某市工业区土壤重金属污染及富集植物的研究

为了促进某市工业区土壤重金属污染的治理,对该区土壤和野生的主要四种植物,用原子吸收的方法测定了金属Cr、Cu和Ni的含量。结果表明：土壤中三种金属的X含量是533．14mg／ks,923．252mg／kg,310．928mg／kg。是国家土壤环境质量三级标准的533．1、2．3和1．55倍,说明污染严重;植物体内的金属含量高出正常土壤环境下的含量,经过对植物转移系数和富集系数分析,蒲公英Taraxacum ohwianum Kitam．对三种金属积累和富集最强;其次菊芋Hellanthus tuberofus L．对Cr能力较强;龙葵Solarium nigrum L．对Cu能力较强;小蓟Cirsium segetum Bunge对Ni能力较强。使利用植物积累和富集还原和净化土壤重金属污染成为可能。     

土壤中重金属测定方法探讨

采用硝酸+氢氟酸+高氯酸全分解方法消解土壤样品,并结合原子吸收分光光度法和标准加入法测定土壤中、锌、铅、镉、镍、总铬的含量.结果表明,该方法具有操作简便、快速,节省试剂,准确可靠等特点:实际土壤样品的检测结果完全能满足环境土壤样品测定的要求.     

火焰原子吸收法测定苹果中波尔多液的农药残留

通过原子吸收法测定苹果果皮、果肉上波尔多液的农药残留铜的含量,结果表明:喷洒了波尔多液的苹果果皮上铜含量明显大于果肉,在果皮上有一定的农药残留;而未喷洒波尔多液的苹果果皮和果肉中铜的含量的差异很小。     

Combined fluorescence and electrochemical investigation on the binding interaction between organic acid and human serum albumin

Human serum albumin (HSA) is a plasma protein responsible for the binding and transport of fatty acids and a variety of exogenous chemicals such as drugs and environmental pollutants. Such binding plays a crucial role in determining the ADME (absorption, distribution, metabolism, and excretion) and bioavailability of the pollutants. We report investigation on the binding interaction between HSA and acetic acid (C2), octanoic acid (C8) and dodecanoic acid (C12) by the combination of site-specific fluorescent probe, tryptophan intrinsic fluorescence and tyrosine electrochemistry. Two fluorescent probes, dansylamide and dansyl-L-proline, were employed in the displacement measurement to study fatty acid interaction with the two drug-binding sites on HSA. Intrinsic fluorescence of tryptophan in HSA was monitored upon addition of the fatty acids into HSA. Electrocatalyzed response of the tyrosine residues in HSA by a redox mediator was used to investigate the binding interaction. Qualitatively, observations made by the three approaches are very similar. HSA did not show any change in either fluorescence or electrochemistry after mixing with C2, suggesting there is no significant interaction with the short-chain fatty acid. For C8, the measured signal dropped in a single-exponential fashion, indicative of independent and non-cooperative binding. The calculated association constant and binding ratio is 3.1×106 L/mol and 1 with drug binding Site I, 1.1×107 L/mol and 1 with Site II, and 7.0×104 L/mol and 4 with the tryptophan site. The measurement with C12 displayed multiple phases of fluorescence change, suggesting cooperativity and allosteric effect of C12 binding. These results correlate well with those obtained by the established methods, and validate the new approach as a viable tool to study the interactions of environmental pollutants with biological molecules.     

采用火焰原子吸收分光光度法测定水样中镍含量的不确定度评定

采用火焰原子吸收分光光度法对水样中镍的含量进行测定,分析测量过程中不确定度来源及各不确定度分量对总不确定度的影响,确定测定结果的置信区间。给出本实验室测定水样中镍含量的扩展不确定度为0．062mg／L（k=2）。     

燃煤锅炉烟气氨法脱硫技术的应用

电厂燃煤锅炉烟气脱硫是减少和控制酸雨的有效手段。LS氨法喷雾脱硫技术具有脱硫效率高、环境效益好、资源综合利用的特点。以合成氨生产装置回收的低浓度氨水为吸收剂,实施锅炉烟气脱硫技术改造．取得良好的应用效果。     

火焰原子吸收法测定土壤中金属锌吸光度高的原因

通过实验发现,由于在消解过程中使用玻璃管移取氢氟酸,导致了玻璃中的锌进入了样品中,给样品的分析带来了干扰,从而导致了分析的失败.     

组合人工湿地对城镇污水处理厂尾水中有机物的去除特征研究

采用物理分级和三维荧光光谱法,研究了组合人工湿地对城镇污水处理厂尾水中不同形态有机物的去除特征.结果表明,组合人工湿地对污水处理厂尾水具有较好的深度处理效果,出水水质基本可以达到国家地表水环境质量标准(GB38382-2002)Ⅲ或Ⅳ类水标准.组合人工湿地处理系统对尾水中CODCr和BOD5总体去除率分别达到35.2%和44.3%,对尾水中总有机碳(TOC)、溶解性有机碳(DOC)、颗粒有机碳(POC)的平均去除率分别为46.9%、45.9%、48.3%.组合人工湿地系统不同单元对尾水中有机物的去除贡献率存在差异,其中,潜流湿地单元对尾水中CODCr和BOD5及其不同组分有机碳的去除效率较高.试验期间,由于藻类滋生,表流湿地单元出水中有机物含量波动较大,去除效果明显降低,藻类被打捞后,出水水质明显改善.三维荧光光谱分析结果显示,各个处理单元取样点的水样三维荧光光谱均出现4个明显的荧光峰.人工湿地各单元出水溶解性有机质(DOM)中,类蛋白和类腐殖酸物质含量较高,类富里酸物质含量较低.人工湿地对类蛋白和类腐殖酸物质有较强的去除作用.     

三元高吸油树脂的制备及其吸油性能

采用本体聚合法,以丙烯酸丁酯(BA)、苯乙烯(St)和甲基丙烯酸十八酯(SMA)为单体,反应型低聚硅氧烷(OSS)为交联剂,偶氮二异丁腈(AIBN)为引发剂制备了三元高吸油树脂,优化了制备条件,考察了其对不同有机溶剂的吸油性能,并对其进行了表征。实验结果表明:树脂制备的优化条件为BA,St,SMA,OSS,AIBN的质量分别占单体总质量的39.60%,39.60%,20.80%,0.21%,1.50%,于55℃下反应24 h;在该优化条件下所制备的树脂对氯仿的吸油率可达80.2 g/g;树脂对氯仿和二氯甲烷的吸油率远高于其他有机溶剂。表征结果显示,树脂形成了一定的网络结构,具有较好的耐热性、耐寒性和热稳定性。     

喷淋工艺处理PVC塑料生产废气

采用喷淋工艺处理PVC塑料生产废气,将专利的吸收液与改型的喷淋塔相结合,在中试成功的基础上进行了实际工业化应用。应用结果表明:采用该工艺处理某PVC塑料生产企业的生产废气,吸收液在喷淋塔循环液中所占体积分数为15%时,废气中各污染物指标的去除率达85%以上,对于难处理的苯系物也能较好地去除;处理后废气中各污染物指标的含量满足GB 14554—1993《恶臭污染物排放标准》和DB 44/27—2001《大气污染物排放限值》的要求;该工艺装置运行费用较低,仅为电费和少量药剂费用,吸收液可循环使用,设备保养及维护简单,可满足市场需求。