散射光下铁(III)-丙酮酸盐配合物还原铬(VI)的研究

研究了在散射光下铁(III)-丙酮酸盐配合物对铬(V I)的光还原反应;考察了溶液pH、铁(III)、丙酮酸钠、铬(V I)浓度对反应的影响;分析了铬(V I)光还原反应的动力学。实验结果表明:铁(III)-丙酮酸盐配合物体系能在较弱的散射光下还原铬(V I)。在铬(V I)浓度为19.2μm o l/L、铁(III)浓度为10.0μm o l/L、丙酮酸钠浓度为240μm o l/L、pH为3.0、光照240m in的条件下,铬(V I)的还原率达到99.7%。从表观动力学方程的反应级数看,铁(III)的级数(0.83)最高,铁(III)浓度是影响铬(V I)光还原反应速率的主要因素,铁(II)是铬(V I)光还原的主要还原剂。     

ARE RURAL RESIDENTS WILLING TO PAY ENOUGH TO IMPROVE DRINKING WATER QUALITY?1

ABSTRACT: The concentrations of iron and sulfate in community water supplies are a concern for a number of areas in southwestern Minnesota. This study used the contingent valuation method to determine how much consumers would be willing to pay to improve their drinking water quality. On average, individuals were willing to pay US$5.25 per month (in 1995 U.S. dollars) to reduce the level of iron and US$4.33 per month to reduce the level of sulfate in their water to the USEPA's secondary standards for drinking water quality. Respondents with negative perceptions of their drinking water quality were willing to pay more to improve water quality. The aggregate annual willingness to pay (WTP) for all consumers in community water systems in southwestern Minnesota that were out of compliance with water quality standards were estimated to be US$2.4 million and US$2.0 million (in 1995 dollars) for reducing the levels of iron and sulfate, respectively. Yet the total WTP of consumers who use small community water systems may not be enough to pay the full cost of providing improved water in those systems. Economies of scale in water treatment and difficulties in financing improvements mean that technical innovation, government assistance, or institutional changes may be needed to improve water quality in these areas.     

A mathematical model of crevice corrosion for buried pipeline with disbonded coatings under cathodic protection

Crevice corrosion occurs in a holiday and disbonded region between coating and pipeline steel. Cathodic protection (CP) is generally recognized as the most effective method for corrosion prevention of pipeline, but its effectiveness may be reduced at defects in a disbonded coating. It is difficult to measure and probe corrosion parameters accurately based on experimental work. Therefore, a mathematical model is necessary to identify the phenomena and mechanisms that contribute to the crevice corrosion process. In this work, a mathematical model was developed to determine the evolution of chemical and electrochemical transient processes of crevice corrosion in NaCl dilute solution, and the effect of cathodic protection and crevice width on corrosion of 20# steel pipeline with disbonded coatings. Results have demonstrated that the extent of crevice corrosion depends on the crevice geometry and could be influenced by the increase of crevice depth and decrease of its width. The oxygen concentrations drop significantly inside a crevice whether CP is applied or not and whether crevice width decreased or not. The pH values and conductivity of crevice solution increase with the time. The research provides a theoretical foundation for cathodic protection of pipelines and establishes an effective corrosion model which can identify the phenomena and mechanisms of the crevice corrosion process. This work could be used to help mitigate the corrosion failure of pipelines to prevent catastrophic accidents in oil, gas and chemical process industries.     

供水管网铁释放的影响因素相对重要性分析

供水管网的铁释放问题近年来日益受到关注.影响供水管网铁释放的因素众多,本研究选取了pH、溶解氧(DO)、碱度(Alk)、硬度、氯离子(Cl~-)、硫酸根(SO_4~(2-))、温度(T)和水力停留时间(HRT)这8个影响因素,利用逐步回归和偏相关分析,建立了铁释放的非线性幂指数模型,并用标准化回归系数和偏相关系数比较了这些因素的相对重要性.结果表明,铁释放模型拟合效果良好;用标准化回归系数衡量影响因素相对重要性时,SO_4~(2-)、HRT、Cl~-和T是相对重要的因素,相对重要性排序为SO_4~(2-)≈HRTCl~-T;用偏相关系数衡量时,HRT、SO_4~(2-)、Alk、Cl~-和T是相对重要的因素,排序为HRTSO_4~(2-)AlkCl~-T.综合两种系数的分析结果,HRT、SO_4~(2-)和Cl~-是本研究条件下相对重要的因素,T和Alk的相对重要性视实际情况变动.     

我国工业危险废物的来源、处理及监管对策与建议

通过大量环境统计数据的分析,对我国工业危险废物的产生、综合利用、处置和贮存,从行业来源、区域分布进行了分析和总结。结合我国工业危险废物企业自建设施和政府集中处理设施处理情况,对我国工业危险废物的处理和环保监管对策提出了若干建议。     

Ti/SnO_2-Sb阳极-空气阴极电催化降解染料废水

为解决电化学法处理高盐染料废水存在的能耗大、成本高等问题,分别采用溶胶-凝胶法和辊压法制备Ti/SnO_2-Sb阳极和空气阴极,构建了Ti/SnO_2-Sb阳极-空气阴极双极体系(TSSA-ADC)。甲基橙(MO)作为高盐染料废水的典型污染物,考察了电流强度、MO浓度、电解液浓度和初始p H对TSSA-ADC体系和TSSA单阳极体系降解MO的影响。结果表明:与TSSA单阳极体系相比,TSSA-ADC体系具有更好的抗有机负荷冲击、抗盐分冲击、抗酸碱波动能力,能够维护酸碱平衡防止硬度离子结垢。最佳反应条件为电流强度为0.030 A,电解液浓度为3%,MO浓度为100 mg/L,初始pH=6。以MO去除率达到98%为基准,TSSA-ADC体系比TSSA体系可节能74.26%。     

军绿有机涂层和金属漆涂层全浸泡下的腐蚀行为对比研究

目的针对车辆装备长期在高盐雾、高湿热、高日照等恶劣的气候环境下使用,会受到腐蚀影响的现状,探究现役军用有机涂层防护性能。方法采用电化学阻抗谱技术研究军绿有机涂层和金属漆涂层在3.5%NaCl溶液中的腐蚀电化学行为,分析这两种涂层在浸泡期间的电化学阻抗谱特征,通过拟合等效电路得到涂层电阻R_c和涂层电容C_c,并用这两个电化学参数评价军绿有机涂层和金属漆涂层的耐蚀性能。结果军绿有机涂层抗腐蚀介质渗透能力很强,而金属漆涂层抗腐蚀介质渗透能力稍弱。结论两种涂层都表现出很好的防护性能,且金属漆涂层在腐蚀后期的防护性能要优于军绿有机涂层。     

海洋环境下ZL115-T5铸铝合金/C41500海军黄铜腐蚀行为研究

目的研究海军某型装备壳体结构材料在海洋环境下的腐蚀行为及规律。方法根据折算出的实验室加速腐蚀试验环境谱,开展了ZL115-T5铸铝合金试验件、ZL115-T5铸铝合金/C41500海军黄铜接触试验件、模拟实际涂抹黄油试验件以及模拟维护涂抹缓蚀剂试验件的实验室加速腐蚀试验。结果得到了该型铝合金在不同服役年限及服役状态下的腐蚀形貌、质量、平均腐蚀深度以及腐蚀损伤度变化规律。结论该型合金在不同服役状态下的腐蚀行为呈现差异化,ZL115-T5铸铝合金与C41500海军黄铜偶合接触会加速铸铝合金的腐蚀,黄油能够在一定程度上抑制电偶腐蚀,但效果并不明显。缓蚀剂能够延缓海洋环境下ZL115-T5铸铝合金腐蚀,其中THFS-10软膜缓蚀剂以及THFS-15长效硬膜缓蚀剂效果较好。     

富营养化淡水中黑色金属试样腐蚀加速的微生物学机制研究

目的探究黑色金属在污染淡水中后期腐蚀加速规律的生物学机制。方法采用高通量测序分析A3钢在富营养化水体和清洁水体中腐蚀产物内微生物的种群结构,并结合元素分析和XPS分析。结果获得了A3钢的腐蚀产物内微生物的门水平物种分布柱状图、OTU估计数统计表、OTU韦恩图、硫酸盐还原菌各属的相对丰度、微生物属水平热图等数据。结论在富营养化水体中,硫酸盐还原菌呈现更显著的水平,造成金属的硫化腐蚀更为严重,验证了黑色金属在富营养化污染淡水水体中后期腐蚀速率反转加速的现象。     

三种流速下高强钢与微弧氧化钛电偶腐蚀研究

目的研究三种流速下微弧氧化钛和高强钢的电偶腐蚀行为。方法在面积比为1:1情况下进行1,3,7 m/s流速下的电化学测试和电偶腐蚀试验研究。结果随着流速的增大,偶合电流、总腐蚀速率和电偶腐蚀速率增大。当流速为7 m/s时,高强钢总腐蚀速率和电偶腐蚀速率分别达到8.64 mm/a和0.39 mm/a,与静态相比分别增大146倍和15.6倍,与1 m/s流速下相比分别增大8.6倍和5倍。结论在面积比为1:1时,冲刷腐蚀速率远大于电偶腐蚀速率。