Rapid degradation of hexachlorobenzene by micron Ag/Fe bimetal particles

The feasibility of the rapid degradation of hexachlorobenzene (HCB) by micron-size silver (Ag)/iron (Fe) particles was investigated.Ag/Fe particles with different ratios (0,0.05%,0.09%,0.20%,and 0.45%) were prepared by electroless silver plating on 300 mesh Fe powder,and were used to degrade HCB at different pH values and temperatures.The dechlorination ability of Fe greatly increased with small Ag addition,whereas too much added Ag would cover the Fe surface and reduce the effective reaction surface,thereby decreasing the extent of dechlorination.The optimal Ag/Fe ratio was 0.09%.Tafel polarization curves showed that HCB was rapidly degraded at neutral or acidic pH,whereas low pH levels severely intensified H2 production,which consumed the reducing electrons needed for the HCB degradation.HCB degradation was more sensitive to temperature than pH.The rate constant of HCB dechlorination was 0.452 min-1 at 85℃,50 times higher than that at 31℃.HCB was degraded in a successive dechlorination pathway,yielding the main products 1,2,4,5-tetrachlorobenzene and 1,2,4-trichlorobenzene within 2 hr.     

Fe3O4稳定化纳米Pd/Fe对水中2,4-D的催化还原脱氯研究

采用四氧化三铁(Fe3O4)稳定化纳米Pd/Fe催化脱氯水溶液中的2,4-二氯苯氧乙酸(2,4-D),获得了良好的处理效果.实验考察了Fe3O4投加量、pH、钯化率、温度、搅拌速率等因素对2,4-D去除的影响.2,4-D去除率随Fe3O4投加量增加而提高,投加量为4.0 g·L-1时,反应210 min后,2,4-D去除率为93.5%,而未稳定的纳米Pd/Fe,去除率为47.3%.低pH可促进2,4-D还原脱氯,pH为2.6~4.1时,2,4-D在110 min内几乎完全去除.2,4-D去除率随钯化率增加而提高.随着钯化率由0.25%、0.50%增加到0.75%,210 min后,2,4-D的去除率也由51.4%、93.5%提高到99.9%.温度在16.5~30.0℃范围内,反应210 min后,2,4-D去除率均可超过90.0%.温度升高到35.0、40.0℃时,去除率显著下降.2,4-D去除率随着搅拌速率加快而提高.Fe3O4的加入可以使纳米Pd/Fe分散和稳定.此外,Fe0可通过Fe3O4将电子传递给H+和2,4-D,促进2,4-D的还原脱氯.     

CMC改性纳米Fe/Cu双金属模拟PRB去除地下水中2,4-二氯苯酚

使用羧甲基纤维素钠（CMC）对纳米零价铁（NZVI）改性,并将铜（Cu）作为复合金属,制得改性纳米Fe/Cu双金属.同时采用模拟反应柱模拟可渗透反应墙（PRB）去除地下水中2,4-二氯苯酚（2,4-DCP）的反应过程.改性前后材料的表征以及沉降实验结果表明,改性后的材料有更强分散性.通过考察污染物浓度、材料投加量、Cu的负载率、pH值、流量等因素对降解2,4-DCP的影响,结果表明：反应过程符合一级动力学模型,较低的pH值与较小的流速以及10%的Cu负载率有利于2,4-DCP脱氯,过多的材料投加量和过高的初始2,4-DCP浓度不利于其脱氯.     

针铁矿、磁铁矿和石膏对2,4-二氯苯酚厌氧降解的影响

2,4-二氯苯酚(2,4-dichlorophenol,2,4-DCP)常用于农药生产,在水体和土壤中广泛分布,具有难降解、高毒性的特点.通过模拟自然过程,在厌氧反应体系中投加铁氧化物和硫酸盐矿物,重点考察了不同矿物对2,4-DCP降解的影响.结果发现,厌氧体系中针铁矿、磁铁矿和石膏对2,4-DCP均没有明显的吸附作用;质量衡算结果表明所有反应体系中仅发生2,4-DCP向4-氯苯酚(4-chlorophenol,4-CP)的转化;与无外加碳源组相比,乙酸钠的加入使得2,4-DCP的还原脱氯反应速率增大一倍.分析表明针铁矿和磁铁矿加入可刺激脱氯功能菌的生长或活性,进而提高微生物的电子传递能力和2,4-DCP的降解速率;石膏加入强烈抑制脱氯功能菌的生长或活性,进而抑制2,4-DCP的降解.研究结果对认识难生化降解卤代酚在厌氧环境中的迁移转化及环境工程中此类物质的处理具有潜在意义.     

CMC改性的纳米Fe/Cu双金属去除2,4-二氯苯酚的研究

为解决纳米零价金属在水中暴露出的极易聚集与氧化的问题,本研究使用铜作为纳米零价铁(NZVI)的复合金属,制得纳米Fe/Cu双金属,并用羧甲基纤维素钠(CMC)对其包覆改性.使用扫描电子显微镜、X射线衍射以及氮气吸附/脱附等温线对改性前后的双金属进行表征.结果表明,改性之后的材料具有更大的尺寸以及比表面积,且抗氧化性得到显著增强.材料的沉降实验以及对2,4-二氯苯酚(2,4-DCP)降解实验的结果揭示,CMC的包覆比对改性后双金属的分散性与反应活性影响较大.当包覆比为80%时,双金属的分散稳定性最强,释放的活性位点个数最多,表现为最高的反应活性.此时脱氯效率达到90.3%,且脱氯过程和产物发生明显改变.     

纳米级Pd/Fe-MWCNTs-Fe3O4体系对2,3-DCB的降解研究

为有效抑制纳米级Pd/Fe颗粒的团聚和钝化及改善磁分离效果,以多壁碳纳米管(MWCNTs)和磁性纳米级Fe_3O_4颗粒为载体,在超声波辐照下利用液相还原法制备纳米级Pd/Fe-MWCNTs-Fe_3O_4颗粒,并采用XRD、TEM、SEM、EDX及BET表征其物性,最后以2,3-二氯联苯(2,3-DCB)为目标污染物,探究其对2,3-DCB还原脱氯的影响因素、降解机理和动力学.结果表明:制备的纳米级颗粒粒径均匀、分散性好、比表面积大;体系中纳米级Pd/Fe投加量、钯化率、纳米级Fe_3O_4投加量、MWCNTs投加量、反应温度、溶液初始pH及共存阴离子均会对2,3-DCB的降解效果产生明显影响;本研究推测出纳米级Pd/Fe-MWCNTs-Fe_3O_4体系对2,3-DCB的降解机理,发现其降解符合拟一级动力学关系.     

基于零价铁的双金属体系对六氯苯还原脱氯研究

利用Ag、Pb和Cu作为催化金属与微米级铁粉制成不同的双金属体系还原脱氯六氯苯(hexachlorobenzene,HCB),探讨不同催化金属种类、不同双金属添加量以及不同离子强度3种因素对HCB脱氯效率的影响,并剖析双金属催化条件下HCB的脱氯规律.结果表明,微米级铁粉对HCB几乎无还原脱氯效果,添加Ag、Pb和Cu对HCB均具有良好的催化脱氯能力,当Ag/Fe、Pb/Fe和Cu/Fe的最佳比例分别为0.2%、0.5%和1%时,反应2 h后HCB的脱氯率分别达到93.5%、88.5%和49.6%;同时,由于催化金属均匀附着在零价铁表面可以形成更多的微型原电池,故增加双金属投加量可有效提高HCB脱氯速率,0.1 g Pb/Fe对HCB脱氯率为38.3%,而0.8 g Pb/Fe对HCB脱氯率可达到88.6%;另外,离子强度增大对HCB的脱氯也有一定促进作用,在Na2SO4浓度分别为0、0.05和0.5 mol·L-1的3个反应器中,反应2 h后HCB脱氯率分别达到93.5%、98.0%和98.9%.     

氯酚溶液的γ辐照还原降解研究

氯酚由于氯取代基产生的诱导效应,使其容易受到亲核粒子的攻击而被还原降解.通过测定γ辐照前后氯酚母体、Cl-离子以及反应中间产物的浓度变化,研究了4种氯酚水溶液(4-CP、2-CP、2,4-DCP、2,4,6-TCP)与水合电子ea-q反应的降解脱氯过程.结果表明,在水合电子ea-q还原体系中,4种氯酚的降解脱氯顺序依次为:2,4,6-TCP>2,4-DCP>2-CP>4-CP,多氯酚比单氯酚容易降解脱氯,邻位上的氯原子要比对位上的氯原子更容易去除,苯酚和Cl-是氯酚反应降解的最终产物.另外,4种氯酚的降解和脱氯过程皆遵循一级反应动力学特征,4-CP、2-CP、2,4-DCP和2,4,6-TCP的降解反应常数分别是0.154、0.253、0.750和1.188 kGy-1,脱氯反应常数分别为0.137、0.219、0.251和0.306 kGy-1.     

Relation between mechanochemical dechlorination rate of polyvinyl chloride and mill power consumption

A sample of polyvinyl chloride (PVC) powder was milled with CaO powder in a planetary mill for various mill operational parameters. The milled product consisted of dechlorinated hydrocarbon and water-soluble CaOHCl. The dechlorination rate of PVC was determined by the concentration of Cl⁻ ions measured in solution after dispersing the milled product in water. To evaluate the power consumption during PVC dechlorination, the mill power consumption was measured during each experimental run. In addition, media motion during planetary milling was simulated using the discrete element method (DEM), enabling calculation of the mill power consumption. The power consumption calculated by the DEM simulation compared well with the power consumption measured experimentally. The dechlorination rate correlated well with the specific mill power consumption, regardless of the sample weight. The dechlorination rate of PVC when milled with oyster shells (CaCO₃) was observed to be faster than that of the PVC/CaO system, and oyster shells could be used as a reactant for the treatment of PVC wastes. This work should be useful for the design of a reactor for the dechlorination of PVC. Chemical Feedstock Recycling & Other Innovative Recycling Techniques 6     

Reductive dechlorination of polychlorinated dibenzo-p-dioxins by zerovalent iron in subcritical water

A new method for reductive dechlorination of polychlorinated dibenzo-p-dioxins (PCDDs) and remediation of contaminated soils is described that uses zerovalent iron as the dechlorination agent and subcritical water as reaction medium and extractive solvent. It is found that the zerovalent iron can be applied for stepwise dechlorination of octachlorinated dibenzo-p-dioxin (OCDD) on various matrixes in subcritical water. By using iron powder as matrix higher chlorinated congeners were practically completely reduced to less than tetra-substituted homologues. A significant part of residual OCDD, when it was spiked in to soils, and formed less chlorinated congeners are extracted with water in the given conditions. The solubility of OCDD was increased by a 4–6 orders over its solubility at ambient conditions. The new method of contentious-flow extraction is described.