内河非溶解性危险化学品泄漏扩散过程影响因素

针对内河中非挥发性危险化学品（危化品）运输船舶的泄漏扩散问题,建立了一种通用数值模拟方法,研究了内河非溶解性危化品泄漏扩散过程的影响因素。结果表明：危化品的密度和黏度对内河危化品泄漏扩散过程的影响相对较小,而水流速率和危化品泄漏速率对危化品泄漏扩散过程的影响较大;水流速率对危化品泄漏扩散过程的影响主要表现在泄漏扩散范围（尤其是泄漏区域长度）方面,而危化品泄漏速率的影响主要表现在泄漏区域宽度、微团数量以及最大微团面积方面。建议应针对丰水期危化品大泄漏量的情况展开监管,并将其作为内河危化品泄漏应急工作的重点。     

基于“情景-应对”模式的危险化学品泄漏应急决策系统的构建

危险化学品泄漏事故严重威胁到社会和环境安全。危化品泄漏事故发生后,快速找到泄漏源并及时采取应对措施是面临的主要任务。构建了基于一般风场的危化品泄漏事故情景库,利用Coyote实验验证了情景库在危化品泄漏事故中反演溯源的效果,据此建立了基于“情景-应对”模式的危险化学品泄漏应急决策系统,并应用于氯气泄漏事故的应急救援中。该方法具有使用方便、决策速度快、救援效率高等特点,对危化品泄漏事故的应急决策具有重要的现实意义。     

油田储油罐非甲烷总挥发实验及仿真模拟

针对油田单井拉油罐非密封生产带来的油气泄漏问题,建立小型原油储油罐挥发损耗实验模拟平台,通过气相色谱法探究各因素对其损耗的影响,利用Fluent仿真软件模拟储油罐的泄漏扩散。结果表明:储液温度和有无风环境对储油罐非甲烷总烃(NMHC)挥发影响较大,储液高度和环境温度对其影响较小;仿真模拟无风环境下,储油罐泄漏口短时间内存在油气积聚现象;有风环境下,当风速为1 m/s,油气积聚不明显;随风速增大,扩散浓度场面积不断增大,油品损耗量增大,在风速为5 m/s的环境下,扩散300 s时的浓度场面积相比扩散200 s时较小,但泄漏口处的油气积聚面积增大。     

氯气泄漏扩散过程及后果评价的研究现状分析

综述了氯气泄漏扩散过程及后果评价的研究成果。从现场试验、实验室模拟和数学模拟三方面分析了氯气泄漏扩散各研究方法的优势和局限性。强调了氯气泄漏扩散后果评价的必要性。指出:必须针对中国特有的一些重气扩散建立专属知识产权的数学模型;不同层次数学模型的精度皆有待于进一步提高;需加强基于特定数学模型的全过程统一界面模拟程序的开发。     

CO2地质封存中单井源泄漏风险的

通过模拟某废弃井CO₂泄漏事故,对CO₂泄漏事故进行风险评估。利用高斯模型得到不同大气条件下泄漏事故的影响范围及CO₂浓度分布特征,并采用信息扩散法对模拟结果进行评价。研究结果可为利用钻井封存CO₂项目的安全规划及风险防控提供理论依据。     

环境风险评价中氯气泄漏扩散的计算

根据HJ/T169-2004((建设项目环境风险评价技术导则>(简称<导则>),对某化工厂使用的液氯钢瓶的事故源进行分析.采用<导则>推荐的Cox和Carpenter稠密气体扩散模型,在氯气泄漏的初期,将其作为重气泄漏扩散进行计算,得到重气云团温度、半径、卷入空气质量和质量浓度随扩散时间的变化关系.计算结果与非重气扩散高斯模式的计算结果有较大差异.因此,对涉及氯气的项目进行环境风险评价时,应重视氯气作为重气泄漏扩散的环节.     

典型液氯泄漏危害的ALOHA软件估算

以瞬时泄漏和连续泄漏两种典型液氯泄漏事故为例,分别运用ALOHA软件和公式计算两种方法对液氯泄漏危害进行量化评估。估算结果表明:ALOHA软件对泄漏毒物的危害区域和敏感点毒物浓度的预测结果均具有良好的精度;软件模拟与公式计算的结果对于液氯瞬时泄漏的相对误差仅为7%,对于连续泄漏的相对误差为8%,二者均在可接受范围内。ALOHA软件计算过程简单、表达形象直观,在泄漏事故应急中具实用性。     

政府力推危化企业搬迁改造

正天津"8·12"事故后,各地危化品企业搬迁改造大大提速。截至2015年11月底,工信部、国家发改委等共征集危化品搬迁改造项目1 350个、总投资6 000多亿元。目前,已从各地上报项目中遴选了3批共238个项目,纳入专项建设基金支持范围,涉及总投资2 750亿元。危化品企业搬迁的主要原因是城市规划变更以及城镇化快速发展导致安全     

矿山粉尘分布及扩散规律研究进展

对采矿粉尘分布及扩散规律的实验研究和数值模拟研究进展进行综述,研究表明实验结果与模拟结果基本一致,但是模拟可以给出更加详尽的粉尘浓度、分布和扩散规律数据,为有针对性地采取防尘措施、选择除尘技术提供科学的理论依据,并对今后的发展方向进行了展望。     

滨海电站温排水数值模拟

针对滨海火（核）电站温排水海洋影响预测及评价的迫切需要,建立了二阶Osher格式水流——温度模型,采用“干湿单元水力模型”处理滨海电站所处海域复杂的计算边界,并结合某大型火电站温排水的数值模拟,显示了该模型正确模拟滨海电站温排水扩散过程的能力,为海洋环境影响评价提供可靠的技术资料.     

危险化学品安全管理现状及对策

分析了我国危险化学品的安全管理形势、现状与评价方法，提出了加强危险化学品安全管理的若干对策。     

Diffusion coefficients of organics in high density polyethylene (HDPE)

Only limited data are available on the diffusion of volatile organic solvents through flexible membrane liners (FMLs) used for lining impoundments and landfills. To expand this database, a rapid, inexpensive method is needed to measure the diffusion coefficients of volatile organic solvents through FML materials. An absorption method has been developed to determine the diffusion coefficients of volatile organic solvents through FML materials. The method is based on the depletion of an organic compound from an aqueous solution due to absorption by a submerged sample of FML. A numerical solution of Fick's second law of diffusion was used to develop a graph which can be used to determine the diffusion coefficient from the time dependent concentration data. The diffusion coefficients obtained from the absorption tests were validated by comparing them with coefficients determined using a two chamber diffusion cell. The diffusion coefficients determined for toluene and xylene in high density polyethylene (HDPE) were 5.1 × 10⁻⁹ cm²s⁻¹ and 1.0 × 10⁻⁹ cm²s⁻¹ by the two methods, respectively. The data indicate that the coefficient of distribution (K_d) between the FML and the organic solution, a value which is needed to calculate the diffusion coefficient from the data, can be estimated from the log of the octanol-water partition coefficient (K_ow), a commonly measured and reported value for many chemicals.     

An evaluation of the performance of multiple passive diffusion devices for indoor air sampling of VOCs

The United States Environmental Protection Agency is considering recommending longer‐term sampling to achieve more accurate time‐weighted‐average detections for indoor air monitoring of volatile organic chemicals. The purpose of the research presented herein was to compare longer sampling times using passive diffusion samplers to the results from shorter‐term testing periods using sorbent tubes and low‐flow pumps (US EPA Method TO‐17) at great frequency for trichloroethene (TCE) in indoor air. A controlled release of TCE in a large room allowed for over two‐orders‐of‐magnitude daily concentration variability over the course of the two‐week monitoring event. The daily concentration measurements by US EPA Method TO‐17 and the passive diffusion samplers were performed in triplicate and had excellent reproducibility. The results of daily tests were averaged and compared with four passive diffusion devices exposed to indoor air for three, seven, ten, and fourteen days in accordance with ASTM D6196‐02. A specific uptake rate for each of the passive devices at the four different time intervals and the statistical significance of the time‐varying uptake rates were evaluated. The performance of each passive diffusion device was determined using a statistical performance criterion. The average concentration for all of the exposure periods could be reliably predicted using the established uptake rates for two of the four passive devices. © 2009 Wiley Periodicals, Inc.     

Application of an Adapted Version of MT3DMS for Modeling Back‐Diffusion Remediation Timeframes

Simulation of back‐diffusion remediation timeframe for thin silt/clay layers, or when contaminant degradation is occurring, typically requires the use of a numerical model. Given the centimeter‐scale vertical grid spacing required to represent diffusion‐dominated transport, simulation of back‐diffusion in a 3‐D model may be computationally prohibitive. Use of a local 1‐D model domain approach for simulating back‐diffusion is demonstrated to have advantages but is limited to only some applications. Incorporation of a local domain approach for simulating back‐diffusion in a new model, In Situ Remediation‐MT3DMS (ISR‐MT3DMS) is validated based on a benchmark with MT3DMS and comparisons with a highly discretized finite difference numerical model. The approach used to estimate the vertical hydrodynamic dispersion coefficient is shown to have a significant influence on the simulated flux into and out of silt/clay layers in early time periods. Previously documented back‐diffusion at a Florida site is modeled for the purpose of evaluating the sensitivity of the back‐diffusion controlled remediation timeframe to various site characteristics. A base case simulation with a clay lens having a thickness of 0.2 m and a length of 100 m indicates that even after 99.96 percent aqueous TCE removal from the clay lens, the down‐gradient concentrations still exceed the MCL in groundwater monitoring wells. This shows that partial mass reduction from a NAPL source zone via in situ treatment may have little benefit for the long‐term management of contaminated sites, given that back‐diffusion will sustain a groundwater plume for a long period of time. Back‐diffusion model input parameters that have the greatest influence on remediation timeframe and thus may warrant more attention during field investigations, include the thickness of silt/clay lenses, retardation coefficient representing sorbed mass in silt/clay, and the groundwater velocity in adjacent higher permeability zones. Therefore, pump‐and‐treat systems implemented for the purpose of providing containment may have an additional benefit of reducing back‐diffusion remediation timeframe due to enhanced transverse advective fluxes at the sand/clay interface. Remediation timeframes are also moderately sensitive to the length of the silt/clay layers and transverse vertical dispersivity, but are less sensitive to degradation rates within silt/clay, contaminant solubility, contact time, tortuosity coefficient, and monitoring well‐screen length for the scenarios examined. ©2015 Wiley Periodicals, Inc.     

基于参数化模型优化的喷氨格栅设计方法研究

从喷氨格栅工程设计要求出发,结合数值模拟分析、代理模型技术以及优化设计方法,提出了一套基于参数化模型优化的喷氨格栅设计方法和流程。该方法从工程设计要求的分析入手,根据喷氨格栅几何参数对喷氨特性的影响特点和规律,建立参数化设计数学模型,并通过优化计算最终获得喷氨格栅的最优设计。另外,通过实例计算验证了该设计方法在SCR脱硝系统喷氨格栅设计中的适用性。