an important role in arsenic(V) removal, and a higher pH can cause lower adsorption capacities. A low concentration level of arsenic(V) was also removed by these adsorbents even at a high flow rate of 250–350 h^?1. Adsorbed arsenic(V) was quantitatively eluted with 1 M HCl acid and regenerated into hydrochloride form simultaneously for the next adsorption operation after rinsing with water. The weak-base anion exchange adsorbents are to be an effective means to remove arsenic(V) from drinking water. The fast adsorption rate and the excellent adsorption capacity in the neutral pH range will render this removal technique attractive in practical use in chemical industry.     

Adsorption and desorption characteristics of hydrophobic pesticide endosulfan in four Indian soils

Adsorption and desorption characteristics of endosulfan in four Indian soils were studied extensively. The soils used were clayey soil (CL--lean clay with sand), red soil (GM--silty gravel with sand), sandy soil (SM--silty sand with gravel) and composted soil (PT--peat) as per ASTM (American Society for Testing and Materials) standards. Adsorption and desorption rates were calculated from kinetic studies. These values varied for alpha and beta endosulfan depending on the soil type. Maximum specific adsorption capacities (qmax) for different soils were calculated by Langmuir model. The values varied from 0.1 to 0.45 mg g(-1) for alpha endosulfan and 0.0942-0.2722 mg g(-1) for beta endosulfan. Maximum adsorption took place in clay soil followed by composted soil and red soil. Adsorptions of alpha and beta endosulfan were negligible in sand. The binding characteristics of various functional groups were calculated using Scatchard plot. Effect of functional groups was more predominant in clayey soil. Organic matter also played a significant role in adsorption and desorption of endosulfan. Endosulfan adsorption decreased drastically in clay soil when the pH was reduced. Desorption was higher at both acidic and alkaline pH ranges compared to neutral pH. Results indicated that alpha endosulfan is more mobile compared to beta endosulfan and mobility of endosulfan is maximum in sandy soil followed by red soil. It can be inferred that crystal lattice of the clay soil plays a significant role in endosulfan adsorption and desorption. Immobilization of endosulfan is more advisable in clay soil whereas biological and or chemical process can be applied effectively for the remediation of other soil types.