高含硫化氢井场公众疏散能力分析方法研究

我国含硫气田存在含硫量高、周边人口稠密、地形复杂等危险因素,如何保证含硫气田周边居民安全疏散成为一个重要的急需解决的问题.针对高含硫气田开发过程面临的公众疏散能力问题,采用毒性负荷判别法作为疏散能力评估的准则,提出一套分析流程,并给出相应的改进措施,形成一整套的复杂地形下高含硫化氢井场公众安全疏散能力分析方法;通过对本方法在现场实际中的应用,在理论和实例分析基础上,发现对高含硫气田井场进行疏散能力评估是可行且非常必要的.     

Accounting for the effect of concentration fluctuations on toxic load for gaseous releases of carbon dioxide

In Great Britain, advice on land-use planning decisions in the vicinity of major hazard sites and pipelines is provided to Local Planning Authorities by the Health and Safety Executive (HSE), based on quantified risk assessments of the risks to the public in the event of an accidental release. For potential exposures to toxic substances, the hazard and risk is estimated by HSE on the basis of a “toxic load”. For carbon dioxide (CO₂), this is calculated from the time-integral of the gas concentration to the power eight. As a consequence of this highly non-linear dependence of the toxic load on the concentration, turbulent concentration fluctuations that occur naturally in jets or plumes of CO₂ may have a significant effect on the calculated hazard ranges. Most dispersion models used for QRA only provide estimates of the time- or ensemble-averaged concentrations. If only mean concentrations are used to calculate the toxic load, and the effects of concentration fluctuations are ignored, there is a danger that toxic loads and hence hazard ranges will be significantly under-estimated.This paper explores a simple and pragmatic modification to the calculation procedure for CO₂ toxic load calculations. It involves the assumption that the concentration fluctuates by a factor of two with a prescribed square-wave variation over time. To assess the validity of this methodology, two simple characteristic flows are analysed: the free jet and the dense plume (or gravity current). In the former case, an empirical model is used to show that the factor-of-two approach provides conservative estimates of the hazard range. In the latter case, a survey of the literature indicates that there is at present insufficient information to come to any definite conclusions.Recommendations are provided for future work to investigate the concentration fluctuation behaviour in dense CO₂ plumes. This includes further analysis of existing dense gas dispersion data, measurements of concentration fluctuations in ongoing large-scale CO₂ release experiments, and numerical simulations.     

救生舱高温环境的传热研究

为提高救生舱热防护能力,延长救援时间,在空载状态下救生舱热载荷研究的基础上,提出救援状态下救生舱外部传热热负荷的量化方法。已知救援状态下救生舱内、外温度随时间变化曲线,拟合温度函数。依据温度变化特点划分区间,积分求取各区间上温度平均值,计算温差,由传热方程计算救援状态下救生舱的热载荷。以某型号救生舱载人综合防护试验为例,根据模拟灾变环境的温度变化特点,运用该方法计算最高温度与常态温度下外部高温空气向舱体及其内部空间传热的热载荷,得到救生舱的总热负荷,外部传热最大传热功率及救生舱热载荷负荷范围。     

洱海北部2种典型种植制度下农田氮污染负荷研究

洱海北部区域农村面源污染是富营养化初期湖泊——洱海氮磷负荷的主要来源.以洱海北部2种典型种植制度下的农田为研究对象,采用现场调查与采样分析相结合的方法,定量分析氮的输入通量(农作物施肥、大气降水降尘、灌水和生物固氮)及输出通量(农田收获物和生物脱氮),并计算其对水环境产生的氮污染负荷净排放量(包括农田地表径流和地下渗透流).结果表明,在水稻-蚕豆种植制度下,农田为环境友好型,基本不向水环境排放氮负荷,净排放量为-30.73 kg·hm-2·a-1,主要氮输入通量为生物固氮(占43.3％),其次为有机肥(占35.O％),且输出通量主要为农作物吸收(占98.5％).在水稻-大蒜种植制度下,农田为环境污染型,净排放量为306.75 kg·hm-2·a-1,主要氮输入通量为肥料(占84.7％),其中化肥占62.1％,而输出通量中水环境排放占45.4％.水稻-大蒜种植制度亟需采取合理施肥和提高肥料利用率等农田污染防治对策.     

Control of chlorinated aromatic compounds from a municipal solid waste incinerator using limestone addition

In this study, limestone powder was directly added to synthetic MSW, which was fed into a small‐scale fluidized bed incinerator. The concentration of CBzs and CPs in the flue gas were measured before and after a secondary combustion air injection. Finally, the PCDDs and PCDFs concentrations were also measured in the flue gas after the secondary combustion zone. The CaCO₃ added to synthetic MSW not only controls HCl in the flue gas, but suppresses the formation of chlorinated aromatic compounds like CBzs, CPs, PCDDs, and PCDFs. The main mechanisms to control the formation of chlorinated aromatic compounds was more likely related to the suppression of catalytic capability of flyash than the HCl reduction in the flue gas. However, the NO concentration was increased by catalytic reaction of limestone in the fluidized bed.     

不同源类型农业非点源负荷特征研究——以新田小流域为例

以珠江三角洲北部新田小流域为研究对象,采用源类型法,在流域范围内建立林地、果园、旱地和水田四个全封闭的农业用地单元,并对四个单元出口处的径流量进行同步采样,分析COD、BOD、氨氮、总氮和总磷等污染物的负荷特征.结果表明:(1)流域地表水存在着明显非点源污染现象,不同源类型,地表径流的污染程度不同.(2)不同源类型农业非点源污染负荷强度不同,其中水田、旱地单位面积非点源负荷强度较大,果园、林地各项污染物的负荷强度相对最小.受地表扰动、施肥等人类活动影响,流域内水田、旱地是农业非点源污染发生的关键源区.(3)流域范围内,不同源类型农业非点源负荷总量不同,其中,果园各项污染物非点源负荷总量最大,其次是林地,水田、旱地非点源负荷输出总量较小,流域范围内,源面积成为影响非点源负荷总量的主要因素.(4)相应的非点源污染治理不仅是关键源区,同时应关注大面积流失区.     

组合型生态浮床对上覆水和沉积物之间氮磷的影响

在天鹅湖水体中构建以水生植物和陆生喜水植物为实验植物,浮法控制器、水循环增氧系统和造浪-输送系统为辅助设备的组合型生态浮床.组合型生态浮床运行期间改变了水体的理化环境,影响了上覆水-沉积物中氮磷形态的迁移转化,跟踪监测在组合型生态浮床影响下上覆水和沉积物TN、NH4+-N和TP含量的浓度变化规律,探讨了在组合型生态浮床作用下,DO、Eh、pH对上覆水和沉积物中营养盐的影响,以及上覆水和沉积物中氮磷之间以及和各环境因子之间的相互关系.结果表明,实验期间上覆水中TN、NH4+-N和TP的去除率分别达到61.92%、63.09%和80.0%.沉积物中TN和NH4+-N的去除率分别达到23.79%和37.04%,沉积物中TP含量上升了43.71%.组合型生态浮床对上覆水环境因子如DO、Eh、pH等产生不同程度的影响,处理区上覆水中DO和Eh均高于对照区,DO由原来的8.7～8.9 mg·L-1上升到9.3～10.4 mg·L-1,Eh由原来的163～178 mV上升到191～198 mV,通过提高上覆水中DO和Eh有效抑制沉积物磷的释放并促进沉积物对上覆水中磷的吸附.pH的波动性较小,维持在7.51～8.32之间,并未促进沉积物磷释放.上覆水中TN、TP和NH4+-N以及与沉积物中的TN、NH4+-N之间呈极显著正相关,与沉积物中的TP极显著负相关;pH与上覆水和沉积物中的TN、TP和NH4+-N都无相关性;上覆水中的DO与Eh显著正相关,与沉积物中的TP显著负相关.     

河冰对桥墩作用的冰荷载计算方法(Ⅰ)——河冰的力学性能试验

通过对松花江河冰的物理力学性能试验和松花江公路大桥桥墩的流冰动压力测量、桥面的脉动测量 ,依据国内外对冰 -结构相互作用的分析 ,提出了适合我国黑龙江冰情特点的春季流冰冰荷载的计算方法。     

A GAME-THEORETIC APPROACH TO ACID RAIN ABATEMENT: CONFLICT ANALYSIS OF ENVIRONMENTAL LOAD ALLOCATION1

ABSTRACT: The detrimental impacts of acid rain have become widely publicized, but effective and equitable methods to mitigate the acid rain problem remain to be found. This paper focuses on conflicts involved in allocation of the total emission loads to be reduced to respective pollution sources of acid rain, and proposes a game-theory approach to the resolution of the conflict. With an example abstracted from a hypothetical case study in the United States of America and Canada, a systematic analysis is performed and policy implications of the results examined to assess the applicability of the proposed model.     

Catalytic decomposition of hydrocarbon into hydrogen and carbon in a spouted-bed reactor as the second-stage reactor of a plastic recycling process

A two-stage process for the chemical recycling of plastics is proposed. In this process, which consists of two reactors, plastics are converted into hydrogen and carbon. In the first reactor, plastic chips are thermally decomposed into hydrocarbons. In the second reactor, the hydrocarbons formed in the first reactor are catalytically decomposed into carbon and hydrogen. In this study, in order to obtain basic data for the second reactor, propene was catalytically decomposed in a laboratory-scale spouted-bed reactor (600mm high, 21.6mm internal diameter, made of SUS304). The effect of the type of spouting medium used on the decomposition behavior of propene was investigated using four types of spouting medium (nickel-plated -alumina, palladium-plated -alumina, nickel-impregnated -alumina, and -alumina). The nickel-impregnated -alumina gave the best propene conversion and hydrogen yield.