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81.
82.
从垂直气液两相流运行动力学角度,提出深井工艺设计中空气量的计算方法。经验证,用此法计算出的风量、风压,可以在工程设计中较合理地选用空压机或鼓风机。 相似文献
83.
Nahanni National Park Reserve is located at southwestern NWT-Yukon border. One of the first UNESCO World Heritage sites, Nahanni lies within Taiga Cordillera and Taiga Shield Ecozones. Base and precious metal mining occurred upstream of Nahanni prior to park establishment. Nahanni waters, sediments, fish, and caribou have naturally elevated metals levels. Baseline water, sediment and fish tissue quality data were collected and analyzed throughout Nahanni during 1988–91 and 1992–97. These two programs characterized how aquatic quality variables are naturally varying in space and time, affected by geology, stream flow, seasonality, and extreme meteorological and geological events. Possible anthropogenic causes of aquatic quality change were examined. Measured values were compared to existing Guidelines and site-specific objectives were established. 相似文献
84.
黄浦江水系水质变化及原因分析 总被引:1,自引:0,他引:1
根据1986—2010年的水质监测数据,研究了黄浦江水系水质变化,并对影响水质的主要因素进行了探讨。结果表明,近25年的黄浦江水系水质变化基本可分为3个阶段:1986—1996年,上海市的畜牧业高速发展,生活污水量逐年上升,工业废水量较大而处理率低,水环境压力加大,水质持续恶化;1996—2002年,上游来水水质、生活污水量和畜牧业污染量均基本稳定,为水质改善创造必要条件,随着工业废水量的下降及废水处理能力的加强,水质持续改善;2002—2010年,上游来水水质在2002—2004年明显恶化,生活污水量再次进入快速上升期,加大了水环境改善的难度,水质改善趋势放缓并渐趋稳定。 相似文献
85.
黄岛电厂温排水对大型底栖生物群落的影响 总被引:2,自引:0,他引:2
以黄岛电厂温排水邻近海域为研究对象,2010年9月调查了电厂温排水对该海域大型底栖生物群落结构的影响。在9个站点共采集到大型底栖生物76种,平均生物量5.79 g/m2,平均密度830 m-2。利用Bray-Curtis相似性聚类对各样本大型底栖生物分析得出,调查区域可划分为4个群落。各样点Shannon-Wiener多样性指数在2.42~4.25之间,平均指数为3.67,其中靠近温排水区域站位的生物多样性呈现下降的趋势。丰度生物量比较(Abundance/biomass comparison, ABC)曲线分析结果显示,靠近排水口处的大型底栖生物群落受到一定程度的干扰。冗余分析( RDA)结果表明,水温是影响底栖生物群落变化的最主要因子,对调查区域大型底栖生物群落变化的解释量达到60.5%,影响范围为排水口附近温升在3℃以上的区域。 相似文献
86.
系统总结了当前大气污染物排放调查监测的主要方法及其在全球、区域、局地等不同尺度的典型应用,分析了地面监测、模型模拟与遥感反演3种方法受排放源多样、成分复杂、时空变异显著等因素影响,在尺度效应、成分解析等方面存在的问题。从优化监测方法、改进监测模式、融合监测技术等角度,提出了构建现代化大气污染物排放调查监测网络、开展污染物在不同排放阶段的变化解析研究及在不同圈层间的迁移全过程研究等建议。 相似文献
87.
Bottled water may not be safer, or healthier, than tap water. The present studies have proved that styrene and some other aromatic compounds leach continuously from polystyrene (PS) bottles used locally for packaging. Water sapmles in contact with PS were extracted by a preconcentration technique called as "purge and trap" and analysed by gas chromatograph-mass spectrometer (GC/MS). Eleven aromatic compounds were identified in these studies. Maximum concentration of styrene in PS bottles was 29.5 μg/L. Apart from styrene, ethyl benzene, toluene and benzene were also quantified but their concentrations were much less than WHO guide line values. All other compounds were in traces. Quality of plastic and storage time were the major factor in leaching of styrene. Concentration of styrene was increased to 69.53 μg/L after one-year storage. In Styrofoam and PS cups studies, hot water was found to be contaminated with styrene and other aromatic compounds. It was observed that temperature played a major role in the leaching of styrene monomer from Styrofoam cups. Paper cups were found to be safe for hot drinks. 相似文献
88.
Masayuki Tanabe Atsumi Miyake 《Journal of Loss Prevention in the Process Industries》2011,24(4):383-390
The functional safety requirement is widely applied in the process plant industry in accordance with the international standards, such as IEC and ISA. The requirement is defined as safety integrity level (SIL) based on the risk reduction concept for protection layers, from original process risk to tolerable risk level. Although the standards specify both, the Prevention System and the Emergency System, as level of protection layers, the standards specify in detail only the use of the Prevention System (i.e., Safety Instrumented System (SIS)). The safety integrity level is not commonly allocated to the Emergency System (e.g., Fire and Gas System, Emergency Shutdown System and Emergency Depressuring System). This is because the required risk reduction can be normally achieved by only the Prevention System (i.e., SIS and Pressure Safety Valve (PSV)). Further, the risk reduction level for the Emergency System is very difficult to be quantified by the actual SIL application (i.e., evaluated based on the single accident scenario, such as an accident from process control deviation), since the escalation scenarios after Loss of Containment (LOC) greatly vary depending on the plant design and equipment. Consequently, there are no clear criteria for evaluating the Emergency System design. This paper aims to provide the functional safety requirement (i.e., required risk reduction level based on IEC 61508 and 61511) as design criteria for the Emergency System.In order to provide clear criteria for the Emergency System evaluation, a risk reduction concept integrated with public’s perception of acceptable risk criteria is proposed and is applied to identify the required safety integrity level for the Emergency System design. Further, to verify the safety integrity levels for the Emergency Systems, the probabilistic model of the Emergency Systems was established considering each Emergency System (e.g., Fire and Gas System, Emergency Shutdown System and Emergency Depressuring System) relation as the Overall Emergency System. This is because the Overall Emergency System can achieve its goal by the combined action of each individual system, including inherent safe design, such as separation distance.The proposed approach applicability was verified by conducting a case study using actual onshore Liquefied Natural Gas Plant data. Further, the design criteria for Emergency Systems for LNG plants are also evaluated by sensitivity analysis. 相似文献
89.
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