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51.
An integrated approach for performance assessment and management of safety barriers in a systemic manner is needed concerning the prevention and mitigation of major accidents in chemical process industries. Particularly, the effects of safety barriers on system risk reduction should be assessed in a dynamic manner to support the decision-making on safety barrier establishments and improvements. A simulation approach, named Simulink-based Safety Barrier Modeling (SSBM), is proposed in this paper to conduct dynamic risk assessment of chemical facilities with the consideration of the degradation of safety barriers. The main functional features of the SSBM include i) the basic model structures of SSBM can be determined based on bow-tie diagrams, ii) multiple data (periodic proof test data, continuous condition-monitoring data, and accident precursor data) may be combined to update barrier failure probabilities and initiating event probabilities, iii) SSBM is able to handle uncertainty propagation in probabilistic risk assessment by using Monte Carlo simulations, and iv) cost-effectiveness analysis (CEA) and optimization algorithms are integrated to support the decision-making on safety barrier establishments and improvements. An illustrative case study is demonstrated to show the procedures of applying the SSBM on dynamic risk-informed safety barrier management and validate the feasibility of implementing the SSBM for cost-effective safety barrier optimization. 相似文献
52.
When a natural disaster occurs, it may damage multiple industrial facilities in a certain area at the same time, and the resulting Natech events may have an impact on the surrounding industrial facilities, generating coupling risk. In this study, the assessment of Natech events coupling risk is conducted using the method of correlated multi-criteria decision-making, and the knowledge of fuzzy measures is introduced to solve the uncertainty problem in Natech coupling risk. Natech Coupling Risk Index is constructed to involve physical and functional facilities. The concept of equivalent population is proposed to compare the risks generated by physical facilities and functional facilities. And economic indicators are added to calculate the comprehensive risk value. The purpose of this contribution is to enable local government managers to use their expertise and resources and the existing risk assessment of the plants themselves and rely on the scoring of experts limitedly to quickly and easily identify potential high Natech risk areas. In the calculation process of coupling risk, the government can also take the lead to promote information communication between different plants and other industrial subjects. The proposed method was applied in a realistic chemical industry area in Guangzhou, China and in a hypothetical town. The result shows that the physical risk may be transferred to the population and economy through the coupling between industrial facilities and the functional link between functional facilities and population and economy. 相似文献
53.
Latex is extensively used in industrial products. However, completing some processes at scale leads to unacceptable levels of risk that need to be quantified and mitigated. Systemic risks must be eliminated wherever possible, and safety takes priority over efficiency and quality. To assess the process risks accurately, four raw materials were examined in this study: polyvinyl acetate (PVA), latex process-initiator-ammonium persulfate (APS) and hydrogen peroxide (H2O2), and vinyl acetate monomer (VAM). The physicochemical composition of the PVA latex process was determined via calorimeters, including differential scanning calorimetry (DSC) and vent sizing package 2 (VSP2). The calorimetry results showed that the protective colloid was a critical component in the polymerisation reaction. In addition, when adding initiators to the system, it is vital to observe the normal ratio of materials and keep the stirring system operating. The scenario system also simulated the effects of shutting down various inhibitory programs, including the build-up of free radicals that could result in a runaway reaction when the initiator was added in excess. On the other hand, the result of the risk matrix displayed as a medium level, indicating that although the probability of an accident is low, the resulting severity is at disaster level. As a result, this study provides process safety engineers with a reliable frame of reference for assessing the potential dangers in the PVA latex manufacturing process. 相似文献
54.
为探究淮河流域安徽段水体与沉积物微塑料赋存特征及生态风险级别,采用野外采样、体式显微镜、扫描电镜、傅里叶红外光谱(FTIR)以及风险指数(H)和污染负荷指数(PLI)模型等方法,分析了流域水体和沉积物微塑料现状,并进行了微塑料生态风险评估.结果表明,流域各点位微塑料检测率为100%,表层水与沉积物微塑料平均丰度分别为(39800±3367) n ·m-3和(5078±447) n ·kg-1,下游微塑料平均丰度要高于上游和中游.水体和沉积物微塑料粒径以20~150 μm为主,占比分别为82.96%和80.77%.微塑料形状主要为纤维(水体76.05%、沉积物84.53%)、薄膜(水体21.83%、沉积物15.43%)和碎片(水体2.12%、沉积物0.04%).水体和沉积物中微塑料主要以透明颜色为主,占比分别为63.31%和83.69%.水体和沉积物主要以聚乙烯(水体65.74%、沉积物80.62%)和聚丙烯(水体18.43%、沉积物9.71%)为主,微塑料主要来源于农业薄膜、废弃渔具渔网和港口人为废弃的塑料袋.微塑料风险指数(H)模型评估表明部分点位风险指数较高,淮河流域安徽段微塑料风险等级为Ⅱ级,污染负荷指数(PLI)模型评估表明流域地表水体和沉积物总体上生态风险较低. 相似文献
55.
56.
采用气相色谱-质谱法(GC-MS)测定了北江中上游流域地表水和沉积物样品中多环芳烃(PAHs)和多氯联苯(PCBs)类污染物的含量,分析了PAHs和PCBs的污染水平和空间分布,并评估了污染物的健康风险和生态风险.结果表明,16种PAHs单体在所有水样和沉积物样品中均被检出,检出范围分别为41.82~443.04 ng·L-1和59.58~635.73 ng·g-1,北江中上游PAHs的污染水平为中、轻度.水中PAHs以二环芳烃和三环芳烃为主,沉积物中以三环芳烃和四环芳烃为主.在水样中检出了17种PCBs,浓度范围0.81~287.50 ng·L-1,以六氯联苯和七氯联苯为主;沉积物中检出了8种PCBs,含量范围0.13~3.96 ng·g-1,以五氯联苯和七氯联苯为主.整个调查区域内地表水中PAHs和PCBs的终生致癌风险指数小于10-4,处于中、低水平;非致癌风险指数均小于1,不存在非致癌风险.采用风险商值(RQ)法对地表水中污染物进行生态风险评价,研究区域内地表水中PAHs和PCBs生态风险总体处于中低风险水平,个别点位存在重度风险的污染物单体,值得引起重视.采用沉积物质量基准法(SQGs)对沉积物中污染物进行生态风险评估,沉积物中PAHs和PCBs均处于较低的生态风险水平. 相似文献
57.
水生生物对三唑磷的物种敏感度分布研究 总被引:1,自引:0,他引:1
针对水环境中日益严重的有机磷农药污染问题,选择广泛使用的三唑磷作为研究对象,利用其对水生生态系统中不同营养层次生物物种的半数效应浓度(median effective concentration, EC50),建立了基于对数-逻辑斯蒂分布的水生生物物种敏感度分布(species sensitivity distribution, SSD)模型,并采用概率图和吻合度检验方法对该模型进行了检验和评价.结果表明,水生生物对三唑磷的 SSD 服从对数-逻辑斯蒂分布,其参数为 α=-0.4788±0.2381,β=0.7546±0.1078.基于该 SSD 模型,获得三唑磷的 5% 危害浓度(hazardous concentration for 5% of the species, HC5)值为 1.992×10-3 mg/L,并推导出三唑磷的最大浓度基准值(criteria maximum concentration, CMC)值为 9.96×10-4 mg/L.对 HC5、CMC 与单一物种的安全浓度的比较研究指出,基于 SSD 方法制定环境质量标准更为严格,也更接近于真实的生态环境.另外,根据渤海莱州湾海域中三唑磷的监测数据,预测了其对物种的潜在影响比例(potentially affected fraction, PAF)为 0.36%,对该水域生态环境的影响处于较低风险水平. 相似文献
58.
以20种微量有机污染物为目标物,针对北京市2个再生水厂的不同工艺,系统地考察了污水再生水中目标化合物的去除效果,并采用重组酵母雌激素活性筛检法(YES法)对再生水中雌激素活性进行评价.结果表明,超滤(UF)+臭氧(O3)氧化处理工艺可有效地去除微量有机污染物,出水中雌二醇当量浓度(EEQ)低于YES法检出范围.A2/O+膜生物反应器(MBR)+反渗透(RO)处理工艺对微量有机污染物有很高的去除能力,出水中可检测出的目标化合物较少.2种工艺均可降低再生水的环境风险,保障其使用安全. 相似文献
59.
海河流域北部地区河流沉积物重金属的生态风险评价 总被引:5,自引:4,他引:5
以海河流域北部地区主要河流为研究对象,采用Hkanson潜在生态风险指数法,根据39个采样点评价了河流沉积物重金属的潜在生态风险程度.结果表明,以中国大陆沉积物重金属背景值作为参考值,研究区内除Pb含量接近背景值外,Cu、Zn、Cd和Cr含量均超出了背景参考值.基于单项重金属的潜在生态风险指数,研究区内采样点Cu、Pb、Zn和Cr的风险等级属于"轻微",Cd则有不同程度的污染,各重金属污染等级排列顺序为Cd>Pb>Cu>Cr>Zn.基于多种重金属的潜在风险指数,32个采样点属于"轻微"等级,5个采样点属于"中等"等级,2个采样点属于"很强"等级.风险较高的河流为北京汤河、大石河和保定拒马河,表明这些河流是需要加强控制的重点地区. 相似文献
60.
太湖底泥疏浚的水环境质量风险性分析 总被引:12,自引:2,他引:12
采用基于因子分析的主成分分析法将五里湖的16个水质参数概括为5个主成分,研究了各主成分以及其综合主成分在疏浚前后的变化,并以此为依据就底泥疏浚对水环境质量的影响进行了评价.结果表明,疏浚过程中,五里湖疏浚区的综合主成分得分最高,为1.15,水质综合排名在最后,水体色度和污染指数(F1)也达到最高值5.0;同时对照区综合主成分得分以及水体污染和色度指数(F1,F2)也相应升高,水质质量明显下降;这说明疏浚运作具有促进表层沉积物发生再悬浮和扩散作用,以及沉积物中内源性营养盐和重金属离子的释放作用.采用Monte Carlo随机采样法,利用平衡分配模型模拟和预测了疏浚过程中悬浮沉积物中重金属离子释放的阈值,结果表明疏浚过程中大部分重金属离子由悬浮沉积物向水体中释放的风险性较高,可信度达到90%以上,尤其是重金属离子Ni2+以及非金属污染物As释放的风险性较大,其可能的释放量分别分布在各自地表水环境质量标准EQS的28.6%~+∞之间和34%~+∞之间,说明底泥疏浚具有导致五里湖水体环境质量短期恶化的风险.此外,Monte Carlo随机采样分析方法应用也许可为湖泊底泥疏浚生态风险评价提供一条新的途径. 相似文献