Leaching of bisphenol A (BPA) to seawater from polycarbonate plastic and its degradation by reactive oxygen species

In this study, (1) change in the concentration of bisphenol A (BPA) leached from polycarbonate (PC) tube to control water (BPA free), seawater and river water at 20 and 37 degrees C as a function of time, (2) the fate of BPA caused by addition of H(2)O(2) and Fe(3+) to seawater containing BPA leached from PC tube were assessed. BPA leached from PC tube to all water samples increased with the ascendant of temperature and with the passage of time. The BPA leaching velocity in seawater was the fastest in three samples (11 ng/day for seawater, 4.8 ng/day for river water 0.8 ng/day for control water at 37 degrees C).BPA leaching velocity from PC tube was significantly high at pH 8 (50 mM Na(2)HPO(4)) and increased dose-dependently. There was no difference in the velocity of BPA among the 50 mM phosphate-buffers at pH 6.5, 7.0 and 7.5. BPA was leached three times higher by addition of Na(+) than K(+). However, the higher the K(+) concentration, the larger the BPA leached from PC tube. Na(+) mixed with PO(4)(-) was effective on BPA leaching from PC tube, but not with SO(4)(-) or Cl(-). The results suggested that BPA leaching from PC tube would be attributed to the concentration of bibasic phosphate such as Na(2)HPO(4) and K(2)HPO(4) in water samples. BPA was degraded in both control water and seawater in the presence of radical oxygen species, but the degradation rate was lower in seawater than in control water, suggesting that anti-oxidative system exists in seawater. Neo-synthesized substance in both control water and seawater in the presence of reactive oxygen species was identified as BPA-quinone by LC-MS.     

Selective leaching of valuable metals from waste printed circuit boards

This study was carried out to recover valuable metals from the printed circuit boards (PCBs) of waste computers. PCB samples were crushed to smaller than 1 mm by a shredder and initially separated into 30% conducting and 70% nonconducting materials by an electrostatic separator. The conducting materials, which contained the valuable metals, were then used as the feed material for magnetic separation, where it was found that 42% of the conducting materials were magnetic and 58% were nonmagnetic. Leaching of the nonmagnetic component using 2 M H2SO4 and 0.2 M H2O2 at 85 degrees C for 12 hr resulted in greater than 95% extraction of Cu, Fe, Zn, Ni, and Al. Au and Ag were extracted at 40 degrees C with a leaching solution of 0.2 M (NH4)2S2O3, 0.02 M CuSO4, and 0.4 M NH4OH, which resulted in recovery of more than 95% of the Au within 48 hr and 100% of the Ag within 24 hr. The residues were next reacted with a 2 M NaCl solution to leach out Pb, which took place within 2 hr at room temperature.     

生物活性炭法深度处理纺织废水二级出水中生物活性的研究

采用上流式曝气生物活性炭法处理碱减量印染废水二级生物处理出水，利用TTC-脱氢酶活性（DHA）法监测反应器内DHA生物活性分布。研究发现反应器内生物炭表面附着生物膜活性较高，特别是反应器上部生物碳粒同样具有较高的DHA活性，这与反应器运行一年多能够保持对COD、色度和UV等较高去除率有一定关系。还研究了活性炭吸附、反应器反冲洗对DHA活性的影响。本研究为曝气生物活性炭法有效去除印染碱减量废水中难降解有机物提供了一定的理论依据。     

含有机物铁泥的超临界水氧化法资源化

氨基染料生产过程中产生大量含有机物的铁泥,对环境造成严重污染并造成资源的极大浪费.利用超临界水氧化法对含有机物铁泥进行资源化处理研究,并对产物进行了X射线衍射分析(XRD)、色差实验与电子探针分析.研究结果显示,用超临界水氧化法处理铁泥可以将铁泥中所含的有机物完全氧化,真正实现环境友好;超临界水首先将铁泥氧化成α-Fe2O3与γ-Fe2O3,再经过800℃煅烧后可以作为氧化铁红颜料使用;超临界反应压力对样品的晶型与颜色影响不大.     

污水处理中的人工湿地强化技术研究

人工湿地作为一种新型污水生态处理工艺受到越来越广泛的重视,在生活污水、特种工业废水、采矿污水、农业和畜牧业污水以及水产养殖废水等处理中得到了广泛的应用.但是其本身的局限却限制了它在高浓度废水、某些工业废水处理等方面的应用,在寒冷地区的应用也受到限制.本研究分析了一些强化技术(如湿地内部要素强化、工艺强化和工程强化等)在提高人工湿地的净化效能以及扩大其应用范围的可能性.     

Determination of the residue dynamics and dietary risk of thiamethoxam and its metabolite clothianidin in citrus and soil by LC-MS/MS

A modified quick, easy, cheap, effective, rugged and safe (QuEChERS) method was developed for the determination of thiamethoxam and its metabolite clothianidin in citrus (including the whole citrus, peel and pulp) and soil samples by liquid chromatography-tandem mass spectrometry. The sample was extracted with acetonitrile and purified with octadecylsilane. The detection limits of both compounds were 0.0001–0.0002?mg kg^–1, while the limit of quantification of thiamethoxam was 0.002?mg kg^–1 and the limit of quantitation of metabolites was 0.001?mg kg^–1. The recovery was 70.37%–109.76%, with inter-day relative standard deviations (RSD) (n?=?15) values ≤9.46% for the two compounds in the four matrices. The degradation curve of thiamethoxam in whole citrus and soil was plotted using the first-order kinetic model. The half-life of the whole citrus was 1.9–6.2?days, and the half-life of the soil was 3.9–4.2?days. The terminal residue of thiamethoxam (the sum of thiamethoxam and clothianidin, expressed as thiamethoxam) was found to be concentrated on the peel. The final residual amount of thiamethoxam in the edible portion (pulp) was less than 0.061?mg kg^–1. The risk quotient values were all below 1, indicating that thiamethoxam as a citrus insecticide does not pose a health risk to humans at the recommended dosage.     

EVO(乳化油)-Mg(OH)2双功能缓释剂强化修复三氯乙烯污染地下水

氯代烃污染地下水在外加有机质(电子供体)进行强化还原脱氯时,存在有机质消耗快、pH持续降低等影响脱氯效率的问题。利用乳化油(EVO)与胶体氢氧化镁复配的方法,制备了一种兼具电子供体缓释性和OH-缓释性的双功能缓释剂EVO-Mg(OH)2;成功制备了不同EVO∶Mg(OH)2配比的EVO-Mg(OH)2试剂,并对其稳定性、分散性及粒径分布进行了研究;向模拟砂柱中注入不同体积的EVO-Mg(OH)2,考察试剂的迁移性能以及试剂注入对三氯乙烯(TCE)迁移的影响;开展了EVO-Mg(OH)2强化TCE还原脱氯摇瓶实验,考察了该试剂对脱氯效果的影响。结果表明：不同EVO∶Mg(OH)2配比的试剂稳定性及分散性良好,粒径无明显差异;EVO-Mg(OH)2可以有效地在多孔介质中迁移并实现部分滞留;注入量对EVO-Mg(OH)2的迁移性有一定的影响;EVO-Mg(OH)2可以促进TCE溶解和迁移从而减小EVO-Mg(OH)2和TCE之间的传质阻力;EVO-Mg(OH)2能够实现电子供体及OH-的双重缓释,有效促进脱氯微生物的生长,提高TCE的降解速率(k=0.128 d-1),同时抑制pH的降低(pH=7.5)。     

低C/N比城市污水短程硝化特性及微生物种群分布

以城市污水厂二沉池回流液为接种污泥,研究了低C/N城市污水短程硝化特性及其微生物种群密度分布规律,并对比研究了SBR和SBBR 2种反应器短程硝化特性的差异。结果表明：在温度（30±1）℃、pH=7.9~8.2、DO=1.0 mg·L-1的条件下,通过分段曝气的运行方式、经过29 d的运行,2个反应器均实现了短程硝化的高效启动,NH4+-N转化率稳定在99%,短程硝化率稳定在90%以上;相比于SBR,SBBR更有利于AOB菌种的富集,且SBBR达到亚硝酸盐积累率最大效果的时间快于SBR。利用聚合酶链反应（PCR）和克隆测序等分子生物学技术分析得出,在短程硝化稳定运行的SBR系统中,AOB菌种与NOB菌种的占比为2.3：1。     

酸碱改性活性炭吸附微污染水源水中的Ni2+

通过HNO3-KOH对活性炭进行改性,采用扫面电镜（SEM）、比表面积分析（BET）、红外光谱分析（FT-IR）和Boehm滴定法对改性前后的活性炭进行表征,研究了改性前后的活性炭在不同条件下对微污染水源水中Ni2+的吸附能力和动力学。结果表明：改性活性炭表面含氧酸性官能团数量增加,比表面积和总孔容均略有降低,孔径变化不明显。在Ni2+浓度为0.4 mg·L-1,改性活性炭投加量5.0 g·L-1,温度30 ℃时,反应1 h去除率可达95.55%,剩余Ni2+浓度为0.017 8 mg·L-1,达到《生活饮用水卫生标准》（GB5749-2006）中的要求。相同条件下,改性前活性炭对Ni2+的去除率仅为74.45%,剩余Ni2+浓度达不到标准要求。活性炭对Ni2+的等温吸附更符合Langmuir方程,吸附动力学数据符合准二级动力学方程。     

氨氮废水处理技术研究进展

氨氮废水是造成水体富营养化的主要因素之一 ,本文综述了氨氮废水的几种主要处理技术 ,介绍了它们的处理原理以及适用条件 ,指出了今后研究工作中需要解决的问题和氨氮废水处理技术今后的发展方向