超滤处理含聚污水过程中通量衰减机理的研究

研究了超滤处理含聚合物污水过程中操作压力、膜面流速、聚合物浓度、料液流变性、阻力等影响因素对膜通量的影响,并进行理论分析,揭示了通量衰减机理.研究结果表明,通量衰减的机理是聚合物的浓差极化和凝胶层的形成,其次是原油和无机物对膜孔的堵塞.     

极地冻土低温力学特性及井眼坍塌风险分析

为解决极地冻土区油气资源储量极大但其力学特性和钻井井壁失稳机理尚不清晰的问题,对冻土岩样开展低温三轴力学特性实验,并基于此开展钻井井壁坍塌失稳相关数值模拟分析.结果表明:冻土的极限强度会随温度的降低和围压的增大而逐渐提高;冻土弹性模量尽管会随温度的降低而增加,但受围压影响较小,而泊松比基本不受温度及围压的影响;冻土内聚...     

基于三层网络的SBR法深度脱氮智能控制系统的中试研究

以一座处理量为60m3·d-1的SBR法中试系统为研究对象,将三层网络智能控制技术引入SBR工艺中,并对该智能控制系统的深度脱氮效果和稳定性进行了中试研究.在SBR法硝化反硝化过程中,pH、DO、ORP曲线上会出现反映生物脱氮进程的特征点,以pH、DO、ORP为控制参数建立的智能控制策略可以准确判断反应的终点,避免了过度曝气,在保证深度脱氮的前提下节省了能耗.经过10个月的稳定运行,即使在温度较低的情况下,该SBR法智能控制中试系统出水的各项指标完全能够达到国家污水排放一级标准,并且达到了深度脱氮的效果,出水COD低于50 mg·L-1,总氮低于5 mg·L-1.     

气象激光雷达的城市边界层探测

为了研究城市边界层结构变化特征,2005年7月利用气象激光雷达在南京城区做了城市边界层探测试验,就此次观测试验作了简要叙述并选取部分观测资料为示例,着重对气象激光雷达确定城市边界层高度垂直分布及逐时变化以及地面气象环境对边界层的日变化影响进行了初步分析.结果表明,主要由近地层对流混合形成的城市边界层高度具有典型的日变化特点,早晚比较低,日间有一个从低到高再到低的变化过程.提出了一种由边界层混合状态确定边界层高度的方法.分析结果表明,由气溶胶消光系数确定城市边界层高度比较准确.将MSL探测结果与同步的低空无线电探测仪的温度探测结果进行比较,结果表明,两者获得的实际廓线分布相当吻合,线性良好.就地表温度、辐射、湿度及云等气象要素对边界层垂直分布及时间变化的影响做了分析.结果表明,这些气象要素的分布对城市边界层高度的垂直分布及其逐时变化有明显影响.     

江西星子镇沙岭沙山顶部一处红色砂层的粒度分析及释光年代研究

鄱阳湖作为我国最大淡水湖,其周边分布若干沙山。此前研究多认为这些沙山为风成堆积的产物。选取星子镇沙岭沙山顶部（吴淞高程约58.3 m）一处红色砂层（含泥质团块）为研究对象,开展粒度分析和释光测年,以进一步揭示其形成环境和年代。粒度结果为：（1）以中粗砂为主;（2）粒度分选性差;（3）频率分布曲线显示该红色砂层包含多峰;（4）概率累积曲线显示该红色砂层包含1个推移组分、2个跃移组分和4个悬移组分;（5）萨胡判别公式值均>-2.74。之后,对红色砂层下伏泥层、红色砂层和红色砂层上覆黄色砂层开展石英单颗粒释光测年,其年代分别为：(24.7±2.1) ka、(24.0±2.4) ka和(22.4±3.9) ka。研究表明该红色砂层虽然形成于MIS2阶段,但其不是干旱环境下的风成沉积砂层。     

横通道通风对隧道火灾烟气蔓延影响的数值模拟研究

为探究隧道横通道通风对隧道火灾烟气蔓延的影响规律,使用火灾动力学模拟软件FDS,对不同火源位置的横通道临界风速、主隧道温度分布以及烟气层高度进行研究。研究结果表明：在一定火源功率范围内,隧道横通道临界风速与火源功率的1/3次方成正比且火源距横通道越远,临界风速越小;当火源位于交叉口,横通道使用临界风速通风时,隧道内烟气温度明显降低,烟气迅速沉降到2 m以下;当火源距离交叉口10,20 m,横通道通风会加快火源下游烟气沉降,烟气沉降速度随横通道通风速率的增大而增大;当火源位于交叉口时,烟气沉降由横通道通风对烟气的降温作用和涡旋作用共同主导,当火源位于距离交叉口10,20 m时,烟气沉降主要由涡旋作用主导。     

Numerical study on premixing characteristics and explosion process of starch in a vertical pipe under turbulent flow

Fire and explosion accidents are frequently caused by combustible dust, which has led to increased interest in this area of research. Although scholars have performed some research in this field, they often ignored interesting phenomena in their experiments. In this paper, we established a 2D numerical method to thoroughly investigate the particle motion and distribution before ignition. The optimal time for the corn starch dust cloud to ignite was determined in a semi-closed tube, and the characteristics of the flame propagation and temperature field were investigated after ignition inside and outside the tube. From the simulation, certain unexpected phenomena that occurred in the experiment were explained, and some suggestions were proposed for future experiments. The results from the simulation showed that 60–70 ms was the best time for the dust cloud to ignite. The local high-temperature flame clusters were caused by the agglomeration of high-temperature particles, and there were no flames near the wall of the tube due to particles gathering and attaching to the wall. Vortices formed around the nozzle, where the particle concentration was low and the flame spread slowly. During the explosion venting, particles flew out of the tube before the flame. The venting flame exhibited a “mushroom cloud” shape due to interactions with the vortex, and the flame maintained this shape as it was driven upward by the vortex.     

气凝胶消防服隔热层研制的可行性分析

为了减少火焰环境对消防员的伤害,基于消防服隔热层对消防员生命安全保障的重要性,运用对比描述的方法对现有隔热层进行了分析比较,探究了其优缺点和性能,提出了轻质且具有优异隔热性能是隔热层的发展趋势,通过对气凝胶性能的理论分析和服用性能分析,研究了利用气凝胶材料研制消防服的隔热层,结果表明气凝胶在服装领域应用已经比较广泛,在消防服领域中也已有初步应用,但用气凝胶研制消防服隔热层仍存在着一定的挑战。     

铁路沿线可燃重气储罐最小隔离区域划分探讨*

为保护铁路线,以某化工厂距离高铁路线最近的丙烯球罐为例,提出丙烯球罐泄漏最小隔离区域划分方法以及2种保护高铁线路方案,利用重气扩散模型和定量风险评价（QRA）软件分别进行丙烯扩散模拟、爆炸模拟,并进行危险与可操作性分析（HAZOP）和保护层分析（LOPA）。结果表明:球罐发生泄漏及火灾爆炸等事故,会给附近铁路线带来严重破坏;丙烯泄漏或球罐因周围其他设备设施或可燃物质着火而温度升高时,保护措施不足;隧道的安全可靠性要高于仅设1道防爆墙,隧道长度需覆盖最小隔离区域的可及范围,在扩散区域内也需设立普通挡墙,在极度危险情况下,需要实施高铁停开等保护措施。     

Effect of pyrolysis and oxidation characteristics on lauric acid and stearic acid dust explosion hazards

The effect of pyrolysis and oxidation characteristics on the explosion sensitivity and severity parameters, including the minimum ignition energy MIE, minimum ignition temperature MIT, minimum explosion concentration MEC, maximum explosion pressure P_max, maximum rate of pressure rise (dP/dt)_max and deflagration index K_st, of lauric acid and stearic acid dust clouds was experimentally investigated. A synchronous thermal analyser was used to test the particle thermal characteristics. The functional test apparatuses including the 1.2 L Hartmann-tube apparatus, modified Godbert-Greenwald furnace, and 20 L explosion apparatus were used to test the explosion parameters. The results indicated that the rapid and slow weight loss processes of lauric acid dust followed a one-dimensional diffusion model (D1 model) and a 1.5 order chemical reaction model (F1.5 model), respectively. In addition, the rapid and slow weight loss processes of stearic acid followed a 1.5 order chemical reaction model (F1.5 model) and a three-dimensional diffusion model (D3 model), respectively, and the corresponding average apparent activation energy E and pre-exponential factor A were larger than those of lauric acid. The stearic acid dust explosion had higher values of MIE and MIT, which were mainly dependent on the higher pyrolysis and oxidation temperatures and the larger apparent activation energy E determining the slower rate of chemical bond breakage during pyrolysis and oxidation. In contrast, the lauric acid dust explosion had a higher MEC related to a smaller pre-exponential factor A with a lower amount of released reaction heat and a lower heat release rate during pyrolysis and oxidation. Additionally, due to the competition regime of the higher oxidation reaction heat release and greater consumption of oxygen during explosion, the explosion pressure P_m of the stearic acid dust was larger in low concentration ranges and decayed to an even smaller pressure than with lauric acid when the concentration exceeded 500 g/m³. The rate of explosion pressure rise (dP/dt)_m of the stearic acid dust was always larger in the experimental concentration range. The stearic acid dust explosion possessed a higher P_max, (dP/dt)_max and K_st mainly because of a larger pre-exponential factor A related to more active sites participating in the pyrolysis and oxidation reaction. Consequently, the active chemical reaction occurred more violently, and the temperature and overpressure rose faster, indicating a higher explosion hazard class for stearic acid dust.