直接高压放电降解水中苯酚的效果

采用直接高压放电降解水中含有苯酚,自行设计加工了线筒式放电反应器,考察了氧气鼓入量、反应器压力、溶液初始pH对苯酚降解效果的影响.结果表明:在所设计的放电反应器中,放电电极直径为0.6 mm、地极直径29 mm或者38 mm,电压8～10 kV,电流4～14 mA,气体鼓入量为60 mL·min-1、溶液初始pH为9左右时,在180 min之内水中苯酚降解达到90%以上.同时发现溶液电导率具有相对应的变化趋势.     

渭河上游天然径流变化及其自然与人为因素影响贡献量

从20世纪60年代开始,渭河上游入陕西境内的水量不断减少,90年代天然径流量仅为60年代的60%。分析天然径流与降水的相关关系,对降水与非降水因素对径流减少的贡献进行了定量分析。结果表明,降水与非降水因素共同作用使得渭河上游径流量不断减少,且从20世纪70年代开始,非降水因素的贡献率逐渐增强,成为影响渭河上游天然径流量减少的主要因素。分析天然径流量与气温的相关关系,两者的相关系数在0.47以上,采用假设法,将气温从非降水因素中提取出来,进一步分析自然因素与人为因素的影响,结果表明,80年代以前,以自然因素影响为主,80年代以后,以人为因素影响为主,且人为因素的影响程度在逐渐增强,其原因在于人类活动改变下垫面导致径流减少。     

聚糖菌颗粒污泥的有机物吸收及胞内储存特性

采用特殊运行方式的厌氧-好氧SBR系统(厌氧后排水),在乙酸钠、葡萄糖及葡萄糖-乙酸钠混合基质条件下均培养出了稳定的聚糖菌颗粒污泥.通过对典型周期有机物、磷酸盐、胞内糖原及聚β-羟基丁酸(PHB)变化的测定分析,证明有机基质的种类对于聚糖菌能量利用模式、有机物吸收速率及胞内储存物质种类具有显著的影响.污泥初始胞内糖原水平是有机物吸收数量及吸收速率的关键影响因素,当糖原水平低于0.05g/gSS时,厌氧有机物去除率与糖原水平直接相关:而糖原水平高于0.05g/gSS时,厌氧有机物去除率趋于稳定.不同糖原水平污泥厌氧吸收有机物的速率具有明显差异,在厌氧初期有机物快速吸收阶段,有机物厌氧吸收速率随胞内糖原水平升高而增加.     

水解-好氧工艺处理生活污水

采用水解 好氧工艺 ,替代了WSZ F地埋式设备处理生活污水。既解决了设备腐蚀 ,又克服了停留时间不足的问题 ,同时提高了处理效果。     

富马酸废水降解菌的选育及降解效果

针对富马酸废水,从活性污泥中筛选出降解富马酸废水的降解菌,通过分离纯化,优选出四株适应能力强、生长旺盛的菌株,分别为FH-1、FH-2、TFH-1、TFH-2。经初步鉴定分别为隐球酵母属、节细菌属、微球菌属、假单胞菌属。试验测定了单株菌和混合菌对富马酸废水的降解效果,结果表明混合菌的降解效果最为明显,降解率为74.9%。     

植物提取液处理恶臭气体的研究进展

介绍了近二十年来国内外关于植物提取液治理恶臭气体的研究成果,内容包括植物提取液的应用研究、除臭机理研究及植物提取液提取方法的研究;指出对恶臭气体中的胺类和醚类除臭机理、对植物提取液提取工艺优化的研究是今后研究的重点。     

聚乙烯醇/氧化石墨插层纳米复合材料的结构和热分析

制备了聚乙烯醇/氧化石墨插层纳米复合材料,并用X-射线衍射仪和高分辨电镜对其结构进行了表征.X-射线衍射仪和高分辨电镜的试验结果表明,氧化石墨和聚乙烯醇插层氧化石墨的层间距分别为0.89 nm和1.4nm.该纳米复合材料的热分析和热失重图说明,氧化石墨的加入有利于提高聚乙烯醇/氧化石墨纳米复合材料的玻璃化转变温度和氧化温度,同时也降低了其热释放速率.     

邹平县大气降水酸度影响因素分析

应用灰色理论,以2002,2003,2004,2005,2006连续五年为时间序列点,取大气降水pH值为参考因素,取大气中SO2、NOx、TSP、降尘的浓度为比较因素进行关联分析。灰关联度矩阵表明：邹平县大气降水酸度的最大影响因素是SO2,其次降尘的影响也不容忽视。     

Reaction pathways of dimethyl phthalate degradation in TiO2-UV-O2 and TiO2-UV-Fe(VI) systems

The photocatalytic degradation of dimethyl phthalate (DMP) in aqueous TiO₂ suspension under UV illumination has been investigated using oxygen (O₂) and ferrate (Fe(VI)) as electron acceptors. The experiments demonstrated that Fe(VI) was a more effective electron acceptor than O₂ for scavenging the conduction band electrons from the surface of the catalyst. Some major intermediate products from DMP degradation were identified by HPLC and GC/MS analyses. The analytical results identified dimethyl 3-hydroxyphthalate and dimethyl 2-hydroxyphthalate as the two main intermediate products from the DMP degradation in the TiO₂–UV–O₂ system, while in contrast phthalic acid was found to be the main intermediate product in the TiO₂–UV–Fe(VI) system. These findings indicate that DMP degradation in the TiO₂–UV–O₂ and TiO₂–UV–Fe(VI) systems followed different reaction pathways. An electron spin resonance analysis confirmed that hydroxyl radicals existed in the TiO₂–UV–O₂ reaction system and an unknown radical species (most likely an iron–oxo species) is suspected to exist in the TiO₂–UV–Fe(VI) reaction system. Two pathway schemes of DMP degradation in the TiO₂–UV–O₂ and TiO₂–UV–Fe(VI) reaction systems are proposed. It is believed that the radicals formed in the TiO₂–UV–O₂ reaction system preferably attack the aromatic ring of the DMP, while in contrast the radicals formed in the TiO₂–UV–Fe(VI) reaction systems attack the alkyl chain of DMP.     

A directional passive air sampler for monitoring polycyclic aromatic hydrocarbons (PAHs) in air mass

A passive air sampler was developed for collecting polycyclic aromatic hydrocarbons (PAHs) in air mass from various directions. The airflow velocity within the sampler was assessed for its responses to ambient wind speed and direction. The sampler was examined for trapped particles, evaluated quantitatively for influence of airflow velocity and temperature on PAH uptake, examined for PAH uptake kinetics, calibrated against active sampling, and finally tested in the field. The airflow volume passing the sampler was linearly proportional to ambient wind speed and sensitive to wind direction. The uptake rate for an individual PAH was a function of airflow velocity, temperature and the octanol-air partitioning coefficient of the PAH. For all PAHs with more than two rings, the passive sampler operated in a linear uptake phase for three weeks. Different PAH concentrations were obtained in air masses from different directions in the field test.