苯酚在氯离子体系中的电化学氧化研究

研究了用Ti/RuO2-IrO2三元电极作阳极电解处理人工合成苯酚废水时Cl-初始浓度对处理效果的影响。结果表明,在一定的电解时间范围内苯酚在阳极上的电化学氧化符合一级动力学关系;废水中Cl-的初始浓度越大,苯酚完全被电化学氧化所需的时间也越短,其表观速度常数越大,电解中间体的生成和降解速率也越大。采用HPLC、GC/MS等方法鉴定出苯酚在Cl-体系下降解的中间产物主要有4-氯苯酚,1-氯苯酚,2,4-二氯苯酚,2,6二氯苯酚,2,4,6-三氯苯酚、各种短链脂肪酸及氯代醇等;最终产物是CO2、CHCl2和CHCl3。依此推导出了苯酚在Cl-体系下电化学降解的途径。     

表面包覆聚合氯化铝吸附材料的制备与性能表征

在颗粒状黏土素瓷载体上 ,经灼烧制备具有共价结合的铝胶薄膜 ,并以此为载体 ,在聚合氯化铝形成过程中与氯化铝悬浊液共熟化 ,在铝胶薄膜表面生成聚合氯化铝 ,经灼烧进一步固化而制得表面包覆聚合氯化铝吸附材料。该吸附材料作为絮凝剂可循环使用约 17次。用于处理造纸污水 ,COD、BOD、悬浮物、硫化物、色度等指标可分别降低约 93%、77%、96 %、94 %和 80 %。     

光致抗蚀剂乳化废水中有机物GC/MS分析

采用色谱－质谱（GC／MS）联用分析仪分析了电子工业光致抗蚀剂乳化废水中的有机化合物成份，测定了该废水中各种有机污染物的含量。分析结果表明：电子工业中光致抗蚀剂乳化废水的主要成份为有机酸类、醛类、酯类、胺类、芳香酮类、酸酐类、砜类、聚醚类、醇类、芳香烃类、杂环类十一大类有机化合物，其中聚丙二醇类、脂肪酸类、丁烯酸类、苯甲酸类、苯甲酸胺、烷基酚聚氧乙烯醚类和噻吩类约占总有机碳含量的95％以上。有机污染物的分析测定对此类废水的处理工艺的研究具有重要的指导作用。     

氯盐阻化剂对煤自燃极限参数影响的试验研究

阻化技术是防治煤自燃的常用技术之一,研究阻化剂对煤自燃极限参数的影响是确定阻化效果的关键.采用程序升温试验,分析气煤和长焰煤的原煤样和经MgCl2、KCl、CaCl2、NaCl 4种阻化剂处理后的煤样耗氧速率和放热强度,并计算自燃极限参数和阻化率.结果表明:氯盐阻化剂可降低煤自燃低温阶段的煤耗氧速率和放热强度;4种阻化剂中对气煤煤样的平均阻化率最高是MgCl2 (63.6％),对长焰煤则是CaCl2 (45.9％),平均阻化率与自燃极限参数变化率呈正相关;气煤经MgCl2处理后自燃极限参数变化率最大,长焰煤经CaCl2阻化处理后的自燃极限参数变化率最大,对于气煤4种阻化剂阻化能力由大到小为MgCl2 KCl、CaCl2、NaCl,对长焰煤则为CaCl2、MgCl2、KCl、NaCl;氯盐阻化剂中MgCl2对气煤自燃极限参数影响最大,阻化效果好,而对长焰煤则为CaCl2.     

流动注射化学发光法测定环境水样中痕量Pb2+的方法研究

在碱性介质中,鲁米诺和过氧化氢能产生稳定的发光信号,Pb2+-EDTA络合物对鲁米诺-过氧化氢体系的化学发光产生微弱的抑制作用,而表面活性剂吐温-80的加入可以改变发光体系的微环境性质,从而对化学发光体系起到增敏作用。据此建立测定环境水样中痕量Pb2+的流动注射化学发光分析方法。此方法用于测定环境水样中Pb2+的含量,具有检出限高,操作简便,分析速度快等优点。     

雨水的混凝处理实验研究

通过烧杯混凝实验,考察了聚合氯化铝(PAC)对模拟雨水及实际的天然降雨、屋面径流雨水和道路径流雨水中各污染物的去除效果,确定了最优的药剂投加量;同时对实际雨水进行三维荧光光谱分析.实验结果表明,雨水中主要荧光物质为类蛋白质类.对于模拟雨水,PAC对TP去除效果较好,但对于COD的去除效果并不理想.对于实际雨水,PAC对于各污染物去除效果均较好,天然降雨、屋面径流雨水和道路径流雨水的PAC最佳投加量分别为:3～5 mg/L、10～20 mg/L和25～25 mg/L.这样不仅能节省药剂、降低工程费用,而且还能在很大程度上提高水的混凝沉淀处理效果.     

Numerical study of the effect of obstacles on the spontaneous ignition of high-pressure hydrogen

A numerical simulation of the spontaneous ignition of high-pressure hydrogen in a duct with two obstacles on the walls is conducted to explore the spontaneous ignition mechanisms. Two-dimensional rectangular ducts are adopted, and the Navier–Stokes equations with a detailed chemical kinetic mechanism are solved by using direct numerical simulations. In this study, we focus on the effects of the initial pressure of hydrogen and the position of the obstacles on the ignition mechanisms. Our results demonstrate that the presence of obstacles significantly changes the spontaneous ignition mechanisms producing three distinct ignition mechanisms. In addition, the position of the obstacles drastically changes the interaction of shock waves with the contact surface, and spontaneous ignition may take place at a relatively low pressure in some obstacle positions, which is attributed to the propagation direction and interaction timing of two reflected shock waves.     

Medium-scale experiments on vented hydrogen deflagration

A series of medium-scale experiments on vented hydrogen deflagration was carried out at the KIT test side in a chamber of 1 × 1 × 1 m³ size with different vent areas. The experimental program was divided in three series: (1) uniform hydrogen–air mixtures; (2) stratified hydrogen–air mixtures within the enclosure; (3) a layer deflagration of uniform mixture. Different uniform hydrogen–air mixtures from 7 to 18% hydrogen were tested with variable vent areas 0.01–1.0 m². One test was done for rich mixture with 50% H₂. To vary a gradient of concentration, all the experiments with a stratified hydrogen–air mixtures had about 4%H₂ at the bottom and 10 to 25% H₂ at the top of the enclosure. Measurement system consisted of a set of pressure sensors and thermocouples inside and outside the enclosure. Four cameras combined with a schlieren system (BOS) for visual observation of combustion process through transparent sidewalls were used. Four experiments were selected as benchmark experiments to compare them with four times larger scale FM Global tests (Bauwens et al., 2011) and to provide experimental data for further CFD modelling. The nature of external explosion leading to the multiple pressure peak structure was investigated in details. Current work addresses knowledge gaps regarding indoor hydrogen accumulations and vented deflagrations. The experiments carried out within this work attend to contribute the data for improved criteria for hydrogen–air mixture and enclosure parameters to avoid unacceptable explosion overpressure. Based on theoretical analysis and current experimental data a further vent sizing technology for hydrogen deflagrations in confined spaces should be developed, taking into account the peculiarities of hydrogen–air mixture deflagrations in presence of obstacles, concentration gradients of hydrogen–air mixtures, dimensions of a layer of flammable cloud, vent inertia, etc.     

Gas leakage consequence modeling for buried gas pipelines

One of conservation transfer methods for such widely-used gases as natural gas and hydrogen is buried pipelines. Safety of these pipelines is of great importance due to potential risks posed by inefficiencies of the pipelines. Therefore, an accurate understanding of release and movement characteristics of the leaked gas, i.e. distribution and speed within soil, the release to the ground surface, the movement of hydrogen gas through the ground, gas underground diffusion, gas dispersion in atmosphere, and following consequences, are very important in order to determine underground dispersion risks. In the present study, consequences of gas leakage within soil were evaluated in two sub-models, i.e. near-field and far-field, and a comprehensive model was proposed in order to ensure safety of buried gas supply pipelines. Near-field model which is related to soil and ground and its output is the gas released at different points and times from ground surface and it was adopted as input of far-field sub-model which is dispersion model in atmosphere or an open space under the surface. Validation of near-field sub-model was performed by the experimental data obtained by Okamoto et al. (2014) on full-scale hydrogen leakage and then, possible scenarios for far-field sub-model were determined.