铝氧化物-水界面化学及其在水处理中的应用

天然水体中,铝氧化物矿物表面上的吸附等各种反应在很大程度上影响着金属阳离子、无机阴离子和一些天然有机物的迁移转化和归趋.在水处理等工业领域中,铝氧化物由于其水合表面的吸附能力而被用做离子交换剂和催化剂载体.因此,对铝氧化物表面化学过程的研究具有重要意义.铝氧化物-水界面上的反应十分复杂,对各种无机、有机污染物的吸附结合能力取决于氧化物固相表面性质、溶液条件和吸附质的性质.从对铝氧化物表面荷电特性和吸附活性的认识出发,就各种铝氧化物的结构特征和表面反应活性及其在水处理技术中的应用进行了简要综述.     

北京地区土壤对柴油的吸附及影响因素研究

通过静态吸附实验,研究了北京地区土壤对柴油的吸附行为,考察了溶液pH和添加乙醇对柴油吸附的影响. 结果表明,6种不同土样对柴油的吸附等温线均较好地符合Langmuir吸附方程,其吸附系数(K)分别为0.193, 0.218, 0.203, 0.199, 0.211和0.182 L/mg,6种土样吸附能力依次为轻壤土>轻粘土>中壤土>砂壤土>重壤土>紧砂土,这主要是由于6种土样的pH,有机质含量和机械组成不同所致;溶液pH的升高,不利于柴油在土壤中的吸附,pH从4升高到10,柴油在1～6号土样中的吸附量分别从1　012, 1　800, 1　377, 1　272, 1　601和862 μg/g降低到114, 236, 163, 150, 201和85 μg/g;向柴油中添加乙醇会减小柴油的吸附量,并且吸附量随添加乙醇量的增大而降低,这有利于柴油的向下运移.      

生物膜MBR反应器和MBR反应器处理洗涤废水比较

比较生物膜MBR反应器和MBR反应器处理洗涤废水的效果。结果表明,两个系统对COD、LAS及氨氮的去除均具有良好的处理效果。和MBR反应器相比,生物膜MBR反应器的运行条件要好。生物膜MBR反应器的运行条件:水力停留时间(HRT)4～4.5h,气水比351∶,而MBR反应器的运行条件:水力停留时间(HRT)9～10h,气水比451∶。通过两个反应器抗冲击负荷实验的研究,结果表明,在进水水质相同的条件下,就膜生物反应器的上清液而言,生物膜MBR反应器具有更好的抗冲击负荷能力。     

Ti/Cu交联累托石光催化氧化处理硝基苯废水研究

以钛酸丁酯为钛源,掺杂铜(CuCl2)制备交联剂.制得柱状Ti/Cu交联累托石,结合其吸附特性并通过其在光催化氧化条件下处理含硝基苯有机废水.在pH=9,交联累托石用量为30 g/L,一根20 W紫外灯光辐照2 h的处理条件下,硝基苯由73.81 mg/L降至3.17 mg/L,去除率达到95.71%,优于GB-8978-1996三级标准,用其处理含硝基苯工业废水,COD去除率为83.73%,由4800 mg/L降至530.4 mg/L,硝基苯去除率达92.3l%,由10.32 mg/L降至0.79 mg/L,小于GB-8978-1996-级标准.     

活性炭纤维对氯仿气体动态吸附的研究

为了探讨活性炭纤维(ACF)对氯仿有机废气的动态吸附,考察氯仿气体流速、浓度、温度、ACF再生次数对吸附效率的影响以及滤速和压降的关系。结果表明:低浓度、低流速、低温度均有利于吸附。ACF对氯仿的吸附以物理吸附为主。提高氯仿气体滤速,气体压降增大。     

玻璃弹簧负载镶嵌纳米粒子TiO2膜光催化降解活性深蓝K-R

以玻璃弹簧负载镶嵌纳米粒子的TiO2膜降解活性深蓝K-R模拟废水,考察了pH值和温度对脱色率的影响以及CODCr去除率与脱色率之间的关系,并用XRD和SEM对催化剂进行了表征.结果表明,pH值和温度对脱色率均有显著影响,CODCr去除率与脱色率的比值约为70%左右;XRD表明,TiO2矿相主要为锐钛型,SEM表明,镶嵌TiO2粒子均匀,粒径约50nm.     

我国典型土壤对病毒等温静态吸附的数值模拟

通过室内等温静态批量平衡吸附实验,采用3种常见的等温线（Freundlich方程、Langmuir方程和Temkin方程）对2种病毒（MS2和X174）在2种处理（非灭菌和灭菌）条件下的6种土壤（红壤土、红粘土、乌栅土、黄泥土、沙质潮土和壤质潮土）中的吸附行为进行了回归拟合.实验结果和模拟结果均表明,土壤性质、病毒性质、土壤中的土著微生物对病毒在土壤中吸附行为均具有重要的影响.红粘土对MS2和X174的平均吸附比例几乎能达到100％,而2种潮土（沙质潮土和壤质潮土）相对较弱;总体来看土壤对X174的吸附能力高于MS2,但灭菌后的土壤对MS2的吸附能力却高于X174.在数值模拟中,Freundlich方程和Langmuir方程均具有理想的相关性.Freundlich方程能够表现出病毒浓度对其在土壤中吸附行为的影响;尽管Langmuir方程能够应用于土壤对病毒吸附能力的比较,但本研究中不能应用Langmuir方程来计算土壤对病毒的最大吸附量.     

钢渣吸附-微波降解法处理碱性品红废水

研究了钢渣对碱性品红染料的吸附性能、影响因素以及微波对吸附在钢渣-焦炭上的染料的降解作用。实验表明,在中性条件下,钢渣对碱性品红具有优良的吸附性能,饱和吸附量可达到42．4mg／g。以钢渣处理质量浓度为100mg/L的碱性品红溶液,当固液质量比为1：50、振荡吸附1h后,染料溶液脱色率达97％。实验还表明,焦炭可吸收微波产生高温,用钢渣-焦炭混合物（质量比1：1）吸附染料后,以微波辐照可使物料达到665℃的高温,吸附的染料降解。吸附剂再生后重复使用4次,脱色率都达到95％以上。     

吸附模式对有机物光催化降解的影响2.H-酸在TiO2表面的光催化降解途径

水溶液中H-酸通过磺酸基团吸附在TiO2表面,UV照射TiO2所产生的自由基首先进攻吸附在TiO2表面的磺酸基团,从而进一步导致萘环开环.pH 2.5条件下,虽然饱和吸附量较大,但由于H-酸仅通过一个磺酸基团吸附在TiO2表面,过程中产生的硫酸根速率较慢,最终的光降解速率也较慢.pH 5.0条件下,虽然饱和吸附量较小,但由于吸附在TiO2表面的两个磺酸基团同时受到来自TiO2表面自由基的进攻,过程中产生的硫酸根速率较快,最终的光降解速率也较快.吸附模式的差异是导致H-酸在不同pH值条件下光催化降解途径和速率差异的关键因素.     

Environmental assessment of mercury dispersion, transformation and bioavailability in the Lake Victoria Goldfields, Tanzania

Environmental dispersion and transformation of mercury discharged from gold mining operations has been investigated in field and laboratory studies in order to provide better understanding of the degree of mercury (Hg) pollution and bioavailability in the Lake Victoria goldfields (LVGF) ecosystems. This paper reviews results already published elsewhere and presents additional data on Hg dynamics in the LVGF. Studies conducted at the Mugusu and Rwamagaza artisanal mines indicated different degrees of Hg contamination and dispersion in environmental matrices. Mercury concentration in contaminated river sediments near the Mugusu mine varied from 6.0 to 0.5 mg/kg on a dry weight basis. The highest Hg contamination levels (165-232 mg/kg) were associated with mine tailings at the Rwamagaza mine. Mercury concentrations in fish representing different dietary habits on the southwestern shore of Lake Victoria at the Nungwe Bay were very low (2-35 microg/kg) and thought to represent background levels. These and other results suggested that the use of Hg in gold extraction in the LVGF has not caused high Hg levels in lake fish. The study of Hg in lichens showed Parmelia lichen to be an effective bioindicator for atmospheric Hg contamination due to Hg emissions from gold-amalgam firing and purification operations. The Hg levels in the lichens around the Mugusu mine ranged from 3.1 to 0.1 microg/g; the highest levels were recorded in the lichens sampled close to gold-amalgam processing sites. The regional background level in the Parmelia lichen was 0.05-0.10 microg/g, with a mean level of 0.07 microg/g. Studies of Hg transformation in the mine tailings revealed unexpectedly high methylmercury (MeHg) levels in the tailings (629-710 ng/g), which indicated that oxidation and methylation of metallic Hg in the tailings occurred at significant levels under tropical conditions. Re-equilibration of the tailings with freshwater (FW) indicated the MeHg was firmly bound in the tailings and therefore very little MeHg was released to the water column (0.2-1.5 ng/L). The methylation of Hg in tropical loamy clay soil contaminated with HgCl(2) (5 mg Hg/kg) yielded MeHg concentrations of 11 and 14 ng/g when inundated with seawater and FW, respectively, for 4 weeks. Little MeHg was transferred from the soil to the equilibrated water (< or = 0.4 ng/L). Atmospheric exposure of the soil pre-inundated with FW resulted in net degradation of MeHg during the 1st week of exposure, followed by net production and accumulation of MeHg in the soil (up to 15.5 ng/g) during atmospheric desiccation. Mercury uptake by fish from the Hg(0)-contaminated aquatic sediment-tailings system in the aquarium experiment was found to be low, suggesting the low availability of MeHg for bioaccumulation in the system. These and other results provide useful insights into Hg transformation, mobility and bioavailability in tropical aquatic systems affected by Hg pollution from gold mining operations.