Ti/Sb-SnO2功能电极的制备及电化学处理废水的性能

采用热分解法制备了Ti/Sb-SnO2电极,并用XRD、SEM对电极涂层进行表征.研究了涂层次数对于析氧过电位的影响,应用阳极快速寿命测试法测试了Ti/Sb-SnO2电极的使用寿命,通过极化曲线考察了电极的析氧过电位.采用该电极对甲基橙模拟废水进行了电化学降解实验,并考察此电极处理实际废水的效果.研究表明,随着涂层次数的增加,其析氧过电位增加,当涂层次数达到15次时,析氧过电位高达1.8 V(vs SCE),有效抑制了阳极析氧副反应的发生.以Ti/Sb-SnO2电极作为阳极,对甲基橙模拟废水电解10 min后,脱色率接近100%,甲基橙模拟废水降解60 min后,TOC去除率才能达到86.2%,TOC去除率明显滞后于脱色率.     

阿特拉津降解菌的生长规律及降解特征的实验

应用了从农药厂阿特拉津生产车间污泥中分离出的菌种AT菌,进行了菌种生长曲线的测定,求得AT菌的对数期代时为3．87d,生长速率为0．258d^-1;不同基质浓度的降解实验表明,在农药污染质阿特拉津的低浓度体系中,AT菌降解阿特拉津的反应符合一级动力学模式,属于米氏方程曲线的第一阶段的情形,并拟合出关系式V＝0．064S。     

On the random placement hypothesis

A traditional method of summarizing spatial distribution of species is the observed species-area curve. Often the observed species-area curve is surprisingly close to the expected species-area curve under the hypothesis of random placement of individuals. This has been used as evidence supporting the hypothesis. In this paper, we argue that using the observed species-area curve to test the general random placement hypothesis is highly inefficient. We present a testing method based on the classical ² test for over-dispersion which is not only more efficient but also applicable to situations where complete abundance information are unavailable. We also discuss three alternatives of the hypothesis. The focus of this paper is on these and other general issues relevant to communities of different types. No applications are included in this paper.     

GDX-502对一元酚动态吸附曲线和吸附容量的研究

测定了GDX-502树脂对水中9种一元酚的动态吸附曲线和吸附容量,讨论了可能的吸附机理?实验结果表明,水中各种酚对GDX-502存在着竞争吸附,若水样体积足够大,则水也参与竞争吸附?浓度高的酚,竞争能力强,被吸附容量大?相同浓度的酚,溶解度越小,偶极矩适当大,并能做为电子受体与树脂形成较强的π-键合作用力,则竞争占优势,被吸附容量大?动态吸附曲线上负吸附现象的存在是竞争吸附,特别是水处于优势吸附时的结果      

废弃绿茶对水溶液中Co2+的吸附研究

利用废弃绿茶叶粉末(简称茶叶末)作为吸附剂,考察了pH、温度、时间等对水溶液中Co2+的影响。结果表明:(1)茶叶末对Co2+的吸附量随着pH的上升而上升,其中pH=5.50为最佳。茶叶末对Co2+的吸附量均随时间延长呈现上升趋势,吸附速度先快后慢,吸附最佳时间为90min。(2)不同温度下,茶叶末对Co2+的吸附较好地符合Langmuir模型。该吸附过程是化学离子交换过程,主要发生在重金属离子与羟基、氨基的氢原子之间。(3)茶叶末对Co2+的吸附是自发、放热过程,降温有利于吸附,反应时吸附界面上的混乱度增加。(4)盐酸是很好的解吸介质,解吸率为92.65%。通过灼烧(或燃烧)可以回收水溶液中绝大部分的Co2+,不仅减小了对环境的污染,而且节约了资源。     

Characterization of primary precipitate composition formed during co-removal of Cr(VI) with Cu(II) in synthetic wastewater

BACKGROUND, AIMS AND SCOPE: Hexavalent chromium [Cr(VI)] cannot react with either carbonate or hydroxide to form chromium precipitates. However, by using a precipitation technology to treat plating wastewater containing Cr(VI), Cu(II), Ni(II) and Zn(II), approximately 78% of Cr(VI) (initial 60 mg/L) was co-removed with the precipitation of Cu(II), Ni(II) and Zn(II) (each 150 mg/L) by dosing with Na2CO3 (Sun 2003). Direct precipitation by forming Cu(II)-Cr(VI) precipitates followed by adsorption of Cr(VI) onto freshly formed Cu-precipitates was subsequently found to be the main mechanism(s) involved in Cr(VI) co-removal with Cu(II) precipitation by dosing Na2CO3 stepwise to various pH values (Sun et al. 2003). This study was. carried out to further characterize the formation of primary precipitates during the early stages of copper precipitation and simultaneous removal of Cr(VI) with Cu(II). METHODS: Test metal-solutions were prepared with industrial grade chemicals: CuCl2 x 2H2O, Na2SO4 and K2Cr2207. NaCO3 was added drop-wise to synthetic metal-solution to progressively increase pH. For each pH increment, removal of soluble metals was detected by atomic absorption spectrophotometer (AAS) and surface morphology of precipitates was analyzed by scanning electron microscope (SEM). To further characterize the formation of primary precipitates, a series of MINEQL+ thermodynamic calculations/analyses and equilibrium calculations/ analyses were conducted. RESULTS AND DISCUSSION: MINEQL+ thermodynamic calculation indicated that, for a system containing 150 mg/L Cu(II) and 60 mg/L Cr(VI) with gradual Na2CO3 dosing, if any precipitates can be formed at pH 5.0 or lower, it should be in the form of CuCrO4. Comparison tests using systems containing the same equivalent of Cu(II) plus Cr(VI) and Cu(II) plus SO4(2-) showed that the precipitation occurred at a pH of around 5.0 in the Cu(II)-Cr(VI) system and around 6.0 in the Cu(II)-SO4(2-) system. The discrepancy of the precipitation was indeed caused by the formation of Cu-Cr precipitates. The initiation of copper removal at pH around 5.0 for the Cu-Cr co-removal test was not attributable to the formation of Cu-CO3 precipitates, instead, it was most likely through the formation of insoluble Cu-Cr precipitates, such as CuCrO4 and CuCrO4 x 2Cu(OH)2. Experimental tests, equilibrium calculations, MINEQL+ thermodynamic calculations and surface morphologies for systems using higher concentrations of Cu(II) and Cr(VI) further verified the most probable composition of primary precipitates is copper-chromate. CONCLUSION: In the Cu-Cr co-removal test with Na2O3 dosing to increase pH and induce metal precipitation, copper-chromate precipitates are the primary precipitates produced and contribute to the initial simultaneous removal of copper and chromium.     

Colloid‐facilitated transport of metolachlor through intact soil columns

Abstract

This study evaluated the role of water dispersible colloids with diverse physicochemical and mineralogical characteristics in facilitating the transport of metolachlor through macropores of intact soil columns. The soil columns represented upper solum horizons of an Alfisol in the Bluegrass region of Kentucky. Three different colloid suspensions tagged with metolachlor [2‐chloro‐N‐(2‐ethyl‐6‐methylphenyl)‐N‐(2‐methoxy‐l‐methylethyl)acetamide] were introduced at a constant flux into undisturbed soil columns. The eluents were collected and analyzed periodically for colloid and metolachlor concentrations. Colloid recovery in the eluents ranged from 54 to 90 %. The presence of colloids enhanced the transport of metolachlor by 22 to 70 % depending on the colloid type and mobility. Colloids with higher pH, organic carbon, cation exchange capacity (CEC), total exchangeable bases (TEB), surface area (SA), and electrophoretic mobility (EM), showed better mobility, greater affinity for interaction with the herbicide and, thus, greater potential to co‐transport metolachlor. In contrast, increased level of kaolinite, Fe, and Al inhibited metolachlor adsorption and transport. In spite of the increased transportability of metolachlor by the presence of soil colloids, the colloid bound herbicide portion accounted for a very small part of the observed increase. This suggests that surface site exclusion mechanisms and preferential sorption induced by the presence of colloids are more important than ion exchange phenomena in promoting herbicide mobility in subsurface environments.     

分子筛负载型吸附剂对典型VOCs的吸附行为特性

以浸渍法制备的分子筛负载铜锰铈(Cu-Mn-Ce/ZSM)为吸附剂,以甲苯、乙酸乙酯和丙酮作为挥发性有机物(VOCs)的典型代表,考察了单组分和混合组分VOCs在吸附剂固定床上的吸附行为。研究表明,Cu-Mn-Ce/ZSM吸附单组分VOCs时,甲苯的吸附穿透时间与饱和吸附量分别为110 min和32.47 mg/g,乙酸乙酯为150 min和52.29 mg/g,丙酮为210 min和86.40 mg/g,可见Cu-Mn-Ce/ZSM对单组分VOCs的吸附能力大小为:丙酮 > 乙酸乙酯 > 甲苯。Cu-Mn-Ce/ZSM吸附混合组分VOCs时,在甲苯与乙酸乙酯的穿透曲线上出现了明显的\"驼峰\",吸附穿透过程中存在共吸附和竞争吸附行为,甲苯的吸附穿透时间与饱和吸附量降至50 min、10.42 mg/g,乙酸乙酯为95 min、15.12 mg/g,丙酮为105 min、44.37 mg/g。通过Yoon-Nelson模型对单组分VOCs吸附穿透曲线的拟合,表明吸附模型参数可以准确地预测吸附质在固定床上的穿透行为。速率参数k'值计算表明,不同VOCs在固定床上的吸附速率大小为丙酮 < 乙酸乙酯 < 甲苯。     

电渗透脱水污泥干燥特性曲线及干燥模型简

通过电渗透脱水技术及自然风干技术两种预处理方式降低污泥含水率,当污泥初始含水率相近时,研究经两种方式处理后污泥的干燥特性曲线,并对电渗透脱水污泥干燥特性曲线的优势情况进行探讨。在40~120℃的低温条件下,研究电渗透脱水污泥（泥饼厚度为3.5 mm）的干燥特性曲线并分析其干燥特性。通过所得电渗透脱水污泥的干燥特性曲线,引入薄层污泥干燥模型进行数值分析。结果表明,在实验条件下,电渗透脱水污泥的干燥速率要优于自然风干污泥的干燥速率。随着温度的升高,电渗透脱水污泥的干燥速率随之升高,干燥到所需含水率的时间则随之减少。Logarithmic模型比其他模型更适合描述薄层电渗透脱水污泥在低温条件下的干燥特性。