粉碎研磨设备粉尘爆炸的预防

粉碎研磨设备火灾爆炸事故发生率较高。针对该过程的火险特点,防火对策应从防止粉尘沉积,消除粉尘源,防止摩擦、撞击、生热,消除静电危害,搞好工艺防火,惰性介质保护,设置防爆泄压装置,粉尘爆炸的抑制,火灾事故处理措施,加强消防安全教育诸方面加以考虑。     

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。     

甜菜制糖生产废水提标改造设计分析

食品废水处理对我国的经济发展以及环境业提高具有重要的推动作用。本文以某制糖厂为例,对甜菜制糖废水处理站的提标改造工程进行详细分析,在此基础上进行合理设计。     

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.     

中国安全生产政策变迁及其内在逻辑——基于间断均衡模型的实证分析*

为全面发挥安全生产政策对推进安全生产治理体系与治理能力现代化的保障作用,基于间断均衡模型审视改革开放以来我国安全生产政策变迁过程,并提出将其划分为3个均衡期和2个间断期。研究结果表明:在政策目标的转换下,我国安全生产政策变迁先后历经“生产安全”、“安全发展”与“总体安全”3个阶段的深刻调整。决策主体注意力分配、焦点事件持续冲击与地方政府创新供给利用改变政策场域而影响安全生产政策变迁,分别呈现“原动力”、“驱动力”与“拉动力”的作用机制,具有典型的中国情境。研究结果可为廓清中国安全生产政策变迁机制提供理论思考。     

着床后引燃对电弧迸溅熔珠组织特征的影响

为探究迸溅熔珠着床后的热交换过程对其组织特征的影响,建立基于着床后高温迸溅熔珠的动态测温方法,从而揭示迸溅熔珠着床后引燃与否对其组织特征形成的影响规律。研究结果表明：引燃可燃物的熔珠受火焰热反馈和铜氧化放热的共同作用,着床后其温度出现反复波动,延长迸溅熔珠的冷却凝固时间,组织呈等轴状;无法引燃可燃物的熔珠在可测范围内,短暂升温后降温速率持续上升,组织更易呈现树枝状或胞状。研究结果可为准确认定电气故障电弧迸溅熔珠引发火灾提供技术支持。     

某处理厂CASS池改造工艺选择及运行效果

随着污水处理厂排到受纳水体标准的不断提高及区域污染物排放限值的要求,已建的污水处理厂需要提标改造提高排放标准。本文所提工程对现有的CASS池进行改造,通过投加悬浮填料形成CASS+MBBR工艺,其中TN污染物的去除率可提高到8%~15%间,其它污染物也能达到预期的设计标准。