不同污染负荷土壤中镉和铅的吸附－解吸行为

采用一次平衡法,对3种不同污染负荷土壤Cd2 和Pb2 的吸附-解吸行为进行了比较.结果表明,低污染负荷土壤对Cd2 和Pb2 的吸附能力高于高污染负荷土壤.3种土壤对Cd2 的吸附等温线与Freundlich方程有较好的拟合性,Pb2 的等温吸附过程可用Langmuir方程与Freundlich方程来描述.双常数方程是描述这3种不同污染负荷土壤中Cd2 和Pb2 吸附动力学行为的最优模型,其次为Elovich方程,最差模型是一级动力学方程.Pb2 的解吸滞后现象较Cd2 明显.高污染负荷土壤的吸附态Cd2 、Pb2 解吸率高于低污染负荷土壤,Cd2 、Pb2 解吸量与其初始吸附量之间的关系符合二次幂方程.3种土壤Cd2 、Pb2 的解吸速率随重金属初始浓度的增加而增加,随解吸时间的延长而降低.     

土生鳞伞对Cd2+的吸附特性

以土生鳞伞（Pholiota terrestris Overh.）子实体为生物吸附剂吸附水溶液中的Cd2+,分析吸附剂用量、初始pH值、初始重金属浓度、反应时间这4个因素对吸附的影响,并采用Langmuir和Freundlich等温吸附模型及准一级、准二级动力学模型拟合土生鳞伞的生物吸附特性.结果表明:水溶液中Cd2+...     

黏土矿物中重金属离子的吸附规律及竞争吸附

采用等温吸附法,研究了重金属铜、铅、镉、镍在膨润土中的吸附特征,发现膨润土对铜、铅的吸附明显强于镉、镍,吸附强度大小顺序为Pb2 >Cu2 >Ni2 >Cd2 。Langmuir和Freundlich方程对这4种金属离子等温吸附的拟合均呈极显著关系。Pb2 、Cd2 、Ni2 分别与Cu2 的双组分竞争吸附表明,黏土矿物对4种离子具有"选择性吸附"。在Pb2 、Ni2 、Cd2 的存在条件下,黏土矿物对Cu2 的吸附产生不同程度的下降;100mg/LCu2 对Pb2 的影响不大,但可完全抑制Ni2 、Cd2 的吸附。建立了IAS和LCA模型来预测Pb2 与Cu2 的双组分竞争吸附,并对LCA模型进行修正,提出了更符合实际情况的竞争吸附模型。文章最后用LCA修正模型对Pb2 与Cu2 的双组分竞争吸附进行了模拟。     

红球菌HX-2所产胞外多糖的特性和对Cu2+的吸附

【背景】目前,微生物所产胞外多糖(exopolysaccharide,EPS)的理化性质及其在重金属吸附中的应用受到了广泛关注。【目的】研究红球菌HX-2所产胞外多糖的理化性质,并探究其对重金属的吸附情况。【方法】使用离子交换和凝胶色谱分离法对胞外多糖粗品进行纯化;利用苯酚硫酸法测胞外多糖中糖含量;用Bradford试剂盒检测胞外多糖中蛋白含量;使用甲醇萃取法检测胞外多糖中脂质含量;用高效液相色谱(high performance liquid chromatography,HPLC)法分析胞外多糖中单糖组成;用扫描电镜(scanningelectronmicroscopy,SEM)法观察多糖表面形态;通过等温吸附模型和动力学模型探究胞外多糖对重金属的吸附效果。【结果】测得胞外多糖主要成分EPS-G-1中总糖含量为78.43%,蛋白含量为8.31%,脂质含量为8.22%;纯化后胞外多糖中单糖组成为葡萄糖、甘露糖、半乳糖、葡萄糖醛酸和岩藻糖,质量比为27.31:26.67:24.83:15.85:4.80;通过等温吸附模型拟合得到HX-2所产胞外多糖对Cu~(2+)的最大吸附量为144.93 mg/g。【结论】红球菌HX-2所产胞外多糖对水体中Cu~(2+)具有良好的吸附作用,可用于工业废水中重金属离子的处理。     

出芽短梗霉菌JB16铅镉吸附特性的研究北大核心

【目的】本文对污染土壤中的耐重金属菌株进行分离鉴定,研究菌株在不同条件下对吸附铅镉的影响因素。【方法】通过生理生化特征及ITS序列分析确定菌株种属,采用平板划线法确定最大耐铅镉浓度并探究菌株吸附的最佳条件;通过准二级动力学、Langmuir和Freundlich等温吸附的模型及红外光谱探究吸附过程。【结果】菌落形态和ITS序列分析鉴定表明,筛选分离的JB16为出芽短梗霉菌(Aureobasidium pullulans),最大耐铅浓度达1500 mg/L,最大耐镉浓度达750 mg/L,最大耐铅镉混合浓度达1500 mg/L和300 mg/L。通过单因素实验(温度、时间、菌龄、pH、湿菌体浓度和初始重金属浓度)得出结论,在温度30℃、时间2 h、菌龄72 h、pH 6、湿菌体浓度5 g/L和初始铅浓度150 mg/L的最佳条件下,菌体对铅的吸附率为88.5%;在温度30℃、时间1 h、菌龄96 h、pH 6、湿菌体浓度5 g/L和初始镉浓度20 mg/L的最佳条件下,菌体对镉的吸附率为59.4%。菌株吸附铅镉过程符合Langmuir吸附模型和准二级动力学模型,为表面单分子层吸附。扫描电镜和红外光谱分析表明,重金属离子对菌体造成影响,吸附前后形态发生变化,细胞表面的羟基、羧基、饱和C−H键和酰胺基等基团参与了吸附过程。【结论】菌株JB16具有一定的铅镉吸附效果,为修复重金属铅镉污染的水体和土壤提供宝贵的菌种资源和数据支持。     

阴离子树脂分离橄榄苦苷的过程及性能研究

目前橄榄苦苷的分离、纯化研究主要集中在大孔吸附树脂,但鲜有阴离子树脂分离、纯化橄榄苦苷的报道。为了研究阴离子树脂(LX-68M)吸附、分离过程及性能,采用吸附动力学及等温吸附模型来研究阴离子树脂静态吸附、解吸橄榄苦苷的行为。结果表明阴离子树脂对橄榄苦苷的吸附符合准二级动力学模型(R²=0.993 4),Freundlich等温吸附模型(R²=0.964 2)。进一步通过动态实验优化阴离子树脂纯化橄榄苦苷工艺,最佳操作工艺为：上样浓度为0.25 g/mL,解吸液为45%乙醇,吸附、解吸速率均为2.0 BV/h。该条件下橄榄苦苷的吸附率、解吸率分别为86.86%、87.08%,纯度为52.33%。此外,阴离子树脂重复使用4次后吸附率为54.9%,经再生处理后,吸附率恢复到93.51%,表明其具有一定的工业化前景。阴离子树脂稳定性好、分离条件温和,适合用于橄榄苦苷及其他相似天然产物的分离纯化。     

耐性真菌HA吸附铅、锌的影响因素及吸附机理研

【目的】从铅锌矿区分离筛选出耐铅锌性菌株,并研究其吸附铅、锌的影响因素及吸附机理,为重金属污染微生物修复提供参考。【方法】以从铅锌矿区筛选出的耐铅锌真菌HA作为试验菌株,考察影响其对铅、锌去除能力的主要因素(初始浓度、pH、接种量),同时通过等温吸附模型、动力学分析及红外光谱分析探讨其相关的吸附机理。【结果】经鉴定,从矿区筛选的对Pb2+、Zn2+有较强耐性的菌株HA为米曲霉(Aspergillus oryzae);在初始铅、锌浓度的实验范围内(100-800mg/L),HA对铅、锌离子的去除率随着其初始浓度增加而减小,25h后HA的生长进入平稳期,且对铅、锌离子的去除率趋于稳定。当铅、锌初始浓度为100mg/L、pH为5.0时,HA对铅、锌离子的去除率均达到最高,分别为97.8%、54.1%;当HA接种量为1mL时,其对铅、锌去除率的增长率达到最大。HA对铅、锌的吸附过程满足Langmuir吸附模型,其吸附以单层吸附为主。在动态吸附过程中,HA对Pb2+、Zn2+离子吸附性能与准二级动力学吸附方程的拟合程度更高,且对Pb2+的吸附效果明显高于Zn2+。红外光谱分析表明,HA细胞中羟基、烷基、酰胺基、羰基、磷酸基等参与了Pb2+、Zn2+的吸附过程。【结论】HA是一株对铅、锌有较强吸附能力的真菌,其吸附铅、锌影响因素及吸附机理研究结果将为重金属污染微生物修复提供指导。     

大孔树脂对八月瓜果皮总三萜的吸附特性研究

研究XDA-1型大孔树脂对八月瓜果皮总三萜的吸附特性。采用准一级动力学方程、准二级动力学方程、Van't Hoff方程和吸附等温方程研究吸附动力学与吸附热力学参数。结果表明,XDA-1大孔树脂对八月瓜果皮中总三萜的吸附符合准二级动力学方程描述;吸附等温线符合Freundlich等温吸附方程;吸附焓变ΔH=-1.2792 kJ/mol,为物理吸附;吉布斯自由能ΔG0,吸附过程是自发过程;吸附熵变ΔS0,表明吸附是熵值增加的过程。     

三氯蔗糖在大孔吸附树脂SP825上的吸附热动力学

采用静态吸附法,系统研究了三氯蔗糖在大孔吸附树脂SP825上的吸附热力学和动力学特性,为后续三氯蔗糖提取工艺的设计提供基础数据。实验结果表明:在283.15、293.15和303.15 K温度下,树脂SP825对三氯蔗糖的最大吸附量(每克湿树脂)分别为0.146、0.151和0.156 g。树脂SP825对三氯蔗糖的吸附平衡数据符合Lang-muir吸附等温方程,吸附过程为自发的物理吸附过程;并运用准二阶动力学模型描述了动力学过程,确定在实验条件范围内,吸附受颗粒内部传质速率的影响。     

黑曲霉发酵菌渣对臧红T的吸附研究

将糖化酶发酵生产过程中产生的黑曲霉菌渣作为一种复合吸附剂进行了染料吸附研究,以挖掘其吸附潜力。首先对菌渣的理化性质进行了分析,然后以臧红T为模型染料,考察了几种因素(接触时间、溶液温度、吸附剂量、初始浓度和盐离子)对吸附的影响,并将所得数据用等温吸附方程、动力学方程和热力学方程进行了模型拟和。结果表明,吸附可在2 h内达到平衡,吸附过程符合准二级动力学模型,属于化学吸附,膜扩散模型比内扩散模型更适合解释吸附行为;温度对吸附有促进作用,吸附过程是一个自发的吸热反应;通过Langmuir方程可计算出最大单分子层吸附容量为166.67 mg/g,但Freundlich能更好的描述吸附行为,说明菌渣表面存在多个不同的吸附位点。此外,菌渣投加量和钠离子浓度均可影响吸附效果,染料去除率最高可达91%。     

小分子有机酸对恒电荷土壤胶体Pb2＋吸附-解吸的影响

供试土壤胶体对Pb²⁺吸附及吸附态Pb²⁺的解吸等温线均符合Freundlich和Langmuir等温式,吸附常数Ka值大小为塿土>黄绵土>黑垆土>黄褐土,其大小次序与表面总电荷密度σ0大小一致,表明了各土壤胶体对Pb²⁺吸附强度的大小,在小分子有机酸作用下,吸附量降低,吸附亲和力增加,柠檬酸的影响大于草酸的影响;解吸后残留Pb^2+吸附常数杨值的大小基本为塿土>黄褐土>黑垆土>黄绵土,反映了解吸残留Pb²⁺吸附强度的大小,与各土壤胶体有机质和游离氧化铁含量有关,在NaNO₃和草酸溶液中,吸附-解吸等温线相距较远,吸附-解吸之间存在着滞后性;在柠檬酸作用下,吸附-解吸等温线基本接近,二者之间具有一定的可逆性。     

Copper dissociation as a mechanism of fungal laccase denaturation by humic acid

Effects of humic acid on removal of hydroxy polychlorobiphenyls (PCBs) with laccase from Trametes versicolor were studied. In the absence of humic acid, hydroxy PCBs were rapidly degraded by laccase. However, the rate constants decreased with increasing humic acid concentration, the reactions being completely inhibited at 150 mg l^-1 of humic acid. Peroxidase from Arthromyces ramosus was not inhibited by the same treatment. The activity of humic acid-deactivated laccase was completely restored by copper ions (500 M of Cu²⁺ in 150 mg l^-1 of humic acid), but not by other metal ions (Zn²⁺, Fe²⁺ and Hg²⁺). Humic acid-deactivated laccase purified by gel permeation chromatography (GPC) showed no activity against 2,2-azino-bis(3-ethylbenzthiazoline sulfonic acid) diammonium salt and 3,5-dichloro-4-hydroxybiphenyl, but its activity was restored by copper ion treatment. Humic acid-deactivated laccase showed similar properties, such as GPC retention time and copper ion requirements for activity, to those of laccase deactivated by nitrilotriacetic acid. The extent of humic acid inhibition, expressed as activity non-recoverable by copper ion treatment, increased over time more rapidly than that of the humic acid-free control. These results suggest that short-term inactivation of laccase, i.e., less than 1 day, is attributable to a depletion of copper ion.     

Effects of humic materials on virus recovery from water.

Humic and fulvic acids were tested for their ability to interfere with virus recovery by microporous filters. Two electropositively charged types of filter (Seitz S and Zeta Plus 60S) were used to concentrate poliovirus in the presence of humic materials. Humic acid inhibited virus adsorption, but even at the highest humic acid concentrations tested (200 mg/liter), 30 to 40% of the virus was recovered by the filters. Fulvic acid, tested with Zeta Plus filters, did not affect virus recovery. For comparison, two electronegatively charged filter types were tested (Cox and Balston). These two types of filter were more sensitive to interference at lower concentrations of humic acid than the more positively charged filters. With Balston filters, at humic acid concentrations above 10 mg/liter, most of the virus was recovered in the filtrate. Fulvic acid, tested with Balston filters, did not interfere with virus recovery. With the electropositively charged filters, the humic materials adsorbed efficiently, even at high input concentrations. Interference with virus adsorption occurred at humic acid concentrations which were below the level of saturation of the filters. In addition, in high-volume experiments, humic acid led to premature blockage of the filters. The efficiency of virus recovery by a second concentration step, organic flocculation of the filter eluate, was tested. For all the filter types tested, this procedure was not affected by the presence of humic or fulvic acid in the input water.     

Effects of humic materials on virus recovery from water

Humic and fulvic acids were tested for their ability to interfere with virus recovery by microporous filters. Two electropositively charged types of filter (Seitz S and Zeta Plus 60S) were used to concentrate poliovirus in the presence of humic materials. Humic acid inhibited virus adsorption, but even at the highest humic acid concentrations tested (200 mg/liter), 30 to 40% of the virus was recovered by the filters. Fulvic acid, tested with Zeta Plus filters, did not affect virus recovery. For comparison, two electronegatively charged filter types were tested (Cox and Balston). These two types of filter were more sensitive to interference at lower concentrations of humic acid than the more positively charged filters. With Balston filters, at humic acid concentrations above 10 mg/liter, most of the virus was recovered in the filtrate. Fulvic acid, tested with Balston filters, did not interfere with virus recovery. With the electropositively charged filters, the humic materials adsorbed efficiently, even at high input concentrations. Interference with virus adsorption occurred at humic acid concentrations which were below the level of saturation of the filters. In addition, in high-volume experiments, humic acid led to premature blockage of the filters. The efficiency of virus recovery by a second concentration step, organic flocculation of the filter eluate, was tested. For all the filter types tested, this procedure was not affected by the presence of humic or fulvic acid in the input water.     

林业入侵植物假苍耳对Cu^2＋的吸附性

选取林业入侵植物假苍耳（Iva xanthifolia）叶片匀浆体（LSI）和茎匀浆体（SSI）作为生物吸附材料,考察了溶液pH值、吸附时间、Cu^2＋浓度对吸附性能的影响,确定了最佳吸附pH值为6．0-7．0,吸附平衡时间为30分钟,处理水体中的Cu^2＋浓度应不超过800mg·L^-1。采用Langmuir和Freundlich等温吸附模型进行线性拟合,推算出LSI和SSI的饱和吸附率分别为28．68mg·g^-1和13．06mg·g^-1。通过对吸附Cu^2＋前后的LSI和SSI进行傅立叶红外光谱和X射线衍射分析可知,假苍耳参与Cu。’吸附的主要物质是纤维素类和糖类,并且可能是由它们具有的-OH、-CONH2及-C=O等官能团提供结合位点。研究结果显示假苍耳有可能成为一种具有开发潜力的新型重金属生物吸附材料。     

Stability of Ca2+-, Cd2+-, Cu2+-[illite-humic] complexes and pH influence

Decomposition of fresh plant residues in soil is expected to produce humic fractions varying in molecular size. It was hypothesized that metal adsorption by soil, to some degree, will depend on humic acid content and molecular size. The latter is expected to vary in number and type of functional groups. In this study, illite-humic complexes were used to evaluate Ca²⁺, Cd²⁺, and Cu²⁺ adsorption and how this adsorption was affected by humic acids, differing in molecular size, under various pH values. Potentiometric titration using ion-selective electrodes with a stop-and-go procedure was employed to evaluate metal-[illite-humic] complex formation. The results showed that illite-humic complexes exhibited at least two types of metal-ion adsorption sites (low and high affinity) and molecular size of humic fractions had a large potential influence on total metal adsorption but a relatively smaller influence on metal-complex stability. Relative strength of metal-ion-[illite-humic] complexes followed the order of Cu²⁺>Cd²⁺>Ca²⁺ and were affected by pH, especially for low metal-ion affinity sites. Magnitude of metal-[illite-humic] stability constants, depending on molecular size of humic fraction and pH, varied on a log-scale from 3.52 to 4.21 for Ca²⁺, 4.38 to 5.18 for Cd²⁺and from 5.23 to 5.83 for Cu²⁺. There was an approximate 5-fold difference in these stability constants between the three different sizes of humic fractions. The larger the humic fraction, the lower the metal-[illite-humic] stability constant. This revised version was published online in June 2006 with corrections to the Cover Date. This revised version was published online in June 2006 with corrections to the Cover Date. This revised version was published online in June 2006 with corrections to the Cover Date.     

Uptake of Cr3+ from aqueous solution by lignite-based humic acids

Humic acid (HA) produced from brown coal, a relatively abundant and inexpensive material is currently being investigated as an adsorbent to remove toxic metals from aqueous solution. The influence of five parameters (contact time, solution pH, initial metal concentration, temperature and amount of adsorbent) on the removal at 20+/-1 degrees C was studied. HAs were prepared from lignites by using alkaline extraction, sedimentation and acidic precipitation. Adsorption equilibrium was achieved in about 60 min for Cr3+ ion. The Langmuir adsorption isotherm was used to describe observed sorption phenomena. The maximum adsorption capacity of 0.17 mmol for Ilgin (HA1), 0.29 mmol for Beysehir (HA2) and 0.18 mmol Ermenek (HA3) and 0.17 mmol of Cr3+/g for activated carbon (AC) was achieved, respectively at pH of 4.1. More than 84% of Cr3+ was removed by HA2, 54% by HA3 and 51% by HA1 and 50% by AC from aqueous solution. The adsorption was strongly dependent on pH but independent of ionic strength and metal ions. The adsorption of Cr3+ was higher between pH 4.1 and 5.1 for all HAs and maximum sorption was observed at pH 4.1. The rise in temperature caused a slight decrease in the value of the equilibrium constant (Kc) for the sorption of Cr3+ ion. Complex mechanisms including ion exchange, complexation and adsorption and size exclusion are possible for sorption of Cr3+ ion on HAs.     

Adsorption isotherms of lanthanum to soil constituents and effects of pH,EDTA and fulvic acid on adsorption of lanthanum onto goethite and humic acid

Abstract

La³⁺ adsorption isotherms to five soil constituents (quartz, feldspar, kaolinite, goethite and humic acid) are studied. EDTA, fulvic acid and pH effects are also investigated on the adsorption of lanthanum by goethite and humic acid because of their relative importance in affecting metal environmental behavior. Adsorption isotherms of La³⁺ to five constituents show differences in adsorption capacity and in shape in the studied range of La³⁺. These constituents can be classified according to their adsorption capacity: humic acid > goethite ≈ kaolinite > feldspar ≈ quartz. pH increase could promote humic acid and goethite adsorption of La³⁺ while EDTA could reduce the adsorption by these two adsorbents. Fulvic acid can reduce humic acid adsorption but has less effect on adsorption by goethite.     

Rodenticide-humic acid adsorption mechanisms and role of humic acid on their toxicity on human keratinocytes: chromatographic approach to support the biological data

Humic substances are the most important soil components affecting the behaviour and performances of herbicides in the soil-water-organism system. In this paper, a chromatographic approach was used for analysis of anticoagulant rodenticide-humic acid adsorption mechanisms. Using an equilibrium perturbation method, it was clearly shown that: (i) humic acid can be adsorbed on the C18 stationary phase, and (ii) all the rodenticides can be adsorbed on the humic acid adsorbed on the C18 stationary phase. This approach allowed the determination of the adsorption constant values between the anticoagulant rodenticides and humic acid as well as the corresponding thermodynamic data of this adsorption mechanism. The role of humic acid on the toxicity of these rodenticides on human keratinocytes was also clearly described in relation to these physico-chemical data.