TiO2/H2O2/UV和TiO2/O3/UV降解对氯苯甲酸和喹啉的试验研究

主要叙述TiO2/H2O2/UV和TiO2/O3/UV体系降解对氯苯甲酸(4-CBA)和喹啉的试验研究.研究表明,(1)在TiO2/H2O2/UV体系里目标物降解速度先随过氧化氢投加量的增加而提高,但超过一定浓度之后便开始下降;(2)在TiO2/O3/UV体系中,目标降解物的反应速度都非常快,且臭氧浓度高的时候降解速度更快;(3)二氧化钛催化剂在TiO2/O3/UV体系中作为积极因素有助于提高反应速率,而在TiO2/H2O2/UV体系是消极因素,会降低反应速率.     

分光光度法测定降水中微量过氧化氢

研究了一种测定降水中微量过氧化氢的方法。在0.4～1.5mol／L磷酸介质中，过氧化氢与钒（V）及2－（3，5-二溴-2-吡啶偶氮）－5-二乙氨基苯酚（3,5-diBr-PADAP）反应形成一种组成比为1：1：1的蓝色三元配合物，其最大吸收波长为598nm，表现摩尔吸光系数为5.6×104L·mol-1·cm-1。过氧化氮量在2×10-7～1．3×10－5mol／L时服从比耳定律。方法简便，选择性较高，用于降水中微量过氧化氢的直接测定，结果令人满意。     

碳纤维生产工艺含氰废气治理

在聚丙烯腈基碳纤维的生产过程中将产生大量有毒含氰废气，其危害性已引起人们的普遍关注。提出了催化燃烧的治理方案和工艺。实际运行结果表明：该工艺过程操作简便，效果较好，净化后气体达到了国家排放标准。     

生物催化氧化法脱除H2S的填料选择研究

针对H2S污染的严峻形势,构建了包括催化再生装置和生物滴滤器的生物催化氧化装置,进行了装置的填料选择研究.经对比试验得出填料脱硫性能的优劣顺序为:沸石＞焦炭＞多面空心塑料小球.在温度为30 ℃、进气量为0.25 m3/h、进气H2S为2 000 mg/m3、喷淋量为1 000 mL/h、喷淋液的pH为1.97、Fe3 为0.05 mol/L的条件下,装填沸石的生物催化氧化装置的出气H2S浓度足以达到<恶臭污染物排放标准>(GB 14554-93)规定的一级厂界标准值.试验证明,生物催化氧化法是有效的新型脱除H2S技术,具有良好的经济、社会及环境效益,应进一步开展中试研究.     

O3/H2O2高级氧化技术H2O2加入量的简易控制方法

对与臭氧有着不同反应活性的3类有机污染物,探讨并建立了O3/H2O2高级氧化技术H2O2较优投加量的简易控制方法.结果表明,水中存在溶解臭氧是H2O2与臭氧降解效率具有协同作用的必要条件,另外,H2O2的较优加入量直接依赖于目标有机污染物与臭氧的反应活性.对于不同的有机物及在常规的臭氧化水处理时间内,H2O2加入量控制在单独臭氧化处理时水中溶解臭氧的20～30倍(质量比)之间为宜.这种简易控制H2O2加入量的方法对推广O3/H2O2技术在实际废水处理中的应用具有重要的意义.     

腐殖质及其模型化合物的H2O2光化学生成研究

在模拟太阳光下研究了多种腐殖质及其模型化合物的过氧化氢（H₂O₂）生成动力学,并对其生成机制进行了探讨.结果表明不同来源或不同形式的腐殖质在模拟太阳光照射下均能产生H₂O₂.不同腐殖质生成H₂O₂速率差异不大,范围为6.379~15.784nmol/（L·min）,腐殖酸生成H₂O₂速率略快于富里酸.对于腐殖质模型化合物,邻苯二酚、间苯二酚、对苯二酚、苯醌、邻茴香胺、对茴香胺、水杨酸和2,6-二甲氧基-1,4-苯醌等8种模型化合物没有产生明显的H₂O₂,而藜芦醇、对氨基苯甲酸、3,5-二羟基苯甲酸（DHBA）、2,5-二羟基-1,4-苯醌、苯酚、苯甲酸和苯胺等7种化合物均可检测到H₂O₂产生.但其产生H₂O₂的速率差异较大,相差1~2个数量级,生成H₂O₂速率最快的化合物为2,5-二羟基-1,4-苯醌和DHBA,较慢的为苯酚、苯甲酸和对氨基苯甲酸.基于腐殖质生成H₂O₂机制,推测典型模型化合物DHBA的H₂O₂生成机制可能为光照条件下该化合物跃迁为单重激发态,该激发态发生分子内电子转移,生成还原性自由基中间体,该中间体和O₂反应,生成了超氧负离子（O₂·^-）,随后与水中H⁺反应生成了H₂O₂.     

胶原纤维基多孔碳纤维用于电化学产双氧水——酸处理对产双氧水性能的影响

为获得通过电化学的氧还原反应（ORR）高效原位生成双氧水（H₂O₂）的新型碳材料,基于一类天然生物质-皮胶原纤维为基础材料制备出多孔碳纤维材料（PCFs-x）.利用皮胶原纤维分子中的-COOH、-NH₂等官能团与铁盐之间的较强的络合作用来吸附铁离子,碳化后经酸浸获得PCFs-x材料.XRD、SEM、BET等手段对不同浓度硝酸浸取后所获得的PCFs-x进行系统的结构表征,测试其电子转移数,考察了其氧还原反应活性及电化学还原氧气产H₂O₂的性能.结果表明,胶原纤维经过上述制备流程后可获得有序结构的PCFs-x,其中浓度为1mol/L时获得的材料具有最好的产H₂O₂效果和电流效率,氧还原反应2.5h后H₂O₂累积浓度达到148.81mg/L,电流效率72.33%.实验结果为基于胶原纤维制备新型高效的原位电化学产双氧水的碳材料提供了理论基础与可借鉴的思路.     

Release kinetics of vanadium from vanadium titano-magnetite: The effects of pH, dissolved oxygen, temperature andforeign ions

As part of a broader study of the environmental geochemistry behavior of vanadium(V), the release kinetics of V from the dissolution of natural vanadium titano-magnetite under environmentally relevant conditions was investigated. In both the acidic and basic domains, the V release rate was found to be proportional to fractional powers of hydrogen ion and dissolved oxygen activities. The dependence of the rate on dissolved oxygen can also be described in terms of the Langmuir adsorption model. The empirical rate equation is given by: r= k′α(H~+)~α(Kα(O_2))/(1+Kα(O_2)) where, α = 0.099–0.265, k′ = 3.2 × 10~(-6)–1.7 × 10~(-5), K =2.7 × 10~4–3.9 × 10~4 mol/L in acid solution(pH 4.1), and α =-0.494-(-0.527), k′ = 2.0 × 10~4–2.5 × 10~(-11), and K = 4.1 × 10~3–6.5 × 10~3 mol/L in basic solution(pH 8.8) at 20°C. Based on the effect of temperature on the release rate of V, the activation energies of minerals at p H 8.8 were determined to be 148–235 k J/mol, suggesting that the dissolution of vanadium titano-magnetite is a surface-controlled process. The presence of Na~+, Ca~(2+), Mg~(2+), K~+, NO_3~-, Cl~-, SO_4~(2-)and CO_3~(2-)was found to accelerate the V release rates. This study improves the understanding of both the V pollution risk in some mine areas and the fate of V in the environment.     

The roles of organic degradation products andselenium in the pathogenesis ofKaschin-Beck disease

An investigation on the organic degradation products and selenium in the pathogenesis of Kaschin-Beck disease was carried out. The results demonstrated that the organic degradation products existed in food and drinking water were the pathogens of the KBD; their leading pathological process of cells would be "membrane injury" due to peroxide. As GSH-Px is a selenium contained enzyme, therefore insufficient selenium would be one of the most important conditions to cause KBD.     

Carbon and hydrogen isotope effects during sorption of organic contaminants on carbonaceous materials

Stable carbon and hydrogen isotopes can be an efficient means to validate biodegradation of organic contaminants in groundwater since it results in an isotopic fractionation. A prerequisite in applying this method in the field is the proof that other processes decreasing the contaminant concentration are conservative with respect to isotope effects. In this paper we show for carbon isotopes of halogenated hydrocarbon compounds [trichloroethene (TCE), cis-dichloroethene (c-DCE), vinylchloride (VC)] and carbon and hydrogen isotopes of BTEX compounds (benzene, toluene, p-xylene) that no significant fractionation occurs during equilibrium sorption onto activated carbon, lignite coke and lignite. In general, effects were in the range of the reproducibility limit of the analytical instrument (0.5 per thousand for delta13C, and 8 per thousand for delta2H). This observation was made for fractions sorbed of less than 5% to more than 95%. Also for rate-limited sorption of TCE onto activated carbon, no significant fractionation in carbon isotopes could be observed. These findings support the assumption that for these classes of compounds, sorption processes in aquifer systems are conservative with respect to isotope effects.