气相色谱法快速测定蔬菜中灭杀毙

用蒸馏水一次提取新鲜蔬菜样品，以SE－30和QF－1为固定液，Chromosorb W AW DMCS为固定相，2m填充柱分离，氢火焰检测器检测，进样10uL测定灭杀毙含量，以保留时间定性，外标法定量，分析时间小于150s，方法回收率95．4％，相对标准差3．6％，可用作上市蔬菜灭杀毙农药残留量的快速测定。     

气相色谱法测定水质苯系物

指出了气相色谱法测定水质苯系物存在的不足，提出用3％有机皂土－34＋2．5％邻苯二甲酸二壬酯混合涂渍的101坦体（60目－80目）不锈钢色谱柱分离苯系物，可在19min内分离水样中7种苯系物，对二甲苯与间二甲苯等难分离物质对可完全分离，改进后的样品前处理顶空装置操作简单、安全、可连续自动振荡，并且可以同时处理多个样品。     

正己烷萃取-气相色谱法快速测定水中三氯乙烯

采用正己烷萃取法对水中三氯乙烯进行富集,用毛细管柱气相色谱法进行测定;通过正交试验,对气相色谱测定的主要影响因素和条件进行优化选择,并进行定量评价,总结其影响规律,最终确定最佳测定条件。同时对该方法检出限、准确度和精密度进行检验,完成方法验证。结果表明,该方法简单、快速、准确可靠,灵敏度高,在水环境质量监测中具有实用性。     

天津静稳指数建立及在环境气象预报和评估中的应用

基于2014—2015年NCEP再分析资料及天津地区PM_2.5质量浓度数据,构建天津地区静稳指数以期反映大气综合扩散能力,为天津霾、空气质量预报和大气环境气象条件评估提供支撑.研究结果表明：本文构建的静稳指数可作为评估天津地区细颗粒物大气扩散能力的重要指标参数,其建模产品与天津地区PM_2.5质量浓度相关系数为0.62,在评测期间（2016年6月1日—2018年5月31日）,基于EC模式的静稳指数24 h预报产品与天津地区PM_2.5质量浓度相关系数为0.67,1~7 d预报产品与PM_2.5质量浓度相关系数超过0.53,8~10 d预报产品随着时效增加指示能力有所下降,相关系数为0.4左右,但通过显著性检验.对比同期基于GFS资料和WRF/Chem构建的天津中长期环境气象数值模式,其相关系数接近,趋势预报效果相当.同时,由于静稳指数综合了水平风速、混合层高度、相对湿度等多项指标,可以综合反映一个地区大气扩散能力,在大气环境气象条件评估中可发挥积极作用,以同排放源不同气象条件的数值模拟为基准定义细颗粒物大气扩散条件,2013—2018年逐月大气扩散条件同比上年改善的占总样本41%,同比转差的占总样本59%,利用静稳指数对大气扩散条件月同比变化趋势进行判断,识别准确率可达80%.     

隧道内氨气泄漏扩散分布特征数值模拟

为分析运输过程中液氨罐车在隧道内泄漏的危险性,利用Fire Dynamics Simulator(FDS)软件模拟氨气在隧道内的扩散过程,发展了隧道内氨气泄漏扩散体积分数分布特征经验公式。采用大涡模拟处理湍流流动,以便兼顾计算精度和计算效率。考虑储罐车发生泄漏后停止不动,液氨在泄漏瞬间转变为气体,模拟在连续点源泄漏情况下的氨气射流及扩散过程。结果表明,高体积分数危险区域主要集中在隧道顶棚附近,更高截面的体积分数处于爆炸极限的区域更长。泄漏源与洞口之间的隧道中段区域的体积分数梯度相对两端较小,此中段区域也是人员安全高度截面最高氨气体积分数发生位置。最大泄漏量情况下氨气在沿纵向扩散过程中平均运动速率保持在0.63~1.06 m/s,扩散速率随纵向距离增加而降低。顶棚氨气体积分数升高程度随纵向距离增加呈幂函数降低,体积分数沿纵向衰减规律适用于其他泄漏量的情况。后期工作可考虑开展缩尺试验,并同时考虑通风条件等因素对氨气泄漏扩散的影响研究。发展的氨气在隧道内泄漏扩散的体积分数分布经验公式可为氨气事故后果评价、应急处置等工作提供参考。     

Gas dispersion risk analysis of safety gap effect on the innovating FLNG vessel with a cylindrical platform

While the effect of the safety gap on explosions is well known, little has been carried out to evaluate the effect of the safety gap on dispersion of gas releases, this paper evaluates the effect of safety gap on gas dispersion for a cylindrical Floating Liquefied Natural Gas (FLNG) vessel. The realistic ship-shaped and circular FLNG platforms are established and used for the detailed CFD based analysis; rather than the structural and hydrodynamics advantages of mobility, stability and cost efficiency etc., this study aims to investigate the safety of gas dispersion on the cylindrical FLNG and compare the safety gap effects on different configurations. A series of different safety gap configurations are evaluated for gas dispersion occurring in near field for the traditional FLNG while both near field and far field gas dispersion simulations are conducted on the cylindrical one. The overall results indicate that the safety gap is effective in reducing the gas cloud size in both FLNG configurations, however, when it comes to the gas dispersion in the far field against the leakage point, the safety gap increases the gas cloud size in the cylindrical FLNG vessel on the contrary.     

Influence of built-in obstacles on unconfined vapor cloud explosion

The obstacle structure in the vapor cloud has a significant influence on the gas explosion. Obstacles could not only lead to the acceleration of flame, but also they may occupy some space, thus affecting the amount of combustible gas. In this paper, a new two-step method was proposed to respectively study the effects of the obstacles amount and volume blockage ratio (VBR) on the gas explosion by using Computation Fluid Dynamic software AutoReaGas, and the obstacles in the vapor cloud were set to “Solid” instead of “Subgrid”. Based on the results and analysis, it is found that the peak overpressure and the maximum combustion rate rise with the increase of the number of obstacles for a single VBR, which indicated that the vapor cloud explosion of more obstacles was more dangerous for a single VBR. However, under a single number of obstacles, the peak overpressure and the maximum combustion rate increase firstly and then decrease as VBR increases and reach the highest at the VBR of 0.74, which indicated that the intensity of vapor cloud explosion reach a peak at a certain VBR in the middle instead of the largest. In addition, the existence and structure of obstacles have little effect on the size of explosion fireball when the size and concentration of combustible gas cloud are the same.     

亚氯酸钠/纯碱溶液处理硝基甲烷工艺废气的脱硝研究

针对硝基甲烷工艺尾气中的高浓度氮氧化物的去除问题,在自行设计的四级填料喷淋吸收塔中进行湿法脱硝研究,实验条件下总脱硝效率能达到85%。实验先采取亚氯酸钠溶液对尾气进行氧化处理,后使用纯碱溶液对尾气进行吸收处理,并对气速、液气比、温度、溶液pH值等工况参数进行了研究,确定了最佳实验条件。     

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。     

A multi-component two-phase flow algorithm for use in landfill processes modelling

This paper describes the finite difference algorithm that has been developed for the flow sub-model of the University of Southampton landfill degradation and transport model LDAT. The liquid and gas phase flow components are first decoupled from the solid phase of the full multi-phase, multi-component landfill process constitutive equations and are then rearranged into a format that can be applied as a calculation procedure within the framework of a three dimensional array of finite difference rectangular elements.The algorithm contains a source term which accommodates the non-flow landfill processes of degradation, gas solubility, and leachate chemical equilibrium, sub-models that have been described in White and Beaven (2013).The paper includes an illustration of the application of the flow sub-model in the context of the leachate recirculation tests carried out at the Beddington landfill project. This illustration demonstrates the ability of the sub-model to track movement in the gas phase as well as the liquid phase, and to simulate multi-directional flow patterns that are different in each of the phases.