Recovery of Ni(II) from real electroplating wastewater using fixed-bed resin adsorption and subsequent electrodeposition

Resin adsorption and subsequent electrodeposition were used for nickel recovery. Treated wastewater can meet the Electroplating Pollutant Discharge Standard. The spent resin is completely regenerated by 3 BV of 4% HCl solution. 95.6% of nickel in concentrated eluent was recovered by electrodeposition. Effective recovery of high-value heavy metals from electroplating wastewater is of great significance, but recovering nickel ions from real electroplating wastewater as nickel sheet has not been reported. In this study, the pilot-scale fixed-bed resin adsorption was conducted to recover Ni(II) ions from real nickel plating wastewater, and then the concentrated Ni(II) ions in the regenerated solution were reduced to nickel sheet via electrodeposition. A commercial cation-exchange resin was selected and the optimal resin adsorption and regeneration conditions were investigated. The resin exhibited an adsorption capacity of 63 mg/g for Ni(II) ions, and the average amount of treated water was 84.6 bed volumes (BV) in the pilot-scale experiments. After the adsorption by two ion-exchange resin columns in series and one chelating resin column, the concentrations of Ni(II) in the treated wastewater were below 0.1 mg/L. After the regeneration of the spent resin using 3 BV of 4% (w/w) HCl solution, 1.5 BV of concentrated neutral nickel solution (>30 g/L) was obtained and used in the subsequent electrodeposition process. Using the aeration method, alkali and water required in resin activation process were greatly reduced to 2 BV and 3 BV, respectively. Under the optimal electrodeposition conditions, 95.6% of Ni(II) in desorption eluent could be recovered as the elemental nickel on the cathode. The total treatment cost for the resin adsorption and regeneration as well as the electrodeposition was calculated.     

粉末活性污泥处理含铀废水的特性

以生活污水处理厂剩余活性污泥为原料,制备粉末活性污泥(PAS)作为生物吸附剂,考察p H值,PAS投加量,U(Ⅵ)初始浓度和吸附时间对PAS吸附U(Ⅵ)的影响,探讨了PAS吸附U(Ⅵ)的作用机理。实验结果表明,在U(Ⅵ)初始浓度为10 mg/L时,其最佳吸附p H值为3,去除率97.77%,吸附平衡时间120 min;吸附过程较好地拟合了准二级动力学模型(R2≈1)和Freundlich等温模型(R2≈1);X射线能谱和离子交换实验分析表明,离子交换为其主要吸附方式,参与交换的主要离子为Ca2+;红外光谱分析表明,PAS吸附U(Ⅵ)后自身结构未发生改变。以0.1 mol/L的HCl溶液作为解吸液,初次解吸率达92.83%,循环利用3次仍具有较好的吸附效果。     

基于热湿交换理论的巷道风流温、湿度影响因素研究

为了研究巷道风流参数的影响因素、预测风流温湿度的变化规律,结合热湿交换理论,建立了风流与围岩壁面之间热湿交换的数学模型,以及贴体坐标系下围岩内部温度场的导热微分方程;利用数值方法,将围岩内部的导热问题与影响风流参数变化的热湿交换问题耦合起来,并以大柳塔煤矿52505综采工作面为例进行计算,得到了与实测参数较为一致的模拟结果,验证了该数值方法的有效性。研究结果表明:风流温度受原始岩温、入风流温度、局部热源强度等因素的影响,风流相对湿度与入风流温、湿度以及井下湿源的数量和强度有关;巷道壁温作为将围岩温度场与风流参数之间关联起来的主要因素,对模拟结果影响较大,其数值取决于壁面与风流之间热湿交换以及围岩原始岩温。     

天然沸石床处理受污染景观水体的试验

采用天然沸石滤床对富营养化景观湖水进行净化试验,结果表明,天然沸石滤床能有效地净化受污染的湖水,CODCr、氨氮、总磷和浊度的去除率分别为35.8%、95.0%、66.7%和78.0%,沸石能有效地去除水中的氨氮,其作用机理包括离子交换和生物硝化两种作用。     

阳离子交换树脂富集衍生气相色谱法测定二甲基胂酸

实验发现,碘化二甲基胂(IDA)具有很好的色谱挥发性,在5％,10％SE-30柱上可得到较好的色谱峰。二甲基胂酸(DMA)碘化后生成碘化二甲基胂(IDA)。本文提出了新的碘化萃取体系:SnCl_2-KI(1moI/l)-HCl(6mol/l)-甲苯。该体系具有转化率高、干扰少的优点。实验还发现,经过阳离子交换树脂富集,有效地消除了低浓度时,DMA转化中或转化后的分解或吸附对测定的影响,从而提高了分析结果的准确度。     

Study of the dynamics of estuarine and coastal waters using remote sensing: the Tinto-Odiel estuary, SW Spain

This paper deals with the application of satellite images to characterize some aspects of the circulation dynamics of the Tinto-Odiel estuary using turbidity patterns as ‘natural tracers’. 15 images (Landsat TM and Spot HRV) were processed to provide synoptic, instantaneous views of the circulation patterns under different environmental conditions. In addition, a comparison was made between results of oceanographic field work, using biplanes and fluorescent tracers, and satellite image turbidity patterns used as ‘ground truth’ data for specific hydroclimatic situations. This approach allowed (1) the identification and mapping of dynamic processes of interest during a theoretical tidal cycle, (2) the elaboration of additional information on the ‘flow schemes’ at the mouth of the estuary with improved spatial and temporal resolution, and (3) the supply of basic data to improve the knowledge of exchange processes between estuarine and coastal waters. The results of this study are considered to be useful for the management of the estuarine system.     

酸阻滞法处理含酸及其相应盐的废液

本文主要介绍在含酸及其相应盐的废液中分离酸和盐的一种方法。将含酸及其相应盐的废液，通过装有强碱性阴离子交换树脂柱，其中的酸受到阻滞，而相应的盐能顺利通过，然后用水洗脱，则流出的是含酸的溶液，使酸和相应的盐得到了分离。经ＦｅＳＯ４－Ｈ２ＳＯ４和ＺｎＳＯ４－Ｈ２ＳＯ４两组废液的试验，均能使酸和金属得到回收。分离后的废水，可达标排放，废液得到了处理。酸阻滞法简单易行，易于投产使用，不受规模大小的限制。     

流动注射在线离子交换富集-原子荧光光谱法测定环境水样中痕量汞

提出了一种流动注射在线离子交换富集一氢化物发生原子荧光光谱法测定水样中总汞的分析方法。设计了双柱并联富集，串联洗脱的在线离子交换流路及操作程序，优化了各项化学条件及流路参数。方法操作简便快速，灵敏度高，干扰少。富集倍数达25倍以上，采样频率为30次／h，回收率达90％－105％。应用于环境水样中痕量汞的测定，获得了满意的结果。     

聚苯乙烯基离子交换纤维去除铅离子的应用研究

聚苯乙烯其离子交换纤维是一种理想的离子交换材料。它的特殊的物理形态决定它对一些有害气体如铅烟、颗粒铅等具有很好的净化作用，铅烟净化效率可达８０％；对水溶液中毒性铅离子去除率可达８６％。该纤维可做为治理毒性铅离子的材料。     

模拟酸雨对烤烟叶片光合特性和叶绿素荧光参数的影响

以烤烟为供试材料,采用土培盆栽的方法研究了不同pH值的模拟酸雨(pH5.6、pH4.5、pH4.0、pH3.5、pH3.0、pH2.5、pH2.0)对烤烟叶片叶绿素含量、气体交换和叶绿素荧光参数的影响.结果表明:pH≥3.5处理的轻度酸雨对烤烟Chl.a含量影响不大,但pH≤3.5处理烤烟叶片Chl.b和总叶绿素含量显著下降.pH≤2.5模拟酸雨使烤烟叶片净光合速率(Pn)、气孔导度(Ls)、胞间CO2浓度(Ci)、叶面饱和蒸气压力亏缺(VPD)显著降低,使烤烟叶片的气孔限制值(Ls)和潜在水分利用效率(WUEi)显著升高,模拟酸雨使pH2.0处理烤烟叶片的蒸腾速率(Tr)和pH2.5处理的瞬时水分利用效率(WUE)显著降低.pH≥3.5处理的光合有效量子产量(EQY)、光合电子传递速率(ETR)和光化学猝灭(qP)与对照差异不大,但pH≤3.0处理明显降低;烤烟叶片的非光化学猝灭呈先升高后降低趋势,pH≥3.5处理的非光化学猝灭(NPQ)明显高于pH≤3.0处理.