基于突变理论的加油站火灾爆炸事故分析与安全评价

为探索加油站火灾爆炸事故致因机理,从而建立安全评价模型,在分析加油站火灾爆炸事故因素的基础上,从人的因素和物的因素视角构建加油站安全状态突变模型,并针对常用加油站安全评价中权重获取受主观影响的问题,提出基于突变理论的加油站火灾爆炸事故安全评价方法,该方法通过对评价目标进行多层次分解,利用归一化公式计算出总突变隶属函数值,实现了加油站安全等级评价与动态评判。实例验证表明:突变模型合理地诠释了加油站火灾爆炸事故形成的规律,安全评价结果是合理、可行的,为加油站安全综合评价提供了新思路。     

How China’s current energy pricing mechanisms will impact its marginal carbon abatement costs?

Economic and social costs and benefits are critical factors affecting greenhouse gas abatement activities. Recognizing that energy prices are one of the most important factors influencing abatement costs, this study improved the basic China Energy and Environmental Policy Analysis (CEEPA) model by introducing a current energy pricing mechanism for China. The improved model was applied to generate marginal abatement cost (MAC) curves for China including the current energy pricing mechanism and to analyze MACs for the whole country and main abatement sectors in China under different energy pricing mechanisms. The results show that China MACs are sensitive to pricing mechanisms for electricity and refined oil. Ignoring the current regulation of these prices will lead to MAC underestimation, and price liberalization of these two energy sources could lead to a decrease in China MACs. Under a 50 % emission reduction target, if the electricity price regulation is ignored, the China MAC is underestimated by almost 16 %. Energy pricing reforms will lead to variations in sectoral abatement costs and overall abatement potential, and these impacts are projected to be large in the electricity sector. Under a 50 % reduction target, if the electricity price regulation is liberalized, MAC for the electricity sector nearly will decrease 50 %.     

Microbial bioavailability of dissolved organic nitrogen (DON) in the sediments of Lake Shankou, Northeastern China

Dissolved organic nitrogen(DON)extracted from Lake Shankou sediments using KCl was isolated into hydrophobic and hydrophilic fractions.The bioavailabilities of the hydrophobic and hydrophilic fractions to three types of bacterial communities collected from sediments,activated sludge and compost products were examined.The DON recoveries obtained by DAX-8 and cation exchange resins treatment were 96.17% ± 1.58% and 98.14% ±0% for the samples obtained from N4 and N14 stations,respectively.After 25 days of incubation at 25°C,most DON(59% to 96%)was degraded.Hydrophilic DON exhibited a higher reduction rate than hydrophobic DON during the growth phase.Untreated wastewater from Changshuihe town was the main degradable DON source to station N4,and 93% of hydrophilic DON and 80% of hydrophobic DON were degraded.Station N14 received a large amount of refractory DON from forest soils and exhibited DON degradation rates of 82% and 71% for the hydrophilic and hydrophobic fractions,respectively.Amino acid contents and fluorescence intensities were also analyzed.Approximately 27% to 74% of amino acids were taken up by day 5,and their concentration gradually increased in the following days due to the decomposition of dissolved proteins.Parallel factor analysis resulted in identification of tryptophan-like proteins,tyrosine-like proteins and FA-like substances.During the growth phase,40%–51% of the tryptophan-like proteins were taken up by bacteria,and the accumulation of tyrosine-like proteins was attributed to the release of biotic substances.The concentration of the FA-like substances decreased due to microbial decomposition.     

Numerical evaluation of the effectiveness of NO2 and N2O5 generation during the NO ozonation process

Wet scrubbing combined with ozone oxidation has become a promising technology for simultaneous removal of SO₂ and NO_x in exhaust gas. In this paper, a new 20-species, 76-step detailed kinetic mechanism was proposed between O₃ and NO_x. The concentration of N₂O₅ was measured using an in-situ IR spectrometer. The numerical evaluation results kept good pace with both the public experiment results and our experiment results. Key reaction parameters for the generation of NO₂ and N₂O₅ during the NO ozonation process were investigated by a numerical simulation method. The effect of temperature on producing NO₂ was found to be negligible. To produce NO₂, the optimal residence time was 1.25 sec and the molar ratio of O₃/NO about 1. For the generation of N₂O₅, the residence time should be about 8 sec while the temperature of the exhaust gas should be strictly controlled and the molar ratio of O₃/NO about 1.75. This study provided detailed investigations on the reaction parameters of ozonation of NO_x by a numerical simulation method, and the results obtained should be helpful for the design and optimization of ozone oxidation combined with the wet flue gas desulfurization methods (WFGD) method for the removal of NO_x.     

磷酸铵镁沉淀法去除垃圾渗滤液中氨氮的实验研究

本试验采用磷酸铵镁沉淀法（MAP）处理垃圾渗滤液中的高浓度氨氮,采用MgCl2.6H2O和Na2HPO4.12H2O为沉淀剂,研究了该方法脱氮的主要影响因素并得出了最佳处理条件,即在室温条件时,pH值为10～10.5、反应摩尔比n（Mg2＋）：n（NH4＋）：n（PO43-）为1.2：1.0：0.9时,对于本试验中的垃圾渗滤液来说,为最佳反应条件,对氨氮的去除率可达到97%以上,达到国家杂用水水质标准中对氨氮的要求。     

UniFed SBR工艺在食品生产废水处理中的应用

UniFed SBR工艺已在某食品生产废水处理工程中成功运行3年以上,且运行效果稳定,出水达标排放。本文简单介绍了该工艺的流程、主要特点、设计参数以及其中空气堰排水器的主要原理和优点,以为类似废水处理提供借鉴。     

二甲基甲酰胺中毒研究进展

介绍了二甲基甲酰胺(DMF)在人体的代谢、毒性作用和临床表现,以及DMF职业接触标志物的研究进展。     

原子荧光不同方法测定水中砷的比较

中华人民共和国水利行业标准(SL 327.1-2005)和中华人民共和国城镇建设行业标准(CJ/T 51-2004)分别对原子荧光法测定水中砷作了一定的阐述,但两者对硫脲-抗坏血酸溶液的加入量有不同的规定,本文就这两种方法分别作了相应的实验,对两者的检出限、精密度以及加标回收率进行比较分析,得出两者在砷的测定方面没有显著差异。     

冷冻分离法处理难降解有机废水的研究

以无机水样、溴氨酸溶液、U llm ann缩合反应生产废水及垃圾渗滤液为研究对象,考察了在人工条件下冷冻法处理无机离子和有机污染物的效果和差别。结果表明:在人工冷冻条件下,无机离子、溴氨酸的去除率均可达到80%~90%以上,并受冷冻时间、初始浓度、污染物自身结构特性等因素影响;而对于无机离子和有机污染物混合的实际有机废水,其去除率相对较低,为70%~80%左右,需要与其他工艺组合,以提高废水的处理效率。     

污泥活性炭处理染料废水的研究

采用污泥活性炭处理酸性品红模拟染料废水,研究了pH值、污泥活性炭投加量、温度、吸附时间等因素对染料废水的脱色率和COD去除率的影响。探讨了污泥活性炭处理染料废水的机理。实验结果表明:污泥活性炭表现出良好的吸附性能,随着酸性品红染料废水浓度的增加,脱色率先增大后减小,COD去除率的变化曲线与脱色率的曲线呈现相似的走势,但在脱色过程中,只有部分染料分子被吸附到污泥活性炭的结构中,另一部分脱色应归因于水溶液中的氢离子吸引染料分子中的碱性助色基团;随着污泥活性炭投加量的增加,脱色率逐渐增大,COD去除率一直减小;由于染料分子中的显色基团和助色基团与废水溶液中氢离子和氢氧根离子之间的相互作用,导致pH对处理效果的影响比较明显,脱色率和COD去除率均在pH为弱酸性范围内效果比较好;随水浴时间的增加,脱色率逐渐增加,COD去除率很低并一直减小;温度的升高使脱色率先增大后减小,COD去除率整体逐渐减小。通过正交试验得到最佳工艺参数为:pH值取5,水浴时间取6.5 h,水浴温度取20℃,染料废水浓度取2.5 mg/L,活性炭投加量取2.5 g,其脱色率为47.73%,COD去除率为62.62%。