应用改进密切值法进行地表水环境综合评价

针对密切值法应用中的实际问题,引入目标差值率和虚拟优点、劣点的概念,对密切值法进行了改进.将改进后的密切值法应用于地表水环境综合评价中,经实例分析表明,该方法概念清晰、计算简便实用,且从评价结果可获许多潜在的信息,是开展地表水流域水环境综合评价的一种有效的方法.     

含菌气溶胶扩散对人群的潜在影响风险

为分析生物气溶胶释放对人群潜在影响风险的情况,利用CALPUFF模型定量模拟了2019年7月24~8月20日中牧兰州生物药厂含菌气溶胶扩散、浓度空间分布、对人群潜在健康风险,并结合公开报道的检测数据开展验证.结果显示：生物药厂的含菌气溶胶排放源附近高值区主要集中于厂区四周,影响范围主要以厂区为中心,并向四周逐渐扩散;检测结果中兰州兽研所1#,兰州大学2#地区健康风险比例41.49：1,在模拟的相对风险大小的误差区间（36.15±8.48）范围内,说明本研究含菌气溶胶对人群潜在影响风险的模拟结果可信.     

某石油炼制企业VOCs排放源强反演研究

选取我国北方某石油炼制企业为研究对象,针对其挥发性有机物(VOCs)排放,于春季3月开展了厂界周边大气VOCs环境浓度监测,并利用ISCST-3空气质量模型反推出该企业VOCs排放源强.监测结果表明,厂外上风向背景点与下风向受体点TVOCs浓度平均值分别为28.6×10-9和88.3×10-9,且2个区域VOCs还存在化学组分特征差异,背景点以乙烷、丙烷、乙烯为主,而受体点化学组分中丙烯、异丁烷、丁烷、异戊烷、戊烷的体积浓度百分比显著上升,说明该炼油厂VOCs排放体量大,对局地环境影响显著.扣除背景点VOCs,获得了该炼油厂VOCs排放化学成分谱,其主要成分体积浓度百分比:乙烷(23.4%)、丙烷(11.8%)、丁烷(10.4%)、异丁烷(9.0%)、戊烷(5.3%)、异戊烷(6.4%)、丙烯(11.5%),成分谱特征与国内相关文献相似.ISCST-3模型反演结果显示,该炼油厂TVOCs年排放量平均值为(2201.6±1011.9) t/a,折合排放因子约0.73g VOCs/kg原油.该计算结果偏低,原因可能在于:其一,测试季节为春季,较低的环境温度致使了炼油厂挥发散逸环节的排放低于全年平均水平;其二,ISCST-3模型为扩散模型,未考虑VOCs化合物在局地范围的化学衰减.     

显像管玻壳铅尘污染特性的研究

以石家庄市显像管玻壳厂排放的铅尘为研究对象，通过在该玻壳厂周围土壤布点采样，较系统地研究了铅尘在大气和周围土壤中的迁移和转化规律，研究表明，用高斯模式能成功地预测铅尘在大气中的迁移扩散规律，玻壳厂周围土壤表层铅含量较大值出现在当地年主导风向（SSE，N）下风向，铅在土壤中的分布主要集中在0－20cm的耕作层，在20－40cm深度范围内，铅含量呈下降趋势，最大降幅达50％。     

道路路障对街道峡谷内污染物扩散的影响

采用数值模拟,研究不同风向角α (α=0°、45°、90°)及道路屏障位置(中间单路障和两侧双路障)对街道峡谷内机动车尾气污染物扩散的影响。数值模拟采用标准 k-ε 湍流模型且Sct选择0.3时,计算结果与风洞实验结果较好吻合。结果表明,2种路障布置方式可有效降低人行道内污染物浓度,特别是,当α=45°时,污染物浓度最多可降低46.23%。同时,风向角α对街道峡谷内污染物扩散影响较大。当 α=90°时,空气流通不良使得污染程度最为严重,且污染集中在背风侧近地面。单路障比双路障布置对污染物扩散影响更大,前者使污染物主要集中在街道中心背风侧,其他位置浓度明显降低;双路障时仅在一定范围内改善人行道内空气品质,但对街道整体污染物分布影响不大。     

2 000 m超深水水下分离器泄漏油气扩散特性研究

深水水下分离器服役过程中由于腐蚀、地质灾害和环境高压作用,存在失效泄漏风险。针对2 000 m超深水水下分离器可能存在的失效泄漏问题,基于计算流体动力学CFD方法,建立分离器失效泄漏后果数值仿真分析模型,对分离器泄漏场景进行模拟与分析,研究2 000 m水深条件下分离器泄漏油气扩散规律,并考虑不同泄漏位置对油气扩散行为的影响。结果表明:水下分离器泄漏包括压力扩散和自由扩散两个阶段,压力扩散阶段历时极短,自由扩散阶段耗时较长;泄漏口位置对泄漏结果有较为明显的影响,分离器上部泄漏,油气全部溢出,分离器中下部泄漏,大部分油气保留于分离器内部,最终形成分明的油气水界面;分离器内部压力随时间迅速上升,t=0.25 s左右接近于20 MPa,后期在20 MPa左右呈极微小波动,泄漏速率随分离器内部压力增大迅速减小,达到最低点之后,呈微小波动状变化。     

Numerical investigation of powder aerosolization in a mining rock dust dispersion chamber

We have conducted numerical simulations of dust dispersion within the NIOSH Rock Dust Dispersion Chamber. The apparatus consists of a low-speed background ventilation flow down a long box in which is placed a tray containing a rock dust powder. A nozzle upstream of the tray introduces a short pulse of a turbulent horizontal jet flow just above the powder surface. We have utilized an incompressible Reynolds-Averaged Navier-Stokes k-ω model for the turbulent flow; particles are incorporated within a one-way Euler-Lagrangian formalism. The Rock Dust Dispersion Chamber ventilation flow exhibits a recirculation zone just above the powder-containing tray. Aerosolization proceeds via the interplay of the jet pulse flow with the background recirculation flow. The air flow is not well-mixed. The aerosolized dust is convected as a concentration cloud downstream towards the detection zone. For larger particles, gravitational settling depletes the convected cloud, so the instrument behaves as a horizontal elutriator. The instrument is robust with respect to misalignment of the jet nozzle. However, reduced streamwise drift velocity allows mixing to disperse the optically detected dust cloud concentration pulse. Our large particle simulation results compare favorably with published experimental results for large, polydisperse calcium carbonate rock dust.     

基于Monte-Carlo方法的长输管道气体扩散模拟研究

目前气体扩散模拟研究多采用流体力学的计算方法,分析气体扩散过程中的动力学特性.有限体积、有限元等方法都需要对事故区域整体进行网格划分,计算过程效率无法满足长输管道事故应急跨区域、多气象以及复杂地形的要求.Monte-Carlo方法利用RAMS预测的平均风场,模拟有限气体粒子在风场中的随机行走特性,有效地弥补了计算效率与网格精度冲突所导致的模拟性能下降的缺点.通过HAVEGE方法收集计算的硬件信息熵形成随机源,修正了以往伪随机数问题,增强了Monte-Carlo方法的计算精度.结果表明Monte-Carlo气体扩散模拟研究方法满足了长输管道事故灾害应急决策的需要.     

Validation of discharge and atmospheric dispersion for unpressurised and pressurised carbon dioxide releases

This paper discusses the validation of discharge and subsequent atmospheric dispersion for both unpressurised and pressurised carbon dioxide releases using the consequence modelling package Phast.The paper first summarises the validation of the Phast dispersion model (UDM) for unpressurised releases. This includes heavy gas dispersion from either a ground-level line source (McQuaid wind-tunnel experiments) or an area source (Kit-Fox field experiments). For the McQuaid experiments minor modifications of the UDM were made to support line sources. For the Kit Fox experiments steady-state and 20-s finite-duration releases were simulated for both neutral and stable conditions. Most accurate predictions of the concentrations for finite duration releases were obtained using the UDM Finite Duration Correction method.Using experiments funded by BP and Shell and made available via DNV's CO2PIPETRANS JIP, the paper secondly summarises the validation of the Phast discharge and dispersion models for pressurised CO₂ releases. This modelling accounted for the possible presence of the solid CO₂ phase following expansion to atmospheric pressure. These experiments included both high-pressure steady-state and time-varying cold releases (liquid storage) and high-pressure time-varying supercritical hot releases. Both the flow rate and the concentrations were found to be predicted accurately.The above validation was carried out with no fitting whatsoever of the Phast extended discharge and dispersion models.