不同晶型纳米CdS的合成及其光催化活性

以醋酸镉为镉源,硫脲为硫源,采用配合物热分解法,通过改变硫脲/醋酸镉的摩尔配比,合成了具有不同晶型的纳米CdS．当n（S）／n（Cd）=0．5—3时,合成的CdS相分别为立方相（n（S）／n（Cd）=0．5）,立方相和六方相的混相（n（S）／n（Cd）=1．0～1．5）,六方相（n（S）／n（Cd）≥2）．通过XRD,TEM,UV—Vis光谱,IR光谱等对CdS的相组成,形貌,粒径,吸光性能,表面结构等进行了表征．光催化降解罗丹明B的活性结果表明,不同CdS相组成的活性顺序为立方相〉六方相〉混相（立方＋六方）,其中立方CdS相由于有较强的吸附作用、光吸收性能和较小的粒径（10～13nm）,对罗丹明B具有最好的光催化降解活性．     

铈添加对Ti26．5Cr20（V45Fe8．5）0．98Si2合金结构及储氢性能的影响

通过XRD,SEM,恒温等容储氢性能测试等方法,研究了Ce添加对Ti265Cr20（V45Fe8．5）098Si2Cex（x=0～2．0％（原子分数））合金结构及储氢性能的影响。结果表明,Ti26．5Cr20（V45Fe85）0.98Si2Cex（x=0～2．0％）合金为BCC和C14 Laves相双相合金,随合金中Ce添加量的增加,合金的晶格常数增大,而合金中C14 Laves相的含量减少,平衡压从0．233MPa降低到0．167MPa,合金的吸氢动力学性能得到改善,最大吸氢量也由3．08％增加至3．19％（质量分数）,PCT曲线的平台斜率减小。合金的储氢性能的改善与Ce的加入抑制了部分C14Laves相的析出,减少了合金中C14Laves相的含量密切相关。     

高硅分子筛ZSM-22的动态合成及表征

 以1，6－己二胺（DAH）为模板剂，采用水热条件下的动态合成方法，合成出结晶度良好的ZSM－22晶体．研究表明，合成的关键是避免ZSM－5分子筛的生长，当n（Si）／n（Al）＝25～65，n（H2O）／n（SiO2）＝16．3～40．3，n（DAH）／n（Si）＝0．1～0．6和T＝428～448K时，都能稳定合成出ZSM－22分子筛．采用TEM，XRD，TG－DTA和NH3－TPD等方法，对ZSM－22晶体的形貌，生长动力学，模板剂的作用以及硅铝比对分子筛酸性的影响等进行了较详细的研究．实验结果和理论计算证实，1，6－己二胺分子以首尾相连的方式，线性排列并完全充满ZSM－22的十元环孔道，同时起到结构导向和骨架电荷平衡的作用．     

Ce0.67Zr0.33O2对CH4燃烧催化剂Fe2O3/Al2O3的改性作用

固定n（Ce）／n（Zr）比为0．67／0．33,用共沉淀法制得一系列CeO2-ZrO2-Al2O3固溶体,采用这些固溶体作载体,以Fe2O3为活性组分,用浸渍法制备了一系列催化剂,BET结果显示,将适量Ce0.67Zr0．33O2引入到Al2O3载体中有助于催化剂保持较高的比表面积,TPR结果显示,载体中引入适量的Ce0．67Zr0.33O2可以改善催化剂的氧化还原性能,XRD结果表明,Fe2O3在CeO2-ZrO2-Al2O3载体上呈现出良好的分散状况,老化前后催化剂的晶相结构基本无明显变化,特别是当载体中m（Ce0.67Zr0.33O2）：m（Al2O3）的值为1：2时,Fe2O3／CeO2-ZrO2-Al2O3催化剂在甲烷催化燃烧中显示出最佳的催化性能和抗高温老化性能。     

La0.6Sr0.4Co1-yFeyO3(y=0.2,0.8)复合氧化物混合导电性能研究

采用甘氨酸-硝酸盐（GNP）法制备了La0．6Sr0．4Co1-yFeyO3（y=0．2，0．8）g合氧化物，研究了材料的结构、电子-离子混合导电性能及其相关性。结果表明，La0.6Sr0.4Co1-yFeyO3（y=0．2，0．8）合成粉料的颗粒细小均匀（～100nm），陶瓷形成菱形六面体钙钛矿结构。与La0．6Sr0．4Co0．2Fe0．8O3（y=0．8）陶瓷相比，La0.6Sr0.4Co0．8Fe0．2O3（y=0．2）陶瓷的晶粒尺寸大、致密度较高。在La0.6Sr0.4Co0．8Fe0．2O3（y=0．2）陶瓷中观察到Co^3＋离子歧化对电子导电性能的影响。与La0.6Sr0.4Co0.2Fe0.8O3（y=0．8）陶瓷相比，La0.6Sr0.4Co0.8Fe0．2O3（y=0．2）陶瓷具有更优异的电子-离子混合导电性能，材料在混合导电性能上的差异与其电子结构和显微结构紧密相关。     

磁载WO3－TiO2／SiO2／Fe3O4复合光催化剂的制备及其光催化活性

 用溶胶－凝胶法在表面包覆了SiO2的磁基体Fe3O4上负载TiO2,从而得到了易于磁性固液分离的磁载WO3－TiO2／SiO2／Fe3O4复合光催化剂,并通过IR,XRD,SEM和XPS等测试手段对催化剂进行了表征．研究了磁载WO3－TiO2／SiO2／Fe3O4复合光催化剂对亚甲基蓝溶液脱色的性能,并考察了WO3掺杂量对样品催化活性的影响．结果表明,n（WO3）／n（TiO2）＝0．001时,磁载WO3－TiO2／SiO2／Fe3O4复合光催化剂的催化活性最高,循环使用3次时脱色率仍保持在98％．     

酶催化-荧光猝灭法测定药物中的姜黄素

酪氨酸在辣根过氧化物酶催化下被H2O2氧化为强荧光物质S,姜黄素对其荧光产生猝灭作用,据此建立了测定姜黄素的新方法。姜黄素浓度c在0．10～16．0μg/mL范围内与F0／F（F和F0分别为姜黄素存在和不存在时产物S的荧光强度）呈线性关系,线性回归方程c=5．4552F0／F-5．4860,线性相关系数r=0．9996,检出限为0．02μg/mL,测定结果的相对标准偏差为0．79％（n=10）,加标回收率为94．7％～102％。研究了pH值、各物质的量、反应时间、干扰离子等对测定的影响。该法可用于药物中姜黄素含量的测定。     

Nd1-yDyyFe11-xTiMx（M=Mo，Si）系列化合物中Mo，Si元素的掺杂对其结构及磁性能的影响

通过电弧方法制备了一系列的Nd1-yDyyFe11-xTiMx（M=Mo,Si）型稀土过渡金属化合物,并且通过X射线衍射和中子衍射对其晶体结构进行了研究．实验发现,Nd1-yDyyFe11-xTiMx（M=Mo,Si）系列中化合物主要结构为ThMn12-type（1：12相）．Dy取代Nd没有明显影响1：12相形成的含量．在Nd0．5Dy0.5Fe11-xTiMx（M=Mo,Si）系列中,当x≤0．8时Nd0．5Dy0．5Fe11-xTiMox化合物主要呈ThMn12-type晶形,当x〉0．8时,化合物中1：12相的含量降至80％以下;对于Nd0.5Dy0.5Fe11-xTiSix,当X≤0．6时,Nd0.5Dy.5Fe11-xTiSix化合物主要呈ThMn12-type晶形,当X〉0．6时,化合物中1：12相的含量降至90％以下但保持在80％以上．     

La0．6Sr0．4Col—yFeyO3钙钛矿复合氧化物的GNP法合成与导电性能

采用甘氨酸-硝酸盐(GNP)法合成出La0．6Sr0．4Col-yFeyO3(y=0-1.0)体系复合氧化物，对合成产物的结构、烧结性能和导电性进行了表征．研究结果表明．不同n(Co)／n(Fe)比的合成粉料中形成菱形六面体钙钛矿结构，合成粉料的颗粒细小均匀．在室温～900℃范围内，La0．6Sr0．4Col-yFeyO3(y=0)的电导率随温度的升高而单调降低，其它n(Co)／n(Fe)比的样品电导率随着温度升高到600℃附近时达到最大值．在低温段．La0．6Sr0．4Col-yFeyO3体系的导电行为符合小极化子导电机制，导电活化能随n(Co)／n(Fe)比的降低而增大．与常规固相合成法相比，甘氨酸-硝酸盐法制备的La0．6Sr0．4Col-yFeyO3具有更高的烧结活性和电导率．     

顶空衍生固相微萃取-气相色谱质谱法测定聚碳酸酯树脂中的环境雌激素

建立了固相微萃取-气相色谱质谱联用测定聚碳酸酯树脂中环境雌激素4-枯基苯酚和双酚A的分析方法。优化了固相微萃取纤维、萃取温度和时间、解吸时间、搅拌速度、pH等萃取条件及衍生化温度和时间、衍生化方式等衍生化条件，并对样品浸泡时间、浸泡温度等进行了研究。方法的线性范围为0．05μg/L～1mg／L，4-枯基苯酚和双酚A的检出限分别为50ng／L和0．5ng／L，相对标准偏差（RSD，n=5）分别为5．2％和1．6％，平均回收率（n=3）在90．50％～107．3％之间，该方法简单、快速、灵敏。     

聚合氯化铁的制备及其絮凝效果

以赤铁矿和工业盐酸为原料,采用盐酸酸浸和加碱聚合等方法制取聚合氯化铁絮凝剂(PFC),将其用来处理造纸废水,并与市售聚合氯化铁和碱式氯化铝絮凝剂进行比较.结果表明,在碱化度为2∶1、聚合温度为40℃、陈化时间为24h时,自制聚合氯化铁絮凝剂对造纸废水具有较好的处理效果;投加量为1.4mL/L时,造纸废水的浊度降低了99%,化学需氧量(COD)降低了69.55%,优于市售絮凝剂对造纸废水的处理效果;且三种絮凝剂用量相同时,自制的聚合氯化铁絮凝剂形成絮体的速率和沉降速率都较快.     

Increasing the arsenate adsorption capacity of neutralized red mud (Bauxsol)

The possibility of increasing the arsenate adsorption capacity of seawater-neutralized red mud (Bauxsol) through acid treatment, combined acid and heat treatment, and the addition of ferric sulfate (Fe(2)(SO(4))(3).7H(2)O) or aluminum sulfate (Al(2)(SO(4))(3). 18H(2)O) is investigated. The results show that acid treatment alone, as well as in combination with heat treatment increases the removal efficiency, with the combination providing the best removal. Adding ferric sulfate or aluminum sulfate, however, suppress the removal. The results also show that activated Bauxsol (AB) produced using combined acid and heat treatment can remove roughly 100% arsenate (at pH 4.5) with or without competing anions (i.e., phosphate, bicarbonate, and sulfate) when the initial arsenate concentration is < or = 2 mgl(-1). Furthermore, it is found that the adsorption process using AB is not accompanied by the release of unwanted contaminants, and TCLP results indicate that the spent AB is not hazardous. It is believed that the AB produced here has good potential as an alternative adsorbent to conventional methods for removing arsenate from water.     

Study on Properties and Synthesize of a new Polymeric Aluminum Sulfate-silicate

The polymeric basic aluminum silicate-sulfate can be made from three substances, such as aluminum sulfate, sodium silicate and sodium aluminates. Adoption sort neote ric one synthesis,under high shear mixing condition to produce polymeric Aluminum Sulfate-silicate--inorganic macromolecule flocculants, that is liquid, PH is 3.0, molecular formula: AlA (OH) B (SO4) C (SiOx)Because inorganic macromolecule have capability of electricity neutralized, bigger molecular mass,strong capability of adsorption, and products are relative stabilize, more economical than organic macromolecule flocculants, innocuity and high effect compared with tradition flocculants.We can use the flocculants to make sewages purified .The sewages contain sulfur, oiliness, which are treated sewages of oil refining to organism treatment sump in parturition course of oil refining,and the sewages of dark and white in parturition course of paper mill. We study the properties of the flocculants, change of CODCr and effect of sewerage decolouring and so on.Thus fig. Can be seen to add the flocculants(0.1ml) to the sewages of the oil refining and the paper mill that effect is not distinctly. Yet increase of quantity to remove turbidity and floccules effect is distinctness. When the flocculants (0.5mi) be added to the dark sewage of, the penetrate light rate attain 90～98%, the sewage of the oil refining is about 90%, but when we make floccules experiment, the color of dark green and auras of the sewages of oil refining and the paper mill are all disappear, the PASS that add to the sewage will have certainly time to flocculate. When use pay attention to quantity and horary the connection.As a result in the sewages purified, those products form quickly, granule density is big, and subsided velocity is quickly, Floccules effect and capability of removing turbidity, removing CODCr are ascendancy than tradition flocculants - aluminates, and the remained aluminum of water treatment is little. It has preponderance property of sedimentation rapidity and purifying rate, and the capability be purified of flocculants is increase 50% than the AS. The flocculants uses little dosage in sewerage treatment. That has wide foreground of application, salience economy and society benefit, congruency extend and applied in sewerage Treatment field. The flocculants has predominant use property than the aluminum sulfate.     

Activation of sulfite by ferric ion for the degradation of 2,4,6-tribromophenol with the addition of sulfite in batches

In this work, the removal of 2,4,6-tribromophenol (TBP) by ferric ion-activated sulfite [Fe(III)/S(IV)] process was systematically investigated with determining the intermediate products and evaluating the influences of some operational conditions and water matrices. Our results show that batching addition of S(IV) benefits the S(IV) utilization efficiency and TBP removal, with SO₄^?? being the primary reactive radical accounting for TBA degradation. The maximum TBP removal in the Fe(III)/S(IV) process was observed at pH 4.0 and oxygen is essential in this process. With increasing Fe(III) and S(IV) dosages from 0.05 and 0.1 mmol/L to 0.2 and 2.0 mmol/L, respectively, TBP removal followed trends of first increase then decrease. As the acute toxicity of the TBP solution was significantly reduced, the Fe(III)/S(IV) process was believed to be a good choice in the treatment of TBP.     

Study of flocculation with PONILIT GT-2 anionic polyelectrolyte applied into a chemical wastewater treatment

This paper discusses the applications of synthetic PONILIT GT-2 anionic polyelectrolyte in conjuction with ferric sulfate in a chemical wastewater treatment viz. wastewater from ceramics manufacturing. Synthetic wastewaters with different colloid concentrations were prepared and the coagulation-flocculation process followed by sedimentation and/or filtration was studied. Variables associated with the chemical wastewater composition, mixing time, and the coagulant and flocculant dose are considered in order to appreciate the process efficiency in terms of turbidity, chemical oxygen demand (COD), and color removal. The degrees are higher for turbidity and color (> 80 %) removal respectively, and, satisfactory for COD (< 50 %). An empirical model was elaborated by a third order rotatable design 2³ type, considering ferric sulfate dose, polyelectrolyte dose, and mixing time as independent variables, while the turbidity and color removal efficiencies were chosen as optimization criteria. The empirical model was found adequate for the chemical wastewater treatment. Also, an analysis of the model was performed to find the optimal operating conditions, in order to apply this process for an efficient chemical wastewater treatment using ferric sulfate as coagulation agent and PONILIT GT-2 anionic polyelectrolyte as flocculation agent. The optimal values correspond to a ferric ions concentration of 6.093 mg/L, a polyelectrolyte dose of 0.651 mg/L, and a mixing time of 24.024 minutes for turbidity removal (95.869 %), respectively, and, to a ferric ions concentration of 6.01 mg/L, a polyelectrolyte dose of 0.69 mg/L, and a mixing time of 26 minutes for color removal (98.741 %).      

In situ and ex situ study of the enhanced modification with iron of clinoptilolite-rich zeolitic tuff for arsenic sorption from aqueous solutions

Adsorption methods have been developed for the removal of arsenic from solution motivated by the adverse health effects of this naturally occurring element. Iron exchanged natural zeolites are promising materials for this application. In this study we introduced iron species into a clinoptilolite-rich zeolitic tuff by the liquid exchange method using different organic and inorganic iron salts after pretreatment with NaCl and quantified the iron content in all trials by XRF spectroscopy. The materials were characterized by XRD, FTIR, FTIR-DR, UV-vis, cyclic voltammetry, ESR and M?ssbauer spectroscopies before and after adsorption of arsenite and arsenate. The reached iron load in the sample T+Fe was %Fe(2)O(3)-2.462, n(Fe)/n(Al)=0.19, n(Si)/n(Fe)=30.9 using FeCl(3), whereby the iron leachability was 0.1-0.2%. The introduced iron corresponded to four coordinated species with tetrahedral geometry, primarily low spin ferric iron adsorbing almost 12 mug g(-1) arsenite (99% removal) from a 360 mug(As(III)) L(-1) and 6 mug g(-1) arsenate from a 230 mug(As(V)) L(-1). Adsorption of arsenite and arsenate reached practically a plateau at n(Fe)/n(Si)=0.1 in the series of exchanged tuffs. The oxidation of arsenite to arsenate in the solution in contact with iron modified tuff during adsorption was observed by speciation. The reduction of ferric iron to ferrous iron could be detected in the electrochemical system comprising an iron-clinoptilolite impregnated electrode and was not observed in the dried tuff after adsorption.     

以赤泥为原料合成聚合氯化铝铁复合絮凝剂及其应用

介绍了用炼铝废弃物赤泥制备聚合氯化铝铁絮凝剂（PAFC）的基本工艺.研究了液固比、反应温度、反应时间对赤泥溶出率的影响,确定了最佳溶出条件为反应液固比3.5∶1、温度85℃、时间1.5 h;制备聚合氯化铝铁絮凝剂的最佳工艺条件为铝铁摩尔比1∶1,温度60℃,反应时间1.0 h.通过对该产品进行混凝试验,得出当PAFC投加量为0.80 mL.L-1,沉降时间为30 min,pH在6～7之间时,浊度、色度、COD的最大去除率分别达到69%、85%、70%.     

混凝沉淀法处理工业含氟废水的工艺研究

以半导体工业中的含氟废水为研究对象,采用混凝沉淀法对去除废水中氟离子进行了系统的工艺研究.以Ca(OH)2为沉淀剂,分别用聚合氯化铁(PFC)和聚合氯化铝(PAC)为混凝剂,并加入聚丙烯酰胺(PAM)助凝剂的方法,对药剂投加量、混凝剂种类、体系pH值、沉降时间等因素进行了实验探索.结果显示,PFC比PAC混凝效果好.当Ca(OH)2添加量为理论值的2.5倍,PFC用量为15mg/L,助凝剂PAM用量为4mg/L,体系的pH值在6～7时,其除氟效果最佳,此时废水中残留氟离子浓度可降低至5.5mg/L,远远低于国家规定的排放标准(10mg/L).     

浮动液滴固化分散液相微萃取-火焰原子吸收光谱法测定环境样品中的镉

建立了以十一醇为萃取剂,吡咯烷二硫代甲酸铵(APDC)为螯合剂的浮动液滴固化分散液相微萃取-火焰原子吸收光谱法(DLLME-SFO-FAAS)测定环境样品中痕量镉的分析方法;优化了分散剂、萃取剂的类型和体积,考察了溶液pH值、APDC浓度以及萃取温度和时间对萃取效率的影响.结果表明,该法检出限(3σ)为0.14μg/L...     

Decolorization of Naphthol Blue Black using the Horseradish Peroxidase

This study evaluates the potential of the enzyme horseradish peroxidase in the decolorization of one common industrial azo dye, naphthol blue black. Studies are carried out to understand the process parameters such as pH, temperature and reaction time. The enzymatic decolorization of the dye was examined by UV-Vis spectrophotometer and LC-MS measurements. Temperature and pH conditions were optimized for obtaining high azo-dye decolorization. Azo-dye removal at a pH range 4-6 was found to be the highest for all temperatures. After 5 minutes of treatment, the color removal of dye was ca. 80-90%. The LC-MS and spectrophotometric analyses indicated that the decolorization of the azo dye with enzyme was due to the reduction of the azo bonds. This study verifies the viability of the use of the horseradish peroxidase in the decolorization of naphthol blue black.