受限空间内惰性气体对CH4爆炸抑制特性研究

N2和CO2是常用的惰性抑爆气体,为研究两种气体的抑爆特性,采用20L球形爆炸试验装置,分析了不同浓度配比条件下N2/CH4/空气以及CO2/CH4/空气混合气体的爆炸压力,同时采集爆炸后的气体样品,对比分析爆炸后残留气体的主要成分。结果显示:随CH4浓度从5%增加至12.5%时,完全抑制CH4爆炸需要的惰性气体最小量先增大后降低,CH4浓度在6.5%~7.5%之间时,抑爆需要的惰性气体的量最大;在同一CH4浓度条件下,抑爆需要N2的量大于CO2,并且CH4浓度在5%~6.5%时,抑爆需要两种惰性气体的量值差别最大;当CH4浓度一定时,随着加入惰性气体量的增大,爆炸最大超压逐渐降低,惰性气体浓度和爆炸超压之间基本呈线性关系;在同样条件下,相对于N2,CO2为抑爆气体时,爆炸后腔体内残留的CH4浓度较高。研究成果为惰性气体抑爆技术提供技术支撑,同时为揭示惰性气体抑爆机理有一定作用。     

Investigation of pool spreading and vaporization behavior in medium-scale LNG tests

A failure of a Liquefied Natural Gas (LNG) tanker can occur due to collision or rupture in loading/unloading lines resulting in spillage of LNG on water. Upon release, a spreading liquid can form a pool with rapid vaporization leading to the formation of a flammable vapor cloud. Safety analysis for the protection of public and property involves the determination of consequences of such accidental releases. To address this complex pool spreading and vaporization phenomenon of LNG, an investigation is performed based on the experimental tests that were conducted by the Mary Kay O'Connor Process Safety Center (MKOPSC) in 2007. The 2007 tests are a part of medium-scale experiments carried out at the Brayton Fire Training Field (BFTF), College Station. The dataset represents a semi-continuous spill on water, where LNG is released on a confined area of water for a specified duration of time. The pool spreading and vaporization behavior are validated using empirical models, which involved determination of pool spreading parameters and vaporization rates with respect to time. Knowledge of the pool diameter, pool height and spreading rate are found to be important in calculating the vaporization rates of the liquid pool. The paper also presents a method to determine the vaporization mass flux of LNG using water temperature data that is recorded in the experiment. The vaporization rates are observed to be high initially and tend to decrease once the pool stopped spreading. The results of the analysis indicated that a vaporization mass flux that is varying with time is required for accurate determination of the vaporization rate. Based on the data analysis, sources of uncertainties in the experimental data were identified to arise from ice formation and vapor blocking.     

燃煤机组烟囱在线烟尘仪监测烟尘浓度偏高原因分析及对策

除尘电价补贴政策的出台以及新环保标准的实施，一方面提高了电厂降低烟尘排放浓度的积极性，另一方面对烟尘在线监测系统提出了更高的要求。针对一些采用湿法脱硫和无GGH的燃煤机组，会出现烟囱在线烟尘仪监测的烟尘浓度高于电除尘器出口烟尘的浓度，对产生这一现象的原因进行了分析并提出相应的解决对策。     

抛光铝粉爆炸及ABC粉体抑爆特性的实验研究

为研究抛光铝粉的爆炸危险和ABC粉体的抑爆特性，在对实验粉体粒径分布进行分析的基础上，采用20 L粉尘爆炸特性实验装置，分别对不同铝粉尘浓度、不同抑爆剂浓度条件下的爆炸特性参数进行测试。研究结果表明:在实验条件下，铝粉的爆炸下限为45 g/m3＜C＜60 g/m3；随铝粉浓度增加，爆炸烈度呈现出先增强后减弱的变化趋势，在浓度为400 g/m3时爆炸烈度最大。ABC抑爆剂能够有效抑制铝粉爆炸超压和爆炸反应进程，随着惰性粉体浓度的增加，抑制效果愈加明显，爆炸逐渐减弱。当ABC惰性粉体的质量占比增加到50%时，相较单一铝粉爆炸，反应过程时间由72 ms增加至785 ms，爆炸最大压力、最大压力上升速率分别下降了61.7%，89.5%；当ABC粉体质量占比为53%时，铝粉被完全惰化，未发生爆炸。     

综合管廊内火灾自动报警探测器实验研究

为了能够有效提升综合管廊内火灾自动报警系统的准确性和可靠性,本文采用火灾实体试验的方法,通过对各类型火灾自动报警探测器响应时间的情况进行分析和比较,研究综合管廊电力舱内常用探测器的性能。研究结果表明:接触式缆式线型感温火灾探测器可以较早的探测到电缆温度异常变化的现象,可用于早期预警。点型感烟探测器对烟粒子浓度较为敏感,可用于综合管廊电力舱室的空间探测。分布式光纤型感温火灾探测器对明火温度的变化较为敏感,作为空间型的火灾探测器比较可靠。     

深部煤层钻屑粒度随钻进深度分布规律

为了研究煤层钻屑粒度随钻进深度分布规律，选取具有冲击危险性的平煤八矿己15煤作为研究对象，采取钻屑量测试和孔口瓦斯浓度监测，通过筛分实验煤样并应用Rosin Rammler分布模型，探究了钻屑粒度和钻屑量大小随孔深变化关系，分析不同点钻屑粒度分布特征。结果表明:小于0.075 mm钻屑粒度分布随孔深变化与钻屑量变化规律相吻合；不同钻孔随深度变化分别对应不同Rosin Rammler分布函数，随着应力过渡越平缓，粒径分布宽度系数n值越小，煤体应力越大粒径相关系数D越大；不同范围钻屑粒度占比大小也会影响钻屑量大小；在钻屑量较大时，孔口瓦斯体积分数会出现增高现象。通过对钻屑粒度分布规律分析，更好地了解深部煤体应力分布，有助于冲击危险的预警。     

山区和平原连接处SF6试验及扩散规律研究

为更好了解污染物在复杂地形条件下的湍流扩散规律,2010年9月开展了一系列SF6示踪扩散试验,获取了SF6浓度数据,以此实验数据为基础,计算出SF6浓度分布在水平和垂直方向的扩散标准差、地面峰值浓度等参数,并与P-T-C扩散参数进行对比,总结得出了污染物在山区和平原连接处中性、稳定、强稳定等气象条件下湍流扩散规律。     

城市交通干道降雨径流中PAHs的污染特征

以上海、温州市典型交通干道地表径流为研究对象,分析了样品中16种溶解态和颗粒态PAHs浓度,了解了城市交通干道降雨径流中PAHs污染特征及其动态变化过程.结果表明,径流中∑PAHs(包括溶解相、颗粒相)浓度范围为919.8～16711.6ng·L-1,溶解相中PAHs浓度要远低于颗粒相(分别为4.9～1558.0ng·L-1,635.4～16624.0ng·L-1).通过对3场降雨事件中PAHs浓度随降雨过程变化的研究,可以发现并不是所有道路径流都有初期冲刷效应,初期冲刷的产生受雨前干期、降雨强度以及径流量等因素共同作用,因此简单拦截初期径流并不能十分有效地降低PAHs污染负荷.径流中PAHs在颗粒相-水相间的分配系数Kp值为2.3×104～2.5×106L·kg-1,随着悬浮颗粒物含量增加而减少,这可能跟径流过程中颗粒物粒径组成有关.     

生物流化床短程硝化的快速启动及影响因素研究

采用内循环生物流化床反应器处理模拟高浓度氨氮废水,以确定其对处理高浓度氨氮废水的可行性,同时对试验条件进行了优化。结果研究表明:控制温度为(31±1)℃,利用反应器自身流化所携带溶解的空气,反应器内DO值可维持在1.5~2.5 mg/L,调节pH为8.0~8.5。经过42 d的污泥驯化适应时期,进水氨氮(NH4+-N)浓度由50 mg/L提高到300 mg/L。由于流化床采用填料载体微生物膜与活性污泥双重作用,同时载体呈流化状态,接触均匀,有巨大的比表面积,可以使床内保持高浓度的生物量,从而达到高效快速的传质效果。在HRT由开始的16 h缩短到8 h的条件下,氨氮(NH4+-N)的去除率达到90%以上,亚硝氮(NO2--N)的积累率达到75%。且在以后30 d的稳定运行阶段,氨氮(NH4+-N)去除率和亚硝氮(NO2--N)积累率均保持稳定。同时反应器最后出水水质澄清,无需二沉池及污泥处理。     

Size distributions of aerosol and water-soluble ions in Nanjing during a crop residual burning event

To investigate the impact on urban air pollution by crop residual burning outside Nanjing, aerosol concentration, pollution gas concentration, mass concentration, and water-soluble ion size distribution were observed during one event of November 4-9, 2010. Results show that the size distribution of aerosol concentration is bimodal on pollution days and normal days, with peak values at 60-70 and 200-300 nm, respectively. Aerosol concentration is 10⁴ cm^-3. nm^-1 on pollution days. The peak value of spectrum distribution of aerosol concentration on pollution days is 1.5-3.3 times higher than that on a normal day. Crop residual burning has a great impact on the concentration of fine particles. Diurnal variation of aerosol concentration is trimodal on pollution days and normal days, with peak values at 03:00, 09:00 and 19:00 local standard time. The first peak is impacted by meteorological elements, while the second and third peaks are due to human activities, such as rush hour traffic. Crop residual burning has the greatest impact on SO₂ concentration, followed by NO₂, O₃ is hardly affected. The impact of crop residual burning on fine particles (< 2.1 μm) is larger than on coarse particles (> 2.1 μm), thus ion concentration in fine particles is higher than that in coarse particles. Crop residual burning leads to similar increase in all ion components, thus it has a small impact on the water-soluble ions order. Crop residual burning has a strong impact on the size distribution of K⁺, Cl^-, Na⁺, and F^- and has a weak impact on the size distributions of NH₄⁺, Ca²⁺, NO₃^- and SO₄^2-.