基于“事故树-层次分析法”的高校学生宿舍火灾风险分析

高校学生宿舍的消防安全是高校安全管理的重要内容之一。对学生宿舍的消防进行风险分析对高校的安全管理具有重要意义。本文采用层次分析法对高校宿舍的消防安全进行风险分析。在进行层次分析法之前,引入了事故树,通过事故树寻求指标层中各类重要因素,从而提高了层次分析的准确性和有效性。分析结果表明：采用事故树-层次分析法,可定量地分析各个因素对建筑火灾风险的影响大小,对制定建筑火灾的防范措施具有一定的指导意义。分析结果表明：消防设施、火灾荷载和安全疏散设备对学生宿舍的火灾安全有着重要的影响,应该引起安全管理人员的重视。     

浅议AP1000核电建造过程本质安全化

为推进我国核电产业技术水平的整体跨越,实现我国第三代核电AP1000的自主化过程中的安全,国家核电技术公司（以下简称“国家核电”）在建造过程中通过加强从业人员安全培训、企业安全文化建设和依托项目的安全管理,大力提升人的本质安全化水平;广泛采用新技术、改进施工工艺,实行模块化、专业化施工,加大安全基础设施投入力度,强化建造过程中的安全控制,努力打造核电建造过程中物的本质安全;完善安全管理制度,建设安全责任体系和监督体系,持续提高管理上的本质安全。     

实验室煤与瓦斯突出模拟试验回顾及展望

为借鉴国内外煤与瓦斯突出模拟试验研究成果,查阅大量相关文献,进行分析和总结。以人们对煤与瓦斯突出试验研究的深入程度为主线,将实验室煤与瓦斯突出模拟试验的研究历程进行阶段划分。研究表明:20世纪50—60年代,成功诱导了突出,初步考察诸因素对突出的影响;70—90年代,深入探究突出发生的力学判据及突出过程,并提出数十种有关突出机理方面的假说;21世纪初,以组建三维模拟试验台进行试验为特点,大大提高了模拟试验条件与现场的相似度,但在力学加载系统的稳定性和可调性、模型的整体密封性、测试探头的精度等方面仍需改进。     

碳酸氢钠及其固态分解产物对玉米淀粉爆炸抑制实验研究

为研究NaHCO3对玉米淀粉爆炸的抑制效果,采用20 L球形爆炸装置测试玉米淀粉在添加不同抑制比NaHCO3及其固态分解产物Na2 CO3后爆炸参数变化规律,并分析NaHCO3抑制淀粉爆炸过程.结果表明:NaHCO3及Na2 CO3对玉米淀粉爆炸均有抑制作用,NaHCO3抑制效果优于Na2 CO3;混合粉尘的最大爆炸压...     

A~2/O联合臭氧污泥减量技术的改造研究

研究了臭氧化污泥减量技术联合A~2/O、倒置A~2/O与传统A~2/O在出水和污泥产率上的变化。结果表明,臭氧化A~2/O、臭氧化倒置A~2/O的出水与传统A~2/O相比未出现恶化,它们对COD和含氮物质的去除率分别为87.4%,53.7%和93%,66.5%,存在倒置A~2/O对臭氧混合液中有机质及含氮物质的利用率较A~2/O高的可能。试验按每克SS投加0.05 g O_3对A2/O与倒置A~2/O产生的约60%剩余污泥处理时,在短期内未造成出水磷含量的大幅升高,并且出水磷含量受臭氧混合液DO、二沉池底部DO的影响,两系统的污泥产率分别较传统A~2/O降低50%,56%。     

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。     

煤矿水害风险量化评价方法

为提高煤矿防治水管理水平,预防和消除矿井水害,在层次分析法的基础上建立中性值作为参照对象对矿井水害风险进行实时评判的方法。根据《煤矿防治水细则》建立以矿井水文地质类型、矿井涌水量标准分数、突水预兆、采掘面位置、探水结果为准则层的层次结构模型,并对各评价指标赋权。依据制定的水害风险评价指标的评分细则和监测监控数据并结合其权重得到水害评价总得分。通过总得分与中性参照分数比较得出预测结果:水害评价总得分大于中性参照分数,证明水害的威胁小,分数越高越安全;反之则水害的威胁较大,分数越低越危险,这时需要加强防治水的力度,令评价分数管控大于中性参照分数。这种方法依赖于井下监测监控数据进行量化评价,能实时、客观、全面且准确地反映煤矿水害的风险情况。     

空气污染天气过程与气象要素之间的关联性分析

随着经济和社会的不断发展,地球的环境正在遭受着严重的侵害,关于环境的问题也日益显现出来,比如全球变暖、雾霾等现象。本文分析了空气污染的因素、气象要素对空气质量的影响,并提出了防治空气污染的对策。     

Inherent thermal runaway hazard evaluation method of chemical process based on fire and explosion index

Thermal runaway hazard assessment provides the basis for comparing the hazard levels of different chemical processes. To make an overall evaluation, hazard of materials and reactions should be considered. However, most existing methods didn't take the both into account simultaneously, which may lead the assessment to a deviation from the actual hazard. Therefore, an integrated approach called Inherent Thermal-runaway Hazard Index (ITHI) was developed in this paper. Similar to Dow Fire and Explosion Index(F&EI) function, thermal runaway hazard of chemical process in ITHI was the product of material factor (MF) and risk index (RI) of reaction. MF was an indicator of material thermal hazards, which can be determined by initial reaction temperature and maximum power density. RI, which was the product of probability and severity, indicated the risk of thermal runaway during the reaction stage. Time to maximum rate under adiabatic conditions and criticality classes of scenario were used to indicate the runaway probability of the chemical process. Adiabatic temperature rise and heat of the desired reaction and secondary reaction were used to determine the severity of runaway reaction. Finally, predefined hazard classification criteria was used to classify and interpret the results obtained by this method. Moreover, the method was validated by case studies.     

Misoperation monitoring and early warning during startup and shutdown of petrochemical units

Most petrochemical units run under extreme conditions, such as high temperatures, pressures, and speeds. Consequently, the equipment operators may commit errors because the startup and shutdown processes usually involve complicated operation steps; moreover, the operators may lack experience in handling abnormal situations. Misoperation can lead to accidents, including fires and explosions. Thus, risk analysis for process operations and the development of preventive measures have become an effective means of avoiding misoperation-related accidents. However, it is challenging to ensure the comprehensiveness of risk-analysis results. In this paper, we present a method for misoperation monitoring and early warning in the startup and shutdown processes of petrochemical units. The mechanisms of misoperation occurrence are summarized based on investigations of serious accidents in the recent past. Knowledge regarding the mechanisms of misoperation is crucial for the risk analysis of petrochemical units. The potential risk information, such as causes, adverse consequences, key monitoring parameters, and prevention control solutions, should be acquired and be employed to construct an early-warning knowledge database. Furthermore, misoperation judgment rules need to be formulated to identify misoperations. The data obtained from the monitoring module, misoperation judgment rules, and analysis results can aid in developing schemes to avoid possible abnormal situations. This paper reports a misoperation monitoring and early-warning system for a hydrogenation unit. As demonstrated, conducting risk analysis to determine the potential operational risks and formulating misoperation judgment rules to analyze the process data are essential for enabling early warning. The application of this method will contribute to operational guidance, economic loss reduction, and accident avoidance.