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991.
The pure decomposition behavior of 2,2′-azobis (isobutyronitrile) (AIBN) and its physical phase transformation were examined and discussed. The thermal decomposition of this self-reactive azo compound was explored using differential scanning calorimetry (DSC) to elucidate the stages in the progress of this chemical reaction. DSC was used to predict the kinetic and process safety parameters, such as self-accelerating decomposition temperature (SADT), time to maximum reaction rate under adiabatic conditions (TMRad), and apparent activation energy (Ea), under isothermal and adiabatic conditions with thermal analysis models. Moreover, vent sizing package 2 (VSP2) was applied to examine the runaway reaction combined with simulation and experiments for thermal hazard assessment of AIBN. A thorough understanding of this reaction process can identify AIBN as a hazardous and vulnerable chemical during upset situations. The sublimation and melting of AIBN near its apparent onset decomposition temperature contributed to the initial steps of the reaction and explained the exothermic attributes of the peaks observed in the calorimetric investigation. 相似文献
992.
993.
为探索钢筋混凝土旧工业厂房的改造与加固风险,进行了实地调研和基础理论研究,借助SPSS 22.0统计软件对32个二级指标进行筛选,确立6个方面29个指标的改造加固风险评价指标体系,运用结构方程模型(SEM)实证分析关键影响因素及其作用路径。研究结果表明:设计方案、结构特征和施工技术对改造加固风险具有影响;结构特征与设计方案之间的强关联形成了隐性且重要的风险路径。基于关键影响因素及因素间关联关系,对宝鸡市某U型厂房主体结构加固实例提出建议,为此类项目的改造施工提供理论依据。 相似文献
994.
针对采空区塌陷危险性评价方法中的赋权争议问题,基于偏序集理论提出偏序集评价模型。首先阐明评价指标并确定其分级标准;然后应用偏序集评价模型得到Hasse图,并通过图展现的层集信息判别采空区塌陷危险程度;最后应用该模型对大宝山矿11个采空区的塌陷程度进行判别,评价结果准确合理。研究结果表明:该模型避免了以往研究中的赋权争议问题,克服了样本量不足致使模型无法应用的问题,而且能够应用更多的赋权方法识别排序的稳定程度,体现出样本间的分层信息。 相似文献
995.
危险品道路运输过程风险管理体系探讨 总被引:5,自引:0,他引:5
危险品道路运输是一个复杂的系统,风险管理涉及危险品运输规划和事故应急响应。本文介绍了现有的危险品运输风险管理模式和基本管理原则,基于运输风险评估、运输路径优化、应急单位优化选址和选线、人员疏散管理以及事件决策管理等构建了危险品道路运输过程风险管理体系,阐述了系统基本要素之间的相互关系。危险品道路运输过程风险管理是一个持续改进的结构化过程风险管理体系,有助于减少危险品运输事故概率和降低运输沿线影响人员风险,为政府监管部门和危险品生产经营单位的运输安全管理、优化选线以及应急救援等工作提供技术依据,合理规划危险品运输系统。 相似文献
996.
介绍了火力发电厂设备中的汽轮机的本体结构, 以及汽轮机的安全评价内容.针对汽轮机的本身特点和安全评价内容,提出了两种安全评价方法对汽轮机进行安全评价. 相似文献
997.
998.
R. P. Cleaver P. S. Cumber A. Halford 《Journal of Loss Prevention in the Process Industries》2003,16(6):533-543
The paper presents a mathematical model for predicting outflow rates from a ruptured pipeline transporting compressed volatile liquids. The main focus of the paper is the methodology used to predict thermodynamic properties of interest. The model is validated using experimental data in the open literature. As the field scale outflow data does not include typical operating conditions the model is further validated at higher pressures and longer pipelines by comparing outflow rates calculated using a commercial pipeline simulation package, PROFES. The mathematical model predictions of mass flow rate and pipeline inventory agree well with the measured data and the more sophisticated pipeline model.
The simple pipeline rupture model is a useful tool for consequence analysis as it has a fast runtime on a standard PC. A further advantage is it is more easily, without having to address all of the numerical issues that arise when using a more sophisticated pipeline model. This allows a safety engineer to focus on the potential hazard rather than driving the model. 相似文献
999.
I-Risk: development of an integrated technical and management risk methodology for chemical installations 总被引:1,自引:0,他引:1
I. A. Papazoglou L. J. Bellamy A. R. Hale O. N. Aneziris B. J. M. Ale J. G. Post J. I. H. Oh 《Journal of Loss Prevention in the Process Industries》2003,16(6):575-591
This paper presents an integrated quantitative risk assessment method for hazardous installations, taking into account management as well as technical design and producing risk level measures. The key components of the I-Risk methodology are the technical model, the management model and their interface. The technical model consists of developing a master logic diagram (MLD) delineating the major immediate causes of loss of containment (LOC) and associated quantitative models for assessing their frequency. The management model consists of the tasks, which must be carried out systematically in the primary business functions (such as operations, emergency operations, maintenance and modifications). A management audit quantifies the quality of these management tasks. The management–technical interface modifies certain parameters of the technical model on the basis of the quality of the safety management system of the specific installation. The methodology is exemplified through its application to the risk assessment of an ammonia storage facility. A detailed technical model simulating the response of the system to various initiating events is developed along with a detailed management model simulating the influence of the plant-specific management and organisational practices. The overall effect is quantified through the frequency of release of ammonia as a result of a loss of containment in a storage tank and in a pipeline. 相似文献
1000.
A. Ronza S. Flez R. M. Darbra S. Carol J. A. Vílchez J. Casal 《Journal of Loss Prevention in the Process Industries》2003,16(6):551-560
The historical analysis of 828 accidents in port areas, which have been selected from a database, has been used to identify the sequences of the accidents. Processing these data has allowed the event trees and the probability of the various accident scenarios to be determined. By using these event trees and figures detailing the frequency of the events that initiated the accidents, as taken from various authors, the frequency of the accidents has been determined. 相似文献