共存物质对重金属絮凝剂MCC除镉性能的影响

为进一步拓展天然高分子絮凝剂壳聚糖的应用范围,以壳聚糖、L-半胱氨酸为原料,通过酰胺化反应制备一种具有重金属捕集功能的高分子重金属絮凝剂-2-氨基-3-巯基丙酰壳聚糖(MCC),研究了水体中常见的阴阳离子、有机配位剂及浊度对MCC除镉性能的影响,探讨了絮体形貌与絮体分形维数及絮凝除镉效果间的关系。结果表明,Na+、Cl-、NO-3、F-、SO2-4的存在对MCC除Cd2+均有促进作用,Ca2+表现为明显的抑制作用;低浓度的EDTA对除镉有促进作用,随着EDTA浓度的增大,逐渐转为抑制作用;低浓度的腐殖酸对MCC去除Cd2+有显著的促进作用;在一定范围内,浊度可促进MCC对Cd2+的去除;絮体间空隙越多,絮体分形维数越小,除镉效果越好。     

共存物质对重金属絮凝齐MCC除镉性能的影响

为进一步拓展天然高分子絮凝剂壳聚糖的应用范围，以壳聚糖、L-半胱氨酸为原料，通过酰胺化反应制备一种具有重金属捕集功能的高分子重金属絮凝剂-2-氨基-3-巯基丙酰壳聚糖（MCC），研究了水体中常见的阴阳离子、有机配位剂及浊度对MCC除镉性能的影响，探讨了絮体形貌与絮体分形维数及絮凝除镉效果间的关系。结果表明，Na＋、Cl-、N03、F-、SO4 2-的存在对MCC除Cd2＋均有促进作用，Ca2＋表现为明显的抑制作用；低浓度的EDTA对除镉有促进作用，随着EDTA浓度的增大，逐渐转为抑制作用；低浓度的腐殖酸对MCC去除Cd2＋有显著的促进作用；在一定范围内，浊度可促进MCC对Cd2＋的去除；絮体间空隙越多，絮体分形维数越小，除镉效果越好。     

几种阴阳离子对磷钨酸光催化降解甲基橙的影响

以磷钨酸为光催化剂，在紫外灯照射下，对甲基橙溶液进行光催化降解，考察了几种阴阳离子对磷钨酸光催化降解甲基橙溶液的影响。结果表明：Mg²⁺、Ca²⁺、NO^-₃、SO^2-₄和CO^2-₃均对催化活性有促进作用，其中Mg²⁺和Ca²⁺仅有微弱的促进作用；NO^-₃和SO^2-₄随着浓度的增加促进作用也有所增加；CO^2-₃则随着浓度的增加促进作用呈下降趋势；Mn²⁺、Al³⁺和Cl^-对光解反应存在较强的抑制作用，且Al³⁺和Cl^-随着其浓度的增加，抑制作用增强。     

绿色絮凝剂PAS的性能及混凝机理探讨

通过向聚硅酸中加入一种高价亲生物环保的金属离子Ti⁴⁺，制备了一种适合处理长江水的绿色絮凝剂PAS，并且通过实验确定了其处理长江水的最佳处理条件：酸性聚硅酸与Ti金属盐溶液复合，n_Ti/n_Si=0.3；投加量为10 mg/L（以Ti⁴⁺计），pH=6～8，UV254的去除率＞61.7％，浊度去除率＞99％。PAS的混凝效果明显优于聚合铝和聚硅铝，而且矾花形成迅速，絮体密实、沉降快、出水更加清澈，无残留铝。Ti也是亲生物金属，健康环保。因此，PAS是绿色环保友好型絮凝剂，可作为饮用水专用絮凝剂。观察所形成絮体的形貌以及观测红外光谱图均发现，絮凝剂对胶体颗粒污染物有较好的架桥网捕与络合反应作用。     

高分子重金属絮凝剂MCC制备及除铜去浊性能

以壳聚糖、L-半胱氨酸为原料,通过酰胺化反应制备了一种具有重金属捕集功能的高分子重金属絮凝剂-2-氨基-3-巯基丙酰壳聚糖(MCC)。以含铜废水为处理对象,通过正交实验研究了MCC的最佳制备条件,对其除铜性能进行了全面探讨,并对絮体形貌进行了观察和分析。结果表明,在最佳条件下制得的MCC具有除浊和捕集重金属离子双重功能,形成的絮体量较大、沉速快,出水水质好,重金属回收率较高,残渣稳定,不易造成二次污染,絮体分形维数越小,空隙越多,除铜效果越好。     

Ca(II)在活性污泥生物絮凝中的作用研究

采用4个平行的序批式反应器(SBR),研究了进水Ca²⁺浓度对活性污泥絮体表面特性和结构稳定性的影响，并由此来确定Ca²⁺在生物絮凝中的作用。结果表明：随着进水Ca²⁺浓度的增加，污泥中的Ca含量逐渐增大。进水中Ca²⁺的加入，增大了污泥絮体的粒径和密度，进而改善了污泥的沉降性能；Ca²⁺的加入，使可供结合的蛋白质数量最高增至近1倍，污泥表面疏水性也相应增强；污泥絮凝性能的改善，主要和可供Ca²⁺结合的蛋白质含量增加有关，而非多糖；EDTA通过络合污泥絮体中的Ca²⁺，破坏了由Ca²⁺架桥形成的污泥絮体结构，这说明Ca²⁺可通过和胞外聚合物（extracellular polymeric substances, EPS）中的负电官能团架桥来促进污泥絮体的形成并维持絮体结构的稳定性。     

原位水解生成的羟基氧化铁凝聚吸附除磷效能与机制简

将不同摩尔比Fe³⁺与OH^-（[Fe³⁺]：[OH^-]=1：0、1：1、1：2和1：3）反应获得原位水解生成的羟基氧化铁（in situ FeO_xH_y），研究了具有不同水解程度的羟基氧化铁对凝聚吸附除磷效能与机制。研究显示，In situ FeO_xH_y对磷的去除率随铁投量增大而升高，且均在中性pH范围内具有最佳除磷效果；在相同铁投量条件下，磷去除率随着[OH^-]：[Fe³⁺]的升高而降低；当体系碱度较低时（pH<6），引入OH^-可促进Fe³⁺水解而提高除磷效果。4种羟基氧化铁均可在15 s内可快速吸附磷，且吸附过程符合准二级动力学模型；Freundlich模型均可很好地描述磷在4种羟基氧化铁表面的吸附行为。磷酸盐吸附后，In situ FeO_xH_y表面Zeta电位明显降低，且[Fe³⁺]：[OH^-]为1：0的羟基氧化铁降低最为显著。结合MINITEQ计算软件磷酸盐、铁盐形态分析结果显示，对于碱度较低的体系，通过投加一定量OH^-可促进Fe³⁺水解，进而使得其更易与水中H₂PO₄^-与HPO₄^2-结合，生成具有多核羟基的磷酸铁络合物，进而提高除磷效果。     

水环境中腐殖酸与镉离子结合作用的影响因素

通过测定不同化学条件下腐殖酸与镉离子作用后的游离态镉离子浓度及其结合率，研究各因素对腐殖酸与镉离子作用的影响。研究结果表明，pH值、离子强度、投加镉离子总浓度、腐殖酸浓度和反应温度均影响腐殖酸与镉离子的结合。pH值在4.5~6.5范围内，随pH值升高，腐殖酸与Cd²⁺的结合率增大，游离态Cd²⁺浓度减少。溶液的离子强度增大对结合反应有抑制作用。投加Cd²⁺总浓度的增大会导致结合态Cd²⁺浓度和游离态Cd²⁺浓度逐渐增加，而其结合率逐渐减小。腐殖酸浓度逐渐增大，使Cd²⁺和腐殖酸的结合率逐渐增大。在20℃~50℃范围内时，随反应温度升高，游离态Cd²⁺浓度逐渐减小，其结合率逐渐增加。     

水体中常见无机阴离子对TiO2薄膜光催化降解甲醛的影响

选择了5种水体中常见的阴离子(Cl^-，SO^2-₄，HPO^2-₄/HPO^2-₄，HCO^-₃/CO^2-₃和NO^-₃)，分别考查了其对TiO₂薄膜光催化降解模拟甲醛废水的反应速率的影响；从上述离子的光吸收，对·OH的捕获及其生成的相应的无机自由基的氧化作用以及与甲醛的竞争吸附3个方面讨论了上述离子影响TiO₂薄膜光催化降解模拟甲醛废水的反应速率的原因。结果表明，HCO^-₃/CO^2-₃对TiO₂薄膜光催化降解甲醛具有抑制作用，Cl^-和SO^2-₄的影响不大，H₂PO^-₄/HPO^2-₄和NO^-₃具有促进作用。造成上述结果的主要原因是HCO^-₃/CO^2-₃具有很强的·OH捕获作用；Cl^-，SO^2-₄对·OH捕获作用以及竞争吸附都较弱；H₂PO^-₄/HPO^2-₄在TiO₂表面具有较强的吸附能力，释放出的H⁺起到了酸催化剂的作用；NO^-₃在紫外光的照射下可以产生·OH，此外NO^-₃作为电子受体而降低了TiO₂表面光生电子和空穴的复合几率。     

混凝法处理含铜电镀废水的实验研究

以FeSO₄、PAC作为絮凝剂去除低浓度电镀废水中的Cu^{2+，考察了絮凝剂投加量、溶液pH值、搅拌速度和时间等影响因素，结果表明，在各自最佳条件下，PAC和FeSO₄对Cu2+的去除可达到99.37%和99.20％，达到《污水综合排放标准》(GB 8978-1996)中一级排放标准。最后通过对FeSO₄、PAC和NaOH 3种药剂的综合分析和比较，发现FeSO₄絮凝处理低浓度电镀废水中的铜比PAC絮凝、NaOH沉淀法操作简单，污泥产生量少、工业应用性强而且去除率高。}     

Cadmium (Cd2+) removal by nano zerovalent iron: surface analysis, effects of solution chemistry and surface complexation modeling

Nano zerovalent iron (nZVI) is an effective remediant for removing various organic and inorganic pollutants from contaminated water sources. Batch experiments were conducted to characterize the nZVI surface and to investigate the effects of various solution properties such as pH, initial cadmium concentration, sorbent dosage, ionic strength, and competitive ions on cadmium removal by nZVI. Energy-dispersive X-ray and X-ray photoelectron spectroscopy results confirmed removal of Cd²⁺ ions by nZVI through adsorption. Cd²⁺ adsorption decreased in the presence of competitive cations in the order: Zn²⁺?>?Co²⁺?>?Mg²⁺?>?Mn²⁺?=?Cu²⁺?>?Ca²⁺?>?Na²⁺?=?K⁺. Higher concentrations of Cl^? significantly decreased the adsorption. Cadmium removal increased with solution pH and reached a maximum at pH 8.0. The effects of various solution properties indicated Cd²⁺ adsorption on nZVI to be a chemisorption (inner-sphere complexation) process. The three surface complexation models (diffuse layer model, constant capacitance model, and triple layer model) fitted well to the adsorption edge experimental data indicating the formation of nZVI–Cd bidentate inner-sphere surface complexes. Our results suggest that nZVI can be effectively used for the removal of cadmium from contaminated water sources with varying chemical conditions.     

电极-SBBR处理含铜有机污水

采用电极一SBBR系统去除Cu^2＋，考察了电流强度，IA竞争离子（阴离子SO4^2-、NO3^-、CL^-和阳离子Zn^2＋、Ph^2＋）、初始含Cu^2＋量及溶液pH值对除铜效除果的影响。结果表明，当电流强度为40mA时Cu^2＋去除率最高为98％。投加阴（SO4^2-、NO3^-、Cl^-）、阳（Zn^2＋、Pb^2＋）离子均会引起出水Cu^2＋浓度的增加，且Cl^-和Ph^2＋含量分别为45mg／L和30mg／L时对Cu^2＋去除的影响更为显著。进水Cu^2＋浓度为30mg／L时，Cu^2＋去除率最高为98．48％，当进水Cu^2＋≥70mg／L时，出水Cu^2＋浓度不能达标。酸性（pH4．0～4．5）与碱性（pH9．0～10．0）条件均不利于Cu^2＋的去除，且酸性条件的负面影响更显著．当pH为4．5～7．5时．Cu^2＋去除率最高为97．78％。     

Effect of Ca2+-ions on the absorption of Pb2+, Cu2+, Cd2+ and Zn2+ by humic substances

Distribution coefficients for the sorption of Pb²⁺, Cu²⁺, Cd²⁺ and Zn²⁺ by peat were determined as a function of the Ca²⁺-content of peat as well as of the Ca²⁺-concentration in the solution. The amount of heavy metal ions taken up was measured for Cu²⁺, Cd²⁺ and Zn²⁺ by atomic absorption spectrometry and for Pb²⁺ by using Pb-212 as a radioactive tracer.The results show that the distribution coefficients of the heavy metal ions increase, if one increases the initial ratio of the $\text{Ca}{}^{\mathrm{2+}}\text{H}{}^{\mathrm{+}}\text{-}\text{ions}$ in the peat phase. The distribution coefficients for the heavy metal ions decrease, however, if - at constant initial Ca²⁺-content of the peat - the Ca²⁺-concentration of the solution is increased.     

Influence of clay on the adsorption of heavy metals like copper and cadmium on chitosan

The influence of clay on the adsorption of heavy metals like copper and cadmium on chitosan from simulated industrial wastewater is evaluated. Chitosan–clay blend with ratio of (1:1), (1:2), and (2:1) have been prepared, and these were used as membranes to remove copper and cadmium ions from synthetic industrial wastewater. The chemical parameters for quantities of adsorption of heavy metal contamination have been done, and the kinetics of adsorption has also been carried out. Clay provides enough absorbable sites to overcome mass transfer limitations. The number of absorbable sites for cadmium is more compared to copper, and thus the rate of recovery of cadmium is faster than copper, and the percentage removal of cadmium is more than copper at all times on clay over nylon 6. This difference indicates the influence of clay in the adsorption of heavy metals in comparison to synthetic polymer nylon 6. Rate constant for first-order kinetics of adsorption, k ₁, for copper and cadmium is less than that of clay, which clearly indicates that clay, which is a natural polymer, is more kinetically favored compared to synthetic polymer. The difference in the intraparticle diffusion in both the natural and synthetic polymer is not much, and it suggests that the particle diffusion mechanism is the same in both cases. Copper and cadmium recovery is parallel at all times. The percentage of removal of copper increased with an increase in pH from 3 to 5. In the case of cadmium containing wastewater, the maximum removal of metal occurred at pH 5. The uptake amount of Cu²⁺ ions on chitosan increased rapidly with increasing the contact time from 0 to 360 min and then reaches equilibrium after 360 min, and the equilibrium constant for copper and cadmium ions are more or less the same for the adsorption reaction. There are more adsorption sites for cadmium in the presence of clay and mass transfer limitation is avoided without resorting to rotation, which is the highlight of the present work. And more so, this is pronounced in the case of natural polymer compared to synthetic polymer.     

Copper and cadmium removal from synthetic industrial wastewater using chitosan and nylon 6

Purpose

Chitosan with nylon 6 membranes was evaluated as adsorbents to remove copper and cadmium ions from synthetic industrial wastewater.

Methods

Chitosan and nylon 6 with glutaraldehyde blend ratio with (1:1+Glu, 1:2+Glu, and 2:1+Glu) have been prepared and these were used as membranes to remove copper and cadmium ions from synthetic industrial wastewater. Characterization of the synthesized membrane has been done with FTIR, XRD, TGA/DTA, DSC, and SEM. Chemical parameters for quantities of adsorption of heavy metal contamination have been done and the kinetics of adsorption has also been carried out.

Results

The optimal pH for the removal of Cd(II) and Cu(II) using chitosan with nylon 6. Maximum removal of the metals was observed at pH 5 for both the metals. The effect of adsorbent dose also has a pronounced effect on the percentage of removal of the metals. Maximum removal of both the metals was observed at 5 g/100 ml of the adsorbent.

Conclusion

Copper and cadmium recovery is parallel at all time. The percentage of removal of copper increased with increase in the pH from 3 to 5. In the case of cadmium containing wastewater, the maximum removal of metal occurred at pH 5. The uptake amount of Cu²⁺ ions on chitosan increased rapidly with increasing contact time from 0 to 360 min and then reaches equilibrium after 360 min; the equilibrium constant for copper and cadmium ions is more or less the same for the adsorption reaction.     

Competitive biosorption of lead, cadmium, copper, and arsenic ions using algae

The present study aims to evaluate the competitive biosorption of lead, cadmium, copper, and arsenic ions by using native algae. A series of experiments were carried out in a batch reactor to obtain equilibrium data for adsorption of single, binary, ternary, and quaternary metal solutions. The biosorption of these metals is based on ion exchange mechanism accompanied by the release of light metals such as calcium, magnesium, and sodium. Experimental parameters such as pH, initial metal concentrations, and temperature were studied. The optimum pH found for removal were 5 for Cd²⁺ and As³⁺ and 3 and 4 for Pb²⁺ and Cu²⁺, respectively. Fourier transformation infrared spectroscopy analysis was used to find the effects of functional groups of algae in biosorption process. The results showed that Pb²⁺ made a greater change in the functional groups of algal biomass due to high affinity to this metal. An ion exchange model was found suitable for describing the biosorption process. The affinity constants sequence calculated for single system was K _Pb > K _Cu > K _Cd > K _As; these values reduced in binary, ternary, and quaternary systems. In addition, the experimental data showed that the biosorption of the four metals fitted well the pseudo-second-order kinetics model.     

金属铁去除水中Cr6+的影响因素研究

研究Fe/Cr6+比值和不同浓度的NO3-、Cl-和SO42-对金属铁去除Cr6+效果的影响.结果表明,金属铁对水中Cr6+有很好的还原去除效果;当金属铁的使用量为Cr6+量的1/2000时,铁对Cr6+的去除效果较差且易失去活性,而当金属铁的使用量为Cr6+量的8 000倍时,铁对Cr6+的去除效果较好且其活性的持续...     

Quantitative assessment of the toxic effects of heavy metals on 1,2-dichloroethane biodegradation in co-contaminated soil under aerobic condition

1,2-Dichloroethane (1,2-DCA) is one of the most hazardous pollutant of soil and groundwater, and is produced in excess of 5.44 × 10⁹ kg annually. Owing to their toxicity, persistence and potential for bioaccumulation, there is a growing interest in technologies for their removal. Heavy metals are known to be toxic to soil microorganisms at high concentrations and can hinder the biodegradation of organic contaminants. In this study, the inhibitory effect of heavy metals, namely; arsenic, cadmium, mercury and lead, on the aerobic biodegradation of 1,2-DCA by autochthonous microorganisms was evaluated in soil microcosm setting. The presence of heavy metals was observed to have a negative impact on the biodegradation of 1,2-DCA in both soil samples tested, with the toxic effect being more pronounced in loam soil, than in clay soil. Generally, 75 ppm As³⁺, 840 ppm Hg²⁺, and 420 ppm Pb²⁺ resulted in 34.24%, 40.64%, and 45.94% increase in the half live (t_½) of 1,2-DCA, respectively, in loam soil, while concentrations above 127.5 ppm Cd²⁺, 840 ppm Hg²⁺ and 420 ppm of Pb²⁺ and less than 75 ppm As³⁺ was required to cause a >10% increase in the t_½ of 1,2-DCA in clay soil. A dose-dependent relationship between degradation rate constant (k₁) of 1,2-DCA and metal ion concentrations was observed for all the heavy metals tested, except for Hg²⁺. This study demonstrated that different heavy metals have different impacts on the degree of 1,2-DCA degradation. Results also suggest that the degree of inhibition is metal specific and is also dependent on several factors including; soil type, pH, moisture content and available nutrients.