Recent application of Computational Fluid Dynamics (CFD) in process safety and loss prevention: A review

In recent years, significant progress has been made to ensure that process industries are among the safest workplaces in the world. However, with the increasing complexity of existing technologies and new problems brought about by emerging technologies, a strong need still exists to study the fundamentals of process safety and predict possible scenarios. This is attained by conducting the corresponding consequence modeling and risk assessments. As a result of the continuous advancement of Computational Fluid Dynamics (CFD) tools and exponentially increased computation capabilities along with better understandings of the underlying physics, CFD simulations have been applied widely in the areas of process safety and loss prevention to gain new insights, improve existing models, and assess new hazardous scenarios. In this review, 126 papers from 2010 to 2020 have been included in order to systematically categorize and summarize recent applications of CFD for fires, explosions, dispersions of flammable and toxic materials from accidental releases, incident investigations and reconstructions, and other areas of process safety. The advantages of CFD modeling are discussed and the future of CFD applications in this research area is outlined.     

The influence of the level of definition of functional specifications on the environmental performances of a complex system. EcoCSP approach

The tendency towards a homogenous mode of development modelled on that of Western countries means that sustainable development has become increasingly urgent. It is necessary to thoroughly redefine products and their expected performances in such a way that the consequences are compatible with sustainable development. In the domain of product design, this means that it is no longer sufficient to use assessment tools “after the fact” to check the impact of products whose functional unit (FU) was defined prior to production; it is now necessary to rethink the definition of the FU itself. This article aims to present an approach based on a combination of life cycle analysis methods and problem-solving by constraint satisfaction. This original approach makes it possible to vary the design of the different dimensions of the FUs of a complex system and thus to make it easier to identify the best architecture along with the best functional definition of the system. In this study, the EcoCSP approach is applied to define the functional performances of an ecological passenger ferry. The complexity of couplings between subsystems and the sheer number of those subsystems mean that the designer has to use “intelligent” tools. These simulate a great number of scenarios and help him/her to fine-tune the system and make the right technological choices with regard to the right functional specifications.     

Liquefaction process for a hydrothermally treated waste mixture containing plastics

Most landfilled plastic waste is a mixture or is in the form of composites with incombustible wastes such as glass, metals, and ceramics. After hydrothermal treatment, including a steam-explosion process, the separation of mixed waste (MW) into organic and inorganic substances becomes easy. However, the effect of hydrothermal pretreatment on the subsequent liquefaction of organic substances from MW is not obvious. In this study, the effects on the liquefaction of polystyrene and high-density polyethylene are discussed. Moreover, optimum conditions for the liquefaction of organic substances from hydrothermally treated MW are identified. By means of this hydrothermal pretreatment, including the steam-explosion process, polystyrene and high-density polyethylene can be significantly converted to oil by liquefaction at 300°–400°C. In comparison with liquefaction of hydrothermally pretreated mixed waste (HMW) at 300°–400°C with a batch type reactor, the yield of oil increases significantly on liquefaction using a semi-batch type reactor. It is considered that the radical chain and termination reactions among the radicals from HMW were inhibited in the semi-batch type reactor. On liquefaction of HMW in a semi-batch reactor, the conversion of HMW to oil was enhanced on increasing the liquefaction temperature to 350°C and the holding time to 60 min. Chemical Feedstock Recycling & Other Innovative Recycling Techniques 6     

基于道化法(DOW)的计算机辅助软件开发

传统的评价方法费时费力,效率低下.将计算机技术与评价方法相结合是评价工作发展的趋势.介绍了为世界各国石油化工企业所广为接受的美国道化学公司(DOW)火灾、爆炸危险性指数评价法,以及根据该法的评价思路所开发的辅助软件的设计思路和功能.     

粒径对镁粉爆炸特性的影响

在简要分析了镁粉爆炸的过程和特性基础上,结合在20 L球型爆炸测试装置中对粒径D50为6,47,104,173 μm镁粉的爆炸特性实验数据,着重分析了粒径对镁粉爆炸特性所产生的影响.实验结果表明,随着粒径的增大,镁粉的爆炸危险性随之减小.     

铁路运输传爆药安全性评价

通过对现有传爆药安全性综合评价方法和装载加固评价方法进行改进,建立导弹铁路运输安全评价模型,运用改进型安全评价方法计算出导弹运输实际现实危险度。通过重大事故后果模拟法对运输过程中存在的最大量危险源进行分析、模拟,得出发生事故后产生的对人、物的危害范围。运用装载加固安全评价方法对装载加固方案进行评价,从而得知铁路运输导弹的危险综合程度,该评价模型可为铁路运输部门危险货物运输安全评价提供参考。     

激波诱导下煤粉的爆炸压力测试

因气体爆炸导致沉积粉尘的二次爆炸的威力远大于单纯的气体或者粉尘爆炸产生的威力,利用自制的装置,诱导煤粉爆炸的激波由甲烷气体爆炸产生,对激波诱导下煤粉的爆炸压力Pmax、爆炸压力上升速率(dp/dt)max进行了实验研究。该实验分别研究煤粉浓度及煤粉粒度对爆炸指数的影响,其结果表明:对于不同的煤粉浓度,存在一个理想煤粉浓度值,在这个浓度下的煤粉爆炸压力值最大;随着煤粉粒度的减小,其爆炸压力不断升高。     

模糊事故树在分析氯乙烯单体槽爆炸风险中的应用

在对氯乙烯单体槽爆炸事故构建事故树的基础上,根据现场设备实际运行状况的统计及依据专家经验所提供的模糊信息,运用模糊事故树理论,引入L-R型模糊数,应用其尖态型隶属函数,对氯乙烯单体槽进行了模糊可靠性分析,求出了氯乙烯单体槽爆炸事故的模糊概率可能性分布;并利用结构重要度系数近似值法对其进行结构重要度分析,运用对事故树底部事件进行排序分级的加权结构重要度分析法,确立了影响系统的最主要因素,为系统安全分析提供了新的方法和途径。     

HAN阻隔防爆模型研究

通过合理简化,利用多方气体状态方程,分别建立油品储运容器内可燃混合气体定容爆炸模型和装设阻隔防爆材料的油品储运容器内可燃混合气体爆炸模型,获得了阻隔防爆性能测试装置的燃爆容器抗爆设计限值,以及其在HAN阻隔防爆测试中燃爆容器试爆压力量级的控制下限值,同时,还给出HAN工程应用中容器留空率的计算方法,具有实际指导意义。