臭氧与过氧化钙协同降解甲基红废水

对单独臭氧（O₃）、臭氧与过氧化钙（O₃/CaO₂）联用技术降解甲基红染料废水进行了研究,考察了O₃流量、温度、废水初始pH值、CaO₂投加量、处理时间以及不同水基质等因素对甲基红降解效果的影响.结果表明,在O₃流量为48L/h,温度为26℃,初始pH值为6.2的纯水中降解10min,单独O₃处理对甲基红的降解率为86.1%.在此条件下投加CaO₂,投加量为6.9mmol/L时,O₃/CaO₂联用技术对甲基红废水的脱色率可达到94%.水基质中草酸的存在并不会对O₃/CaO₂联用体系的降解作用造成抑制.O₃/CaO₂联用体系在多种复杂水基质中都能达到较好的脱色效果.通过对比试验发现,O₃/CaO₂联用对甲基红的降解起协同作用,CaO₂不仅可以产生H₂O₂促进染料被O₃降解,而且CaO₂的吸附作用也有利于染料和污染物质的氧化去除.该联用工艺可高效地去除印染废水的色度,达到出水水质处理标准.     

以淀粉为模板多孔纳米氧化铈的制备及其催化性能研究

为获得多孔纳米CeO₂（氧化铈）,以淀粉为生物模板,以Ce（NO₃）₃·6H₂O为铈源,在温和条件下制备出海绵状的多孔纳米CeO₂,同时考察了焙烧温度、碱液、铈源投加量对样品形貌的影响.利用XRD（X射线衍射光谱）、SEM（扫描电镜）、N₂吸附-脱附等表征手段对合成的多孔纳米CeO₂进行物相组成、微观形貌及孔径大小分布的分析.通过湿式催化过氧化试验,探究其对腈纶废水中有机物COD_Cr的催化降解性能.结果表明:①所制备的多孔纳米CeO₂具有多孔结构,孔径分布范围为2~4 nm,孔容为0.225 cm3/g,BET比表面积为256.426 m2/g;②多孔纳米CeO₂的最佳制备条件为1 g淀粉溶解于20 mL水中,加入0.02 mol Ce（NO₃）₃·6H₂O,以5%的氨水调节前驱体混合液pH,以1℃/min升至400℃,焙烧4 h,得到海绵状的多孔纳米CeO₂.③以不同形貌的CeO₂作为湿式催化反应中的催化剂,催化降解腈纶废水中有机物,其中以制备的多孔纳米CeO₂催化性能最佳,COD_Cr去除率可达82.5%.研究显示,焙烧温度、碱液、铈源投加量均可影响样品的形貌,在湿式催化过氧化处理腈纶废水试验中,多孔纳米CeO₂能显著提高废水COD_Cr的去除率.      

CaO2不同投加方式对黑臭河道底泥内源磷释放抑制作用

以S市某黑臭河道底泥和上覆水为研究材料,研究了CaO_2在3种不同投加方式下对内源磷释放的抑制效果.结果表明CaO_2在3种投加方式下,均导致上覆水中pH和DO有所增加.注射条件下,上覆水DO浓度明显低于覆盖,说明注射确实延缓了CaO_2的氧化速度,有利于创造底泥微氧化环境.CaO_2覆盖和注射条件下,上覆水中TP和DIP浓度以及变化趋势基本一致,均明显低于混匀条件.但是,覆盖条件下,间隙水中DIP浓度最高,达到注射条件下的120.33~142.18倍.相反,注射条件下,间隙水中DIP浓度最低,并且上覆水中DIP浓度也较低,说明注射条件下CaO_2对内源磷的释放确有抑制作用,这与其创造的微氧化环境密切相关.底泥中不同形态磷数量分布也证实了这一点.投加CaO_2加快了有机磷的矿化速度,铁铝结合态磷和钙结合态磷也明显增加,使得内源磷持留能力增强.     

基于过氧化物的消毒技术研究进展

对环境友好消毒技术需求的增长,推动了过氧化物消毒技术的快速发展,并已被广泛应用于反化学和生物恐怖袭击、化生灾害处置、环境污染治理等领域.在综述了过氧化物消毒剂α亲核取代/氧化消毒反应机制研究进展的基础上,介绍了以过氧化物为活性组分的水基消毒溶液、消毒泡沫、消毒乳液、消毒凝胶、消毒气雾、自消毒材料、纳米材料催化消毒技术等典型消毒体系.针对现有过氧化物消毒技术消毒效率偏低、对个别毒剂消毒效果不理想的缺点,建议在过氧化物消毒技术研究中,加强消毒反应机制、多相体系界面相互作用研究,开发新型催化剂、多功能表面活性剂、自消毒材料和消毒剂缓蚀技术,以实现真正的绿色消毒.     

Explosion hazards related to hydrogen releases in nuclear facilities

Hydrogen explosion risk needs to be carefully assessed and evaluated in nuclear facilities because of the potential catastrophic consequences: breakdown of safety equipments, failure of containment, dissemination of radioactive materials in the environment.When studying an indoor release, one possible simplification is to assume a perfect gas mixing inside the room. This assumption is effectively often used to evaluate toxic risks in the environment outside a building (Mastellone, Ponte, & Arena, 2003). However, perfect gas mixing assumption is only a rough approximation, as indoor concentrations can largely differ from mean values, due to buoyancy, recirculation zones or obstacles for example.In order to better evaluate the risk of explosion in case of an accidental release of hydrogen, IRSN conducted a numerical study using FLACS CFD software. Several parameters have been studied to identify dangerous situations and draw a representative picture of the risk: room size, position and direction of hydrogen leak, ventilation characteristics. Hydrogen release flow rates used for numerical simulations have been chosen as the highest leak rate which, by applying the assumption of perfect mixing, produces an average concentration in the room equal to hydrogen lower flammability limit (LFL).Simulation results indicate that in some particular configurations, especially for impinging hydrogen jets, hydrogen concentrations can locally be above LFL and then create explosive atmospheres with significant volumes.     

Determination of the minimum ignition energy on the basis of a statistical approach

Based on existing MIE test results and new measurements, a statistical analysis for the MIE of hydrogen, ethene and propane is made by means of the logistic regression. The conditions necessary to carry out such an approach are discussed. It is shown that MIE values which are connected with a certain ignition probability could be determined adequately and lead to a more sophisticated result, also with regard to measurement uncertainties. This, in turn, leads to a better comparability and a higher informative content. At the same time, the MIEs of hydrogen, ethene and propane are reviewed. In doing so, a useful contribution to the discussion concerning the MIE of propane is made.     

Flame acceleration in unconfined hydrogen/air deflagrations using infrared photography

Flame behavior and blast waves generated during unconfined hydrogen deflagrations were experimentally studied using infrared photography. Infrared photography enables expanding spherical flame behaviors to be measured and flame acceleration exponents to be evaluated. In the present experiments, hydrogen/air mixtures of various concentrations were filled in a plastic tent of thin vinyl sheet of 1 m³ and ignited by an electric spark. The onset of accelerative dynamics on the flame propagation was analyzed by the time histories of the flame radius and the stretched flame speed. The results demonstrated that the self-acceleration of the flame, which was caused by diffusional-thermal and hydrodynamic instabilities of the blast wave, was influenced by hydrogen deflagrations in unconfined areas. In particular, it was demonstrated that the overpressure rapidly increased with time. The burning velocity acceleration was greatly enhanced with spontaneous-turbulization.     

Photocatalytic Production of Methane and Hydrogen Through Reduction of Carbon Dioxide with Water Using Titania Pellets

This paper presents an experimental study on employing a pellet form of catalyst in photo-reduction of carbon dioxide with water. Water was first absorbed into titania pellets. Highly purified carbon dioxide gas was then discharged into a reactor containing the wet pellets, which were then illuminated continuously for 65 hours using UVC lamps. Analysing the products accumulated in the reactor confirmed that methane and hydrogen were produced through photo-reduction of carbon dioxide with water. No other hydrocarbons were detected. Increasing the temperature in the reactor has showed little change on the amount of methane produced.     

高效吸收氧化法处理炼油工业恶臭气体研究

以碳酸钠溶液为吸收液,对苯二酚为催化荆,研究了对炼油企业硫化氢恶臭气体的吸收氧化效果,考察了吸收氧化的影响因素、再生方法及再生效果。结果表明：高效氧化吸收法处理硫化氢恶臭气体效果很好,吸收液可循环使用。     

Hydrogen and transportation: alternative scenarios

If hydrogen (H₂) is to significantly reduce greenhouse gas emissions and oil use, it needs to displace conventional transport fuels and be produced in ways that do not generate significant greenhouse gas emissions. This paper analyses alternative ways H₂ can be produced, transported and used to achieve these goals. Several H₂ scenarios are developed and compared to each other. In addition, other technology options to achieve these goals are analyzed. A full fuel cycle analysis is used to compare the energy use and carbon (C) emissions of different fuel and vehicle strategies. Fuel and vehicle costs are presented as well as cost-effectiveness estimates. Lowest hydrogen fuel costs are achieved using fossil fuels with carbon capture and storage. The fuel supply cost for a H₂ fuel cell car would be close to those for an advanced gasoline car, once a large-scale supply system has been established. Biomass, wind, nuclear and solar sources are estimated to be considerably more expensive. However fuel cells cost much more than combustion engines. When vehicle costs are considered, climate policy incentives are probably insufficient to achieve a switch to H₂. The carbon dioxide (CO₂) mitigation cost would amount to several hundred US$ per ton of CO₂. Energy security goals and the eventual need to stabilize greenhouse gas concentrations could be sufficient. Nonetheless, substantial development of related technologies, such as C capture and storage will be needed. Significant H₂ use will also require substantial market intervention during a transition period when there are too few vehicles to motivate widely available H₂ refueling.