Improved models of failure time for atmospheric tanks under the coupling effect of multiple pool fires

Fire accidents of chemical installations may cause domino effects in atmospheric tank farms, where a large amount of hazardous substances are stored or processed. Pool fire is a major form of fire accidents, and the thermal radiation from pool fire is the primary hazard of domino accidents. The coupling of multiple pool fires is a realistic and important accident phenomenon that enhances the propagation of domino accidents. However, previous research has mostly focused on the escalation of domino accidents induced by a single pool fire. To overcome the drawback, in this study, the failure of a storage tank under the coupling effect of multiple pool fires was studied in view of spatial and temporal synergistic process. The historical accident statistics indicated that the accident scenario of two-pool fires accounted for 30.6% in pool fires. The domino accident scenario involving three tanks is analyzed, and the typical layout of tanks is isosceles right triangle based on Chinese standard “GB50341-2014”. The thermal response and damage of a target tank heated by pool fires were numerically investigated. The volume of 500 m³, 3000 m³, 5000 m³ and 10000 m³ were selected. Flame temperature was obtained by FDS, and then was input onto the finite element model. The temperature field and stress field of target tanks were simulated by ABAQUS. The results showed that the temperature rise rate of the target tanks under multiple pool fires was higher than that under a single pool fire. The failure time of the tank under the coupling effect of multiple fires was lower than that under the superposition of multiple fires without the first stage. The stress and yield strength were compared to judge the failure of the target tank. The model of failure time for the tank under the coupling effect of pool fires was established. Through the verification, the deviation of this model is 4.02%, which is better than the deviation of 15.76% with Cozzani's model.     

街道峡谷对称性对污染物扩散的影响

采用数值模拟的方法,研究了行列式和错列式街谷两侧建筑物的对称性对街谷内和下游建筑尾流区污染物浓度的影响,并引入3个用于评价室内空气环境的指标来描述街谷中人员区域内的空气质量.结果表明,平均残留时间(ART)和有效通风率(PFR)可用于评价不对称街谷内的空气质量.街谷的不对称性对街谷内部和下游建筑尾流区污染物浓度分布均有明显影响.下游建筑越低,则尾流区的浓度越高.行列式和错列式街谷中人员活动空间的无量纲平均浓度分别在建筑高度比例为7/3和7/2时最大.为在城市规划中尽可能避免出现最不利比例的街谷,根据平均残留时间和有效通风率等指标,给出了上下游建筑高度比与最不利街谷改善率的关系.     

基于多源数据融合的石油罐区安全监控模型

由于单一传感器在石油罐区安全监控中容易受到外界因素影响从而产生误差,为提高传感器检测结果的可靠性和罐区安全监控预警的准确性,基于多源数据融合技术,建立罐区安全状态预警模型。首先,介绍了多源数据融合技术的3个层级:数据级融合,特征级融合和决策级融合,以及目前各领域常见的数据融合方法;其次,建立了基于最优加权融合算法的一级融合模型和基于BP神经网络算法的二级融合模型;最后,得到石油罐区安全监控数据融合模型,并为进一步的实践应用打下了理论基础。     

基于火灾场景的大型浮顶储罐区全过程风险防范体系研究

针对大型浮顶罐区火灾事故风险特征,通过对火灾场景辨识及其火灾风险影响因素分析,结合预防初期火灾场景风险要素和消防系统有效性,提出了罐区火灾事故现实风险的评估框架及确定方法。在此基础上,构建了基于火灾场景的全过程风险防范体系,包括库区评估规划、罐体本质安全化设计、库区火灾预防、罐区火灾扑救、园区火灾事故管理等5个方面,并给出相应的对策措施。大型浮顶罐区全过程火灾风险防范是一个持续改进的结构化过程风险管理体系,有助于实现罐区火灾风险的过程安全管理,进而提高仓储型园区的整体消防安全保障能力和风险防控水平。     

储罐长周期腐蚀声发射监测试验

对一放置2年时间的储罐试验模型进行长周期的声发射腐蚀监测,通过研究其在稳定腐蚀状态下的声发射信号特征,分析其腐蚀的机理和信号产生的原因,形成对储罐腐蚀更深入的认识。文章还对稳定腐蚀状态下的储罐声发射特征参数进行统计分析,为后续的储罐在线声发射检测评价打下数据基础。     

液氧储罐爆炸事故树分析

采用安全系数工程的方法,对液氧储罐爆炸进行丁事故树分析,通过求事故树最小割集,进行结构重要度分析,从而对液氧储罐爆炸的事故原因进行分析、预测,并提出了相应的预防控制措施。     

基于潜在生命损失的危险化学品仓储区规划选址和安全布局方法研究

在现有基于风险的土地使用安全规划方法的基础上,通过引入潜在生命损失这一综合风险评价指标,建立了基于移动危险源潜在生命损失的危险化学品仓储区规划选址模型和基于固定危险源潜在生命损失的仓储区安全布局优化模型。在此基础上,提出了危险化学品仓储区规划选址和安全布局优化方法,并通过案例分析验证了该方法的适用性和可行性。采用该规划选址和安全布局优化方法可提高区域土地使用安全规划的效率,为进行城市重大危险源的规划选址和安全布局提供了新的思路。     

Fermentative hydrogen production from beet sugar factory wastewater treatment in a continuous stirred tank reactor using anaerobic mixed consortia

A low pH, ethanol-type fermentation process was evaluated for wastewater treatment and bio-hydrogen production from acidic beet sugar factory wastewater in a continuous stirred tank reactor (CSTR) with an effective volume of 9.6 L by anaerobic mixed cultures in this present study. After inoculating with aerobic activated sludge and operating at organic loading rate (OLR) of 12 kgCOD?m^-3·d^-1, HRT of 8h, and temperature of 35°C for 28 days, the CSTR achieved stable ethanol-type fermentation. When OLR was further increased to 18 kgCOD?m^-3·d^-1 on the 53rd day, ethanol-type fermentation dominant microflora was enhanced. The liquid fermentation products, including volatile fatty acids (VFAs) and ethanol, stabilized at 1493 mg·L^-1 in the bioreactor. Effluent pH, oxidation-reduction potential (ORP), and alkalinity ranged at 4.1–4.5, -250–(-290) mV, and 230–260 mgCaCO₃?L^-1. The specific hydrogen production rate of anaerobic activated sludge was 0.1 L?gMLVSS^-1·d^-1 and the COD removal efficiency was 45%. The experimental results showed that the CSTR system had good operation stability and microbial activity, which led to high substrate conversion rate and hydrogen production ability.     

昆明主城合流污水调蓄池截污效能模拟

为评估昆明市计划首批建设二环路内16座合流污水调蓄池(规模为21.3×104 m3)的环境效益,采用构建降雨径流管理模型(SWMM)模拟调蓄池的运行情况,对其截污效能进行分析. 结果表明,2008年的113场降雨中,调蓄池共截流污水量1 868.73×104 m3,COD_Cr、TN、TP污染负荷的截流量分别为5 195.28、810.76、68.78 t,污水截流量占合流污水溢流量的11.18%. 昆明主城调蓄池是在充分利用和衔接已建、在建的排水管网收集系统和污水处理设施的基础上设计的,调蓄池效能受既定配套条件、场地、降雨特征等的多重影响,建议加大调蓄池和污水处理厂的联动性,并采取集中调蓄截流为主、分散式面源治理为辅的策略,综合防治初期雨水径流污染和合流污水溢流污染.