铬(Ⅵ)污染高岭土电动修复实验研究

用电动方法对铬(Ⅵ)污染高岭土的修复进行了实验室研究。选用重铬酸钾作为污染物,配制的高岭土的重铬酸钾质量分数为100mg·kg-1。实验研究了铬(Ⅵ)污染高岭土电动修复的可行性,施加电压和处理时间对去除效率的影响,阴极电解产生的OH-对去除效率的影响及其控制方法,以及铬的迁移和分布规律。实验结果表明,电动修复可以有效去除高岭土中存在的铬(Ⅵ),最高去除效率可达97.8%;高岭中六价铬[Cr(Ⅵ)]以含氧阴离子形式存在,在电动修复过程中向阳极区域迁移;用蒸馏水冲洗和醋酸中和阴极电解产生的OH-,可以提高铬的去除效率。     

由电镀含铬废水合成吡啶酸铬(Ⅲ)的研究

本文对电镀含铬废水进行了处理,采用电镀含铬废水合成了有机铬饲料添加剂-吡啶酸铬（Ⅲ）,同时采用电导、紫外、红外光谱对吡啶酸铬的性质进行了研究。     

陕西某地区地下水Cr(Ⅵ)异常的水化学特征及其富集因素分析

以42组水化学测试数据为基础,结合野外调查资料,分析研究区Cr(Ⅵ)异常地下水的分布规律和水化学特征,探讨Cr(Ⅵ)富集的影响因素.结果表明Cr(Ⅵ)异常地下水主要位于基岩含水层,水化学类型以HCO3-Na、HCO3-Na·Ca型为主,随地下水埋深的增加,Cr(Ⅵ)浓度、γNa+/γCl-系数逐渐增大,γCa2+/γHCO-3系数逐渐减小;与正常水相比,Cr(Ⅵ)异常地下水的p H、溶解氧、离子强度的平均值分别由7.2、4.3 mg·L-1、0.011 mol·L-1变为7.6、5.5 mg·L-1、0.028 mol·L-1,溶解氧增加有利于Cr(Ⅲ)的氧化,p H升高、离子强度降低可以促进Cr(Ⅵ)的活化,这些是促使含水介质中Cr(Ⅵ)的解吸、迁移和富集的主要水化学因素.     

湘江(长沙段)沿岸土壤中铬的形态分布及其在水草中的积累

铬在土壤中主要以Cr(Ⅲ)和Cr(Ⅵ)两种形态存在,而Cr(Ⅵ)主要以CrO2-4,Cr2O2-7,Cr(Ⅲ)主要以Cr3 和CrO-2等形式存在.上述存在形式在土壤中的迁移转化主要受土壤pH值和氧化还原电位(Eh)的制约.另外,也受土壤有机质含量、无机胶体组成、土壤质地及其化合物种类的影响.不同形态的铬在一定条件下可以相互转化.但是单从价态来区分并不能完全反映土壤中铬的真实存在形态,当前较为公认的是Tesseler的形态划分法. 本文研究了湘江(长沙段)沿岸土壤中铬的形态分布、转化及其在水草中的吸收.     

Cr（Ⅵ）、Ni耐性植物筛选及其吸收富集特性研究

采用营养液培养法和二因素完全实验设计,在5 mg.L-1Cr（Ⅵ）、Ni复合污染条件下对22种植物进行筛选实验,选取富集量较高且生长较快的旱伞草Cyperus alternifolius,分析其对Cr（Ⅵ）、Ni的累积规律及生理生化效应。结果表明：（1）在Cr（Ⅵ）、Ni复合污染胁迫下,旱伞草生长状况良好,对铬、镍具有较高的富集能力;（2）在Cr（Ⅵ）、Ni复合污染下,Cr（Ⅵ）抑制旱伞草对Ni的吸收,Ni促进旱伞草对Cr的吸收;（3）分别在单因素Cr（Ⅵ）、Ni的胁迫下,SOD和CAT活性随着Cr（Ⅵ）、Ni质量浓度（0-50 mg.L-1）的增加都是先上升后下降,MDA总体都呈增加的趋势;（4）在Cr（Ⅵ）胁迫下,旱伞草地上部富集总铬的含量较高,但六价铬含量较低,对Cr（Ⅵ）的转化率最大可达到97.00%。研究表明,旱伞草是一种修复Cr（Ⅵ）、Ni污染很有潜力的物种。     

铁粉和煤灰去除地下水中的六价铬Cr(Ⅵ)的研究

通过静态实验和动态实验研究了铁粉、煤灰及其混合物对地下水中六价铬离子Cr(Ⅵ)的去除效果。在静态实验中,探讨了铁粉用量,煤灰用量,煤灰粒度,放置时间对地下水中Cr(Ⅵ)去除率的影响及两者混合后对地下水中Cr(Ⅵ)去除效果。实验结果表明,两者混合后,对水中Cr(Ⅵ)的去除效果较好,并可节省铁粉的用量,即0.5g铁粉和10.0g煤灰混合,处理50mLCr(Ⅵ)质量浓度为10mg·L-1的水样,与单独用0.7g铁粉处理的效果相同,水中Cr(Ⅵ)的去除率接近100%。在动态实验中,用与静态实验等量的铁粉和煤灰,可处理150MlCr(Ⅵ)质量浓度为10mg·L-1的水样,处理后水中的Cr(Ⅵ)可达到饮用水的水质标准。结果表明,铁粉和煤灰可作为原位处理地下水中Cr(Ⅵ)的反应材料,为地下水的原位处理技术奠定了实验基础。     

胡敏酸、富里酸对土壤-地下水系统中BDE-47迁移的影响

多溴联苯醚(polybrominated diphenyl ethers,PBDEs)是土壤-地下水系统中广泛存在的有机污染物,研究土壤组分对其迁移行为的影响是解决土壤-地下水系统中多溴联苯醚归趋问题的关键。以典型多溴联苯醚同系物2,2',4,4'-四溴联苯醚(2,2',4,4'-tetrabromodiphenyl ether,BDE-47)为研究对象,选取胡敏酸(humic acid,HA)、富里酸(fulvic acid,FA)2种代表性土壤有机组分,配制不同浓度的FA、HA溶液(150 mg·L~(-1)、50 mg·L~(-1)),分别对不同浓度的BDE-47(100μg·g~(-1)、10μg·g~(-1))污染土壤进行土柱淋滤实验,探讨FA、HA对土壤-地下水系统中BDE-47迁移的影响。结果表明,HA作用下,实验组下层土壤中BDE-47的残留比例分别为0.62%和0.40%,分别低于对照组的0.72%和3.36%;FA作用下,实验组下层土壤中BDE-47的残留比例分别为6.40%和6.71%,分别高于对照组的0.72%和3.36%。结合HA和FA的元素组成和结构特征分析可知,疏水性强的HA能够促进BDE-47随水流迁移进入地下水系统;亲水性强的FA促进BDE-47在土壤系统中的分布,阻滞了土壤系统中BDE-47进入地下水系统。本文为评估HA、FA对土壤-地下水系统中BDE-47迁移的影响提供依据。     

砖红壤对Cr(Ⅵ)吸附-解吸反应动力学研究

研究了表面覆盖度、H2PO-4等因素对砖红壤吸附Cr(Ⅵ)反应动力学的影响,以及土壤与Cr(Ⅵ)反应时间对表面吸附态C r(Ⅵ)解吸量的影响,还对土壤吸附Cr(Ⅵ)机理进行了初步探讨.在所研究的pH值范围内,砖红壤对Cr(Ⅵ)的吸附量随离子强度增加而减少,这表明砖红壤吸附Cr(Ⅵ)机理中存在静电吸附.动力学实验表明,当Cr(Ⅵ)初始浓度较高时(0.1 mmo.ll-1),吸附反应速率开始比较快,持续约5m in,随后逐渐减缓.而当Cr(Ⅵ)初始浓度较低时(0.05 mmo.ll-1),土壤对其吸附速率十分迅速,5m in内的吸附量占总吸附量的96%以上.该结果表明,表面覆盖度越低,吸附反应速率越快.H2PO-4的存在将降低吸附反应速率和吸附量.H2PO-4对土壤表面吸附态Cr(Ⅵ)的解吸反应动力学也表现出双速率特征,即开始比较迅速而随后逐渐变缓.当延长土壤对Cr(Ⅵ)的吸附时间后,Cr(Ⅵ)吸附量虽然没有增加,但其解吸量却减少,这说明吸附态Cr(Ⅵ)滞留在土壤表面期间,其结合形态向难解吸态方向发生了转变.     

改性稻草对Cr(Ⅵ)的吸附动力学

以氢氧化钠作为预处理剂,以环氧氯丙烷作为醚化交联剂,以三甲胺作为季铵化反应剂,对原稻草进行改性;比较改性前后稻草的吸附效果,探究pH对吸附效果的影响以及不同初始浓度、温度条件下改性稻草吸附Cr(Ⅵ)的动力学特性.结果表明,改性稻草对Cr(Ⅵ)的吸附量得到很大提高;pH值在2.0—6.4之间时,Cr(Ⅵ)的吸附量达到最大值,本实验选择pH=6.4;不同Cr(Ⅵ)初始浓度和不同温度下,准二级速率方程相关系数R2的范围为0.9562—0.9982,证明准二级速率方程能够很好地描述改性稻草对Cr(Ⅵ)的吸附过程,准二级速率方程的吸附速率常数k2随温度的升高而增大;准一级速率方程只适合描述Cr(Ⅵ)吸附过程的初始阶段,吸附过程受颗粒内扩散的控制;稻草秸秆通过化学改性制成表面有季铵基的氯型吸附剂,Cr(Ⅵ)的阴离子与改性稻草上的氯离子交换从而得以去除.     

木本泥炭对Cr(Ⅵ)的吸附性能

以木本泥炭为吸附材料,用于去除水中的Cr(Ⅵ).研究了溶液pH值、吸附时间、木本泥炭用量、缓冲液浓度和初始浓度对Cr(Ⅵ)吸附的影响,以及溶液pH值对Cr(Ⅵ)解吸附的影响.结果表明,木本泥炭对Cr(Ⅵ)的去除率随溶液pH值的增大而减小,当溶液pH值为4时,木本泥炭对Cr(Ⅵ)的吸附能力最强,3.33 g·L~(-1)木本泥炭对100 mg·L~(-1)Cr(Ⅵ)的吸附量为29. 98 mg·g~(-1);当磷酸盐缓冲液浓度在0. 10—0.20 mol·L~(-1)范围内时,随着缓冲液浓度的增大Cr(Ⅵ)的吸附量逐渐减小;木本泥炭对Cr(Ⅵ)的吸附符合准一级反应动力学,其吸附等温线符合Langmuir吸附模型;当溶液pH值小于6时,Cr(Ⅵ)的解吸率低于0.32%.     

含铬污液在土壤中迁移规律的研究

通过静态吸附和动态土柱淋溶实验,研究了含铬污液中Ｃｒ（Ⅲ）、Ｃｒ（Ⅵ）在土壤中的迁移规律。结果表明,土壤对Ｃｒ（Ⅲ）、Ｃｒ（Ⅵ）的等温吸附过程均符合Ｌａｎｇｍｕｉｒ方程,土壤对Ｃｒ（Ⅲ）、Ｃｒ（Ⅵ）的饱和吸附量分别为２．１７＊１０＾４ｍｇ／ｋｇ、１７５ｍｇ／ｋｇ;动态截留量分别为７．００＊１０＾３ｍｇ／ｋｇ、５６．７ｍｇ／ｋｇ。     

Phytoextraction of Cr(VI) from soil using Portulaca oleracea

Cr(VI) represents an environmental challenge in both soil and water as it is soluble and bioavailable over a wide range of pH. In previous investigations, Portulaca oleracea (a plant local to the United Arab Emirates (UAE)) demonstrated particular ability for the phytoextraction of Cr(VI) from calcareous soil of the UAE. In this publication, the results of the evaluation of P. oleracea phytoextraction of Cr(VI) from UAE soil at higher concentrations are reported. P. oleracea was exposed to nine different concentrations of Cr(VI) in soil from 0 to 400 mg kg^?1. The uptake of Cr(VI) increased as its concentration in soil increased between 50 and 400 mg kg^?1, with the most efficient removal in the range from 150 to 200 mg kg^?1. The total chromium concentrations exceeded 4600 mg kg^?1 in roots and 1400 mg kg^?1 in stems, confirming the role of P. oleracea as an effective Cr(VI) accumulator. More than 95% of the accumulated Cr(VI) was reduced to the less toxic Cr(III) within the plant.     

Mass-transfer processes of chromium(VI) adsorption onto guava seeds

The chromium(VI) biosorption onto guava seeds, as an alternative method for Cr⁶⁺ removal from aqueous solutions, was investigated. The parameters affecting kinetics and equilibrium of Cr⁶⁺ adsorption onto guava seeds were studied. An external mass-transfer diffusion coefficient k and intra-particle diffusion coefficient k_i were determined to measure the rate-limiting step of adsorption. A single external mass-transfer diffusion model and intra-particle diffusion models were used. The effects of initial pH, sorbent mass, and initial Cr⁶⁺ concentrations on mass-transfer coefficients were investigated. The external mass-transfer coefficient has an average value of 7.2×10^-3 cm s^-1, while the intra-particle mass-transfer diffusion coefficient was 0.34 mg g^-1 min^-0.5. This indicates that external diffusion to the guava seeds surface and intra-particle diffusion are both involved in the sorption process. The isotherm equilibrium data were well fitted by the Langmuir and Freundlich models with an average correlation coefficient R²=0.98. The maximum removal of Cr⁶⁺ was obtained at pH 1 (about 100% for adsorbent dose of 15 g l^-1 and 25 mg l^-1 initial concentration of Cr⁶⁺). The results indicated that the guava seeds exhibit acceptable sorption capacity.     

1,3,5-triazine-triethylenetetramine polymer: an efficient adsorbent for removal of Cr(VI) ions from aqueous solution

The synthesis of 1,3,5-triazine-triethylenetetramine (TATETA), its characterization by infrared spectroscopy and elemental analysis, and its application for removal of Cr(VI) ions from aqueous solution is reported. The effects of pH, contact time, initial concentration of Cr(VI), sorbent dose, and temperature on adsorption were investigated and optimized by batch adsorption experiments. Adsorption was highest at acidic conditions with an equilibration time of 25 min. The adsorption followed a Langmuir model, with an adsorption capacity of 303 mg g^?1, was second order in its kinetics, and exothermic and thus spontaneous.     

Enhancement of extracellular Cr(VI) reduction for anammox recovery using hydrazine: performance,pathways, and mechanism

● N₂H₄ addition enhanced and recovered anammox performance under Cr(VI) stress. ● N₂H₄ accelerated electron transfer of Cr(VI) reduction for detoxification. ● N₂H₄ enhanced anammox metabolism for activity recovery from Cr(VI) inhibition. ● Extracellular Cr(VI) reduction to less toxic Cr(III) was the dominant mechanism. The hexavalent chromium (Cr(VI)) would frequently impose inhibition to anaerobic ammonium oxidation (anammox) process, hindering the efficiency of nitrogen removal in wastewater treatment. Hydrazine (N₂H₄), which is an intermediate product of anammox, participates in intracellular metabolism and extracellular Cr(VI) reduction. However, the roles of N₂H₄-induced intracellular metabolism and extracellular reduction in nitrogen removal under Cr(VI) stress remain unclear. The addition of 3.67 mg/L of N₂H₄ increased the anammox activity by 17%. As an intermediate, N₂H₄ enhanced anammox metabolism by increasing the heme c content and electron transfer system activity. As a reductant, N₂H₄ accelerated the reduction of c-Cyts-mediated extracellular Cr(VI) to the less toxic Cr(III). Extracellular Cr(III) accounts for 74% of the total Cr in a Cr(VI)-stressed anammox consortia. These findings highlight that N₂H₄-induced extracellular Cr(VI) reduction is the dominant mechanism for the survival of anammox consortia. We also found that N₂H₄ increased the production of extracellular polymeric substances to sequester excessive Cr(VI) and produced Cr(III). Taken together, the study findings suggest a potential strategy for enhancing nitrogen removal from ammonium-rich wastewater contaminated with Cr(VI).     

Removal of cadmium(II), lead(II), and chromium(VI) ions from aqueous solution using clay

Removal of cadmium(II), lead(II), and chromium(VI) from aqueous solution using clay, a naturally occurring low-cost adsorbent, under various conditions, such as contact time, initial concentration, temperature, and pH has been investigated. The sorption of these metals follows both Langmuir and Freundlich adsorption isotherms. The magnitude of Langmuir and Freundlich constants at 30°C for cadmium, lead, and chromium indicate good adsorption capacity. The kinetic rate constants (K _ad) indicate that the adsorption follows first order. The thermodynamic parameters: free energy change (ΔG ^o), enthalpy change (ΔH ^o), and entropy change (ΔS ^o) show that adsorption is an endothermic process and that adsorption is favored at high temperature. The results reveal that clay is a good adsorbent for the removal of these metals from wastewater.