水体溶解有机质富集分离方法的研究进展

溶解有机质,作为全球碳循环的主要组成部分,在水生生态系统的各种物理、化学和生物过程中扮演着非常重要的角色。富集分离溶解有机质是研究其化学特征和环境地球行为的必要前提。在总结XAD树脂分离技术在溶解有机质富集分离的基础上,本文对其它三种常用的分离方法—二乙氨基乙基纤维素(DEAE)吸附分离法、超滤(UF)分离法以及反渗透(RO)分离法进行了综述。介绍了各分离方法的分离原理、分离流程、存在的优缺点及应用范围。最后对超滤或反渗透与XAD树脂相结合的联用技术在溶解有机质环境地球化学研究中的应用前景进行了展望。     

大气扩散浓度估算在锅炉房烟囱高度计算中的应用

锅炉房的烟囱已从单纯的排气装置发展成为控制污染、保护环境的设备。因此烟囱高度的正确估算对于环境影响评价工作、建设单位都至关重要。结合唐山某城区集中供热锅炉房环境影响评价案例,利用大气扩散浓度公式估算锅炉房烟囱高度。在计算过程中,考虑了烟气流速及当地常年风向、风速、稳定度等污染气象特征,由正态分布模式导出的简化公式导出最大着地浓度与烟囱有效高度的平方成反比,从而计算出烟囱高度。另外还总结烟囱设计中应注意的一些问题,为建有锅炉房的建设项目环境影响评价工作提供参考。     

DO浓度对生活污水硝化过程中N2Ｏ产生量的影响

为确定污水脱氮过程中最优的DO浓度和曝气方式,以提高污水处理效率,降低N₂Ｏ产生量,采用实际生活污水应用小试SBR反应器,重点考察了不同DO浓度条件下,硝化效率和硝化过程中N₂Ｏ的产生量.结果表明,当DO浓度恒定为0.4 mg·L^-1时,虽然硝化过程所消耗的能量最低,但其氨氮氧化的速率较低.提高DO浓度,氨氮氧化速率可随之升高.低氨氮生活污水硝化过程中仍有N₂Ｏ产生.DO浓度为0.4 mg·L^-1 和0.9 mg·L^-1时,污水N₂Ｏ产生量(以N计)分别为1.5 mg·L^-1和1.6 mg·L^-1;而DO浓度为1.5 mg·L^-1和2.0 mg·L^-1时,N₂Ｏ产生量则分别降低至0.5 mg·L^-1和0.4 mg·L^-1.当DO浓度高于1.5 mg·L^-1后,继续提高DO浓度,氨氮氧化速率升高的速率变缓,同时N₂Ｏ产生量大幅降低.因此,从提高污水脱氮效率节能降耗和控制N₂Ｏ产生量2个角度考虑,生活污水脱氮过程中控制DO浓度在1.5 mg·L^-1较为适宜.     

毒气泄漏威胁下建筑气密性对就地避难效果影响研究*

针对我国毒气泄漏生产安全事故中就地避难策略的选择缺乏依据的问题，基于毒气扩散理论、建筑气密性分级模型及毒物浓度伤害准则，评析位于毒气泄漏源不同距离处不同气密性建筑作为“就地避难场所”的可靠性与有效性。结果表明:事故中，室外毒气浓度短时间内达到峰值后迅速回落，而室内毒气浓度达到峰值后回落缓慢；室内毒气浓度达到峰值所需时间受气密性影响小，但其降速随气密性等级的增大而明显放缓。最后，研究提出距泄漏源不同距离处就地避难建筑应达到的气密性水平。     

Dust ignition of pure and encapsulated paraffin phase change materials

In this study, the dependence of the flammable concentration on particle size is investigated for Phase Change Material (PCM) and Encapsulated Phase Change Material (EPCM) particles using a novel continuous particle dispersion apparatus into which a propane flame is introduced creating a test akin to the flash-point test for liquids. The results show that the threshold concentration is a strong function of particle size. For tested particles with size ranging from 290 μm to 750 μm, the threshold concentration is above the predictions based on an instantaneous heat transfer limit, and is approximately linear with the particle size, following a heat transfer limited ignition model. For sizes above ≈1 mm, the particles behave like the bulk material, and ignition is not observed for the concentrations tested. The results obtained here are important for the safe construction, handling, and operation of systems using PCM and other particles.     

Effects of premixed methane concentration on distribution of flame region and hazard effects in a tube and a tunnel gas explosion

Study of flame distribution laws and the hazard effects in a tunnel gas explosion accident is of great importance for safety issue. However, it has not yet been fully explored. The object of present work is mainly to study the effects of premixed gas concentration on the distribution law of the flame region and the hazard effects involving methane-air explosion in a tube and a tunnel based on experimental and numerical results. The experiments were conducted in a tube with one end closed and the other open. The tube was partially filled with premixed methane-air mixture with six different premixed methane concentrations. Major simulation works were performed in a full-scale tunnel with a length of 1000 m. The first 56 m of the tunnel were occupied by methane–air mixture. Results show that the flame region is always longer than the original gas region in any case. Concentration has significant effects on the flame region distribution and the explosion behaviors. In the tube, peak overpressures and maximum rates of overpressure rise (dp/dt)_max for mixtures with lower and higher concentrations are great lower than that for mixtures close to stoichiometric concentration. Due to the gas diffusion effect, not the stoichiometric mixture but the mixture with a slightly higher concentration of 11% gets the highest peak overpressure and the shock wave speed along the tube. In the full-scale tunnel, for fuel lean and stoichiometric mixture, the maximum peak combustion rates is achieved before arriving at the boundary of the original methane accumulation region, while for fuel rich mixture, the maximum value appears beyond the region. It is also found that the flame region for the case of stoichiometric mixture is the shortest as 72 m since the higher explosion intensity shortens the gas diffusion time. The case for concentration of 13% can reach up to a longest value of 128 m for longer diffusion time and the abundant fuel. The “serious injury and death” zone caused by shock wave may reach up to 3–8 times of the length of the original methane occupied region, which is the widest damage region.     

Occupational exposure in the fluorescent lamp recycling sector in France

The fluorescent lamp recycling sector is growing considerably in Europe due to increasingly strict regulations aimed at inciting the consumption of low energy light bulbs and their end-of-life management. Chemical risks were assessed in fluorescent lamp recycling facilities by field measurement surveys in France, highlighting that occupational exposure and pollutant levels in the working environment were correlated with the main recycling steps and processes.The mean levels of worker exposure are 4.4 mg/m³, 15.4 μg/m³, 14.0 μg/m³, 247.6 μg/m³, respectively, for total inhalable dust, mercury, lead and yttrium. The mean levels of airborne pollutants are 3.1 mg/m³, 9.0 μg/m³, 9.0 μg/m³, 219.2 μg/m³, respectively, for total inhalable dust, mercury, lead and yttrium. The ranges are very wide. Surface samples from employees’ skin and granulometric analysis were also carried out. The overview shows that all the stages and processes involved in lamp recycling are concerned by the risk of hazardous substances penetrating into the bodies of employees, although exposure of the latter varies depending on the processes and tasks they perform. The conclusion of this study strongly recommends the development of a new generation of processes in parallel with more information sharing and regulatory measures.     

内盘管接管泄漏成因及改进

对反应釜内盘管接管处发生泄漏的原因进行了探讨，通过入釜检查和有限元分析，确认了该处由于局部应力集中导致角焊缝出现微小开裂，并结合该釜结构特点和工况对其改进方法进行了讨论。     

工业高浓度苯胺废水处理技术研究

染料厂、农药厂、制药厂等工业都会产生含有高浓度苯胺的废水，处理苯胺废水的方法较多，本文通过实验的方式着重研究了膜萃取法处理高浓度苯胺废水，并通过分析实验结果得出了相应结论。     

Key airborne concentrations of chemicals for emergency response planning in HAZMAT road transportation- margin of safety or survival

The release of chemicals due to road transportation accidents could have adverse consequences such as fatality, physical and financial loss and environmental damage. The purpose of this study was to determine the suitable margin of safety/survival of individuals in HAZMAT road transportation accidents for use in Emergency Response Planning (ERP). In this study, at first, the safety margin and survival margin were defined and proposed. Then, as a case study, the chemical tanker trucks in Iran's road transport fleet were investigated and the full bore rupture of the tanker trucks was considered as the selective scenario. Eventually, safety margin and survival margin were determined using ALOHA and PHAST software and the Chemical Exposure Index (CEI). The results showed that using the CEI, among the selected chemicals, ammonia, chlorine and 1,3-butadiene had the highest chemical release potential with the exposure indices of 597, 548 and 284, respectively, and need further investigation. The possible safety margin obtained in this study was distances over 5100 m (using ALOHA software for ammonia) and 10,983 m (using PHAST software for chlorine). On the other hand, the survival margin was distances over 980 m away from the accident area (using ALOHA software for ammonia) and 620 m away from the accident area (using the PHAST software for chlorine). The results of this study indicate that determining the safety and survival margins surrounding the tanker trucks and containers of chemicals is a critical issue for the emergency response planning and determining the standards of road's safety and survival margins. On the other hand, due to the obtainment of different results by various methods and software, in road accidents, the highest hazard distance is suggested to be considered to determine the safety margin (distances longer than 10,983 m) and survival margin (distances longer than 980 m) for ERP, regardless of the type of used material and software.