一步法烟气浸锰-脱硫的工艺参数及机理

应用一步法烟气浸锰-脱硫的新工艺,考察烟气流量、烟气SO2浓度、吸收时间、液固比及浸出时间等工艺参数对烟气氧化脱硫效果的影响,并运用溶液化学原理,对SO2及Mn2 在溶液中的组分进行了计算,研究Mn2 液相催化氧化烟气脱硫的机理.在吸收液pH值5-6时,锰主要以Mn2 形态存在,Mn2 的存在强化了从HSO-3开始发生的SO2氧化反应.采用菱锰矿为原料,能有效地脱除含SO2烟气中的硫,在实现烟气脱硫的同时自动调节溶液的pH值,并可从浸出液中回收高价值的硫酸锰.在最佳的工艺条件下,仅一步吸收过程,取得了锰浸出率85%,含SO2烟气脱硫率70%以上的效果.     

二(2-乙基己基)磷酸络合萃取邻氨基苯酚的研究

以二(2-乙基己基)磷酸(D2EHPA)为萃取剂,研究稀释剂种类、萃取剂浓度、溶液的初始pH值、溶液中甲(乙)醇等因素对邻氨基酚(OAP)稀溶液分配比(D)的影响.结果表明:溶液的初始pH值在7左右时,D有最大值;D值随二(2-乙基己基)磷酸浓度的增大而提高,且在极性环境要优于惰性环境;甲(乙)醇是影响萃取结果的主要因素.     

阴离子交换树脂回收土壤淋洗液中的EDTA-Cd

以湖南株洲污染土壤作为研究对象,研究了Na-EDTA、NH_4-EDTA、Ca-EDTA在不同浓度下对土壤中Cd的去除效果,确定出适合的浓度与淋洗剂;并采用氯型717阴离子交换树脂对土壤淋洗液中的EDTA-Cd络合物进行吸附与回收试验,主要方法流程如下:采用静态法考察了固液比、pH值、时间、温度对树脂吸附EDTA-Cd络合物的影响,确定最佳吸附条件;采用上柱吸附法研究了在不同流速下穿透曲线的变化,确定树脂的穿透点;选取Fe_2(SO_4)_3多价金属盐溶液作为再生剂,对树脂中的EDTA-Cd络合物进行动态洗脱回收,测定出洗脱曲线与体积.随后进行连续5次吸附洗脱试验,探究树脂的再生性与树脂中EDTA-Cd络合物的回收效果.结果表明,在浓度为2.5 mmol·L~(-1)时,Na-EDTA、NH_4-EDTA、Ca-EDTA溶液对土壤中的Cd具有较好的去除效果,其去除率分别为64.75%、66.11%、68.29%.另外,在静态吸附过程中,随着固液比增加,树脂对EDTACd的吸附效率减少,在pH值为5.6时,对EDTA-Cd络合物吸附效率达到93.53%,树脂达到吸附平衡所需的时间为30—45 min,最佳反应温度区间为25—35℃;在动态吸附回收过程中,当上柱流速为4 m L·min~(-1)时,树脂达穿透点所需EDTA-Cd络合溶液为650 m L;再生剂Fe_2(SO_4)_3的洗脱体积为60 m L,洗脱溶液与吸附EDTA-Cd络合物溶液的体积比例达到1∶10.经过连续5次吸附洗脱试验后,树脂对EDTA-Cd络合物的去除率和再生率分别达到76.64%—93.43%、75.65%—84.19%.利用氯型717阴离子交换树脂提取以及回收土壤淋洗液中EDTA-Cd络合物是可行的.     

聚丙烯中空纤维膜萃取水溶液中铜离子的研究

研究了聚丙烯中空纤维膜萃取二(2-乙基己基)膦酸(D2EHPA)水溶液中铜离子的工艺条件.结果表明,两相流速、膜面积对萃取率基本无影响;而水溶液的pH值和有机相初始铜离子浓度的改变使萃取率在40%-99%之间变化.整个萃取过程的传质阻力主要来源于D2EHPA和 Cu2 的界面配位络合反应阻力,铜浓度比较高时,传质阻力与铜浓度无关;而当铜浓度降低时,传质阻力随着铜浓度的降低而增大.     

废碱锰电池焙烧干粉中Mn2+浸出行为的研究

研究了废碱性锌锰电池焙烧干粉(BakePowderofSpentAlkalineZincManganeseBattery,简称SLR干粉)在硫酸体系中的酸解行为,分析了硫酸浓度、反应温度、催化剂用量和固液比对SLR干粉中Mn2+浸出率的影响,探讨了在硫酸体系中Mn2+的浸出行为。试验数据表明:硫酸浓度和催化剂用量对反应影响较大,同时得出了最佳的酸解反应条件:硫酸浓度10%、反应温度40℃、催化剂用量2%(体积比)、固液比1:10和反应时间2h。在此条件下Mn2+浸出率达87%以上,为进一步回收利用废碱性锌锰电池提供理论依据。     

澳门城市垃圾焚烧底灰的重金属淋溶及其遗传毒性评价

应用美国国家环境保护局推荐的毒性特性溶出程序(toxicitycharacteristicleachingprocedure,TCLP),以及ICP-MS和ICP-AES技术研究了澳门城市垃圾焚烧底灰中重金属的淋溶,并结合蚕豆根尖微核试验评价了其潜在的生态与健康风险.结果显示,该底灰淋溶出来的重金属元素:铝(Al)、锰(Mn)、钴(Co)和汞(Hg)的浓度低于0.01mg·L-1,铁(Fe)、铜(Cu)和钼(Mo)的浓度低于0.1mg·L-1,而铬(Cr)、锌(Zn)、硒(Se)、锶(Sr)、钡(Ba)和铯(Cs)的浓度在0.11mg·L-1￣2.19mg·L-1之间.需要注意的是淋溶液中铅(Pb)的浓度异常高,最高可达19.06mg·L-1,超过了美国相关标准的上限(5mg·L-1);对比不同条件下底灰中重金属的淋溶情况,表明溶解作用和淋溶液的pH值是影响其淋溶的2个重要因素.蚕豆根尖微核试验显示各淋溶液处理组根尖细胞微核率明显升高,与阴性对照组相比具有显著性差异(p<0.05),表明各淋溶液具有遗传毒性;随着淋溶液中重金属浓度的增加,蚕豆根尖细胞所表现出来的毒性效应增强,表明重金属是淋溶液具有遗传毒性的重要原因.     

正辛醇萃取苯酚稀溶液的特性研究

为探索工业含酚废水处理的适宜萃取剂，进行了正辛醇萃取苯酚稀溶液的实验研究，测定了不同pH值和苯酚初始浓度条件下的萃取平衡数据，萃残液CODCr值，分析了萃残液中CODCr值的来源。综合考虑萃取剂的萃取能力和产生的CODCr值，提出了酸性和中性溶液为正辛醇处理苯酚废水的适宜操作条件。以正辛醇为萃取剂对工业含酚废水进行了错流萃取实验，论证了其应用的可行性。     

氧化锌表面的Fe(Ⅱ)对三氯乙烯的还原脱氯研究

通过批量实验研究了在氧化锌-Fe(Ⅱ)混合体系中,束缚在氧化锌表面的Fe(Ⅱ)对三氯乙烯的还原脱氯作用。结果表明,这种束缚在氧化锌表面的Fe(Ⅱ)对三氯乙烯有一定的还原脱氯作用,且脱氯反应符合准一级反应动力学方程。与均质溶液中的Fe(Ⅱ)相比,束缚在氧化锌表面的Fe(Ⅱ)对三氯乙烯有更强的还原脱氯作用。实验还发现三氯乙烯在氧化锌-Fe(Ⅱ)混合体系中的还原脱氯速率受pH值和Fe(Ⅱ)浓度的影响。Fe(Ⅱ)浓度为1mmol·L-1,在pH值5.0～9.0范围内,还原脱氯反应速率常数kobs及三氯乙烯去除率随着pH值的升高而增大。维持pH值7.0不变,在Fe(Ⅱ)浓度1～4mmol·L-1范围内,kobs及三氯乙烯去除率随Fe(Ⅱ)浓度的增大而增大,但是Fe(Ⅱ)浓度进一步升高,kobs及三氯乙烯去除率反而降低。当Fe(Ⅱ)初始浓度为4mmol·L-1、pH=7.0时,三氯乙烯在氧化锌-Fe(Ⅱ)混合体系中的kobs及三氯乙烯去除率均达到最大值,分别为0.260h-1、71.7%。     

纤维膜三相液相微萃取在测定偶氮染料降解产生芳香胺中的应用

采用纤维膜保护的三相液相微萃取（HF-LLLME）技术,对偶氮染料在人工汗液和光辐照协同作用下降解产生致癌芳香胺的分析方法进行了研究.选用苯胺、邻甲苯胺、对氯苯胺和对硝基苯胺的汗液混合溶液进行模拟样品预处理,以正辛醇为有机萃取相,在供体相pH值为9,NaC l浓度为200.gL-1,接收相为pH=1的盐酸水溶液,萃取时...     

中空纤维膜辅助离子液体液相微萃取-高效液相色谱法测定环境水体中的水杨酸

分别以l-辛基-3-甲基咪唑六氟磷酸离子液体([C8MIM][PF6])和三辛基氧化膦(TOPO)作为萃取剂与辅助萃取剂,建立了中空纤维膜辅助的两相液液微萃取-高效液相色谱测定环境水体中水杨酸(Salicylicacid,SA)的新方法.通过对中空纤维膜种类、萃取剂、供体相体积、供体相pH、离子强度和萃取时间相关参数进行优化,获得了较高的富集倍数(1653倍).方法的检出限为0.1μg.L-1,线性范围为0.5—1000μg.L-1.方法对实际样品的加标回收率为89.6%—102.4%,可应用于环境水体中痕量SA的测定.     

PERCOLATION OF LEAD(II) AND CADMIUM(II) THROUGH TWO BENTONITES USED AS LANDFILL LINER

In order to prevent contamination of subsoil and groundwater by leachates containing heavy metals, montmorillonite linings are used on landfill bottoms. It is therefore important to understand ion uptake by this clay. In this study we have performed percolation of lead(II) and cadmium(II) through columns filled firstly with a technical bentonite and then with a reference bentonite. Elution curves provide an evaluation of metals retention. After the percolation step, columns are cut and metal ions are extracted to evaluate influence of side effects and soil depth on metal uptake. Moreover retentions of lead(II) and cadmium(II) are compared.     

CuO和Cu(Ⅱ)催化臭氧氧化的研究

以乙二酸为实验对象,研究了CuO/Al_2O_3和Cu(II)对臭氧的催化作用实验结果表明,在低pH条件下,CuO/Al2O3有较强的催化臭氧氧化能力,可以将乙二酸的去除率提高约15%而在中性条件下,20g·l-1CuO/Al2O3的催化效果有限磷酸盐缓冲液可以强烈抑制臭氧氧化乙二酸以及CuO/Al2O3的催化作用与CuO/Al2O3相比,Cu(II)离子有更强的催化臭氧氧化乙二酸的能力     

Impact of Ni(II), Zn(II) and Cd(II) on biogassification of potato waste

A study was conducted on anaerobic digestion of potato waste and cattle manure mixture, inoculated with 12% inoculum and diluted to 1:1 substrate water ratio at 37 +/- 1 degrees C. Initially pH of substrate was found to be 4.5 to 5.0. Lime and sodium bicarbonate solutions were employed to adjust the pH to 7.5. Biogas production continued up to 10 and 7 days, when lime and sodium bicarbonate solutions were used to adjust the pH, respectively. Biogassification potential was studied in response to different ratio of waste and cattle manure. Biogas production rate was higher when potato waste and cattle manure were used in 50:50 ratio. Effect of two different concentrations (2.5 and 5.0 ppm) of three heavy metals viz. (Ni (II), Zn (II) and Cd (II)) on anaerobic digestion of substrate (potato waste--cattle manure, 50:50) was studied. At 2.5 ppm, all the three heavy metals increased biogas production rate over the control value. The percentage increase in biogas production over the control was highest by Cd, followed by Ni and Zn. In all the treatments, methane content of biogas increased with increase in time after feeding. Various physico-chemical parameters viz. total solids, total volatile solids, total organic carbon and chemical oxygen demand considerably declined after 7 days of digestion and decline was greater in presence of heavy metals as compared to control. The physico-chemical parameters revealed maximum decrease in the presence of 2.5-ppm concentrations of heavy metals with the substrate. Among all the three heavy metals employed in the study, Cd++ at 2.5 ppm was found to produce maximum biogas production rate. The use of three heavy metals to enhance biogas production from potato and other horticultural waste is discussed.     

Effect of Ca(II), Fe(II), and Fe(III) on Cu(II) adsorption by a polyvinylidene fluoride-based chelating membrane from Cu(II)–EDTA complex solution

A polyvinylidene fluoride-based membrane bearing the diethylenetriaminepentaacetic acid chelating group was employed to recover Cu(II) from the Cu(II)-ethylenediaminetetraacetic acid complex aqueous solution. Effects of Ca(II), Fe(II), and Fe(III) on Cu(II) uptake were investigated by static batch adsorption tests and dynamic adsorption filtration. Isotherms, kinetics, and breakthrough curves of Cu(II) uptakes in the presence of the three cations at concentrations of 1 mmol L^?1 were elucidated. The three cations showed a positive effect on the Cu(II) uptake; the stimulative roles were in the order of Fe(III) > Fe(II) > Ca(II). They did not alter the adsorption behavior of the membrane; adsorption isotherms and kinetics could be described by Langmuir and Lagergren second-order models, and Cu(II) adsorption was a spontaneous and exothermic process. The presence of Ca(II), Fe(II), and Fe(III) increased the sorption capacity of the membrane stack by 1.3, 1.9, and 3 times. Breakthrough time and the exhaustion time of membrane stacks were also extended.     

Influence of complexation on lead(II) and cadmium(II) percolation through a clay liner

Wastes are usually stocked in waste disposals without any pre-treatment. Runoff waters lead to the formation of leachates containing mineral and organic pollutants. In order to prevent groundwater contamination, a double barrier is placed on the landfill bottom. The first one is an active barrier made up of a draining system and a geomembrane, and the second one, consisting of a clay liner allowing pollutant retention, is considered as a passive system. The aim of this work is to evaluate the complexation impact on the organic and inorganic retention. Percolations on columns filled with clay are performed, which allow a better knowledge of the transfer of metallic pollutants, complexed or not, through a model porous media, considering charge and conditional stability of complexes.     

Percolation of Lead(II) and Cadmium(II) through two bentonites used as landfill liner

In order to prevent contamination of subsoil and groundwater by leachates containing heavy metals, montmorillonite linings are used on landfill bottoms. It is therefore important to understand ion uptake by this clay. In this study we have performed percolation of lead(II) and cadmium(II) through columns filled firstly with a technical bentonite and then with a reference bentonite. Elution curves provide an evaluation of metals retention. After the percolation step, columns are cut and metal ions are extracted to evaluate influence of side effects and soil depth on metal uptake. Moreover retentions of lead(II) and cadmium(II) are compared.     

Influence of complexation on lead(II) and cadmium(II) percolation through a clay liner

Wastes are usually stocked in waste disposals without any pre-treatment. Runoff waters lead to the formation of leachates containing mineral and organic pollutants. In order to prevent groundwater contamination, a double barrier is placed on the landfill bottom. The first one is an active barrier made up of a draining system and a geomembrane, and the second one, consisting of a clay liner allowing pollutant retention, is considered as a passive system. The aim of this work is to evaluate the complexation impact on the organic and inorganic retention. Percolations on columns filled with clay are performed, which allow a better knowledge of the transfer of metallic pollutants, complexed or not, through a model porous media, considering charge and conditional stability of complexes.     

Biosorption of Cu(II) and Zn(II) onto a lignocellulosic substrate extracted from wheat bran

We studied the removal of copper and zinc ions from aqueous solutions using a lignocellulosic substrate obtained by an acido-basic treatment of wheat bran. The sorption capacity of this material was investigated through batch and column experiments. Batch experimental results showed that the retention capacity of the lignocellulosic substrate was 0.20×10^–3 mol g^–1 at pH 4.5 for copper(II) and 0.24×10^–3 mol g^–1 at pH 6.5 for zinc(II). Column experiments showed a reduced sorption capacity for both ions compared to batch experiments. Batch and column data were analysed using the Langmuir equation in order to determine the affinity constant and the binding capacity of the sorbent and to compare both retention processes.     

Comparative adsorption of Pb(II) and Cd(II) ions on chestnut shell in aqueous system

In this study, high capacity Chestnut shell, a waste product from the chestnut sugar production industry, was successfully applied to remove Pb (II) and Cd (II) ions from aqueous solutions. Maximum adsorption capacities were found as 541.25?mg/g and 75.86?mg/g for Pb(II), and Cd(II) respectively. Several important parameters influencing the adsorption of Pb(II) and Cd(II) ions such as contact time, pH, temperature and effect of metal concentration were investigated systematically by batch experiments. Langmuir and Freundlich adsorption models were used to describe adsorption isotherms and constants. The thermodynamic parameters, such as standard free energy (ΔG°), standard enthalpy (ΔH°), and standard entropy (ΔS°), of the adsorption process were calculated. The adsorbents were characterised by scanning electron microscopy. It has been observed from the experimental results that in case of both Cd (II) and Pb (II), pseudo 2nd order kinetic model. From the results, Chestnut Shell are considered as an effective, low cost and environmental friendly adsorbent for the removal of Pb (II) and Cd (II) from wastewater.     

Biosorption of chromium(VI), nickel(II) and copper(II) ions from aqueous solutions using Pithophora algae

The biosorption of heavy metals is considered to be one of the best alternatives for the treatment of wastewater. The metal binding capacity of algae and acid-treated algae is investigated to find out the removal characteristics of Cr(VI), Ni(II) and Cu(II) ions from single metal solutions. Batch experiments are conducted and the study is extended to investigate the effect of pH, amount of adsorbent and adsorbate concentration on the extent of biosorption. The results indicate that the adsorption capacity of algae depends strongly on pH. The maximum adsorption of Cr(VI), Ni(II) and Cu(II) occurs at pH values of 2, 7 and 4.3, respectively. The adsorption process follows first-order kinetic equation. The data obtained are correlated with Freundlich and Langmuir adsorption isotherms.