实时尾气检测系统OEM的应用

机动车尾气排放实时检测系统OEM是基于车辆实际行驶路况的新型车载尾气检测系统。该系统突破了传统的定点尾气收集数据的局限性，能够方便快捷地获得不同路段、不同车型、不同时段的以秒为单位的尾气排放数据以及包括速度和加速度在内的瞬间车辆行驶数据。文中对OEM系统的基本原理和方法进行了简单的介绍，并给出了应用该系统在北京市交通网络测试尾气的一些初始结果。     

船舶柴油机NOx后处理技术的进展

根据国内外的降低NOx排放方面最新的成果和科研动态，主要介绍了当前正在研究或者已经应用于实际的有效降低柴油机NOx排放的技术措施，并分析了各种技术方法的特点和在实际应用过程中面临的问题。     

沈大高速公路沿线气象因子特征研究

选用沈大高速公路沿线 7个气象台站 195 5～ 1995年的累年气象要素值 ,通过对影响高速公路运行和车辆尾气污染物排放、扩散相关的气象因子分析 ,为今后的高速公路建设和沈大高速公路管理 ,提供较科学的依据。     

污染物零排放的化石燃料燃烧系统

介绍了熔融盐循环热载体无烟燃烧技术(nonflame combustion technology usingthermal cyclic carrier of molten salt,简称NFCT).利用沉淀法制备了Fe2O3粉末,并通过机械法加工成氧载体.XRD分析表明所制备的Fe2O3粉末为单一的α-Fe2O3相在固定床反应器中表征了氧载体得失晶格氧的过程,随循环次数的增多,氧载体被CH4还原的速率会有所增加,氧载体在CH4和空气气氛中得失晶格氧是可逆过程,反应后,氧载体内部形成了蜂窝状结构.氧载体的转化度最大为82%,占氧载体总质量18%的晶格氧可以用来氧化CH4.在熔融盐反应器中用CH4作为燃料和所制备的氧载体进行了燃料燃烧和氧载体复原的实验研究在燃料燃烧反应的开始阶段,CH4大部分被氧化成了CO2,CO2的体积分数最高可以达到85%,随着反应时间的增加,氧载体的氧化能力下降,不完全氧化产物CO和未反应的CH4的体积分数逐渐升高,3000s时,CO2的体积分数只有50%在氧载体恢复晶格氧的过程中,在1500s以前,空气中的O2都被氧载体所吸收,1500s以后,该过程排出气体中的O2体积分数开始上升,至2000s气体成分与空气的成分相同.在实验中没有检测出NOx的生成.     

炼油企业中环境因素的识别

简要叙述了环境因素的识别在炼油企业中的必要性和存在的一些问题，并提出改进工作的建议。     

城市交通机动车污染控制研究进展

城市交通机动车污染问题非常复杂，在许多不可控因素，城市交通是一个动态系统，污染物排放量始终处于变化之中，控制城市交通污染，必须严格控制机动车排放，该文介绍了国内外对城市机动车污染控制研究的概况，以及几种城市中污染物扩散的模型，展望了这方面研究前发展趋势，并提出了可持续发展的效能系统设计与管理的新概念。     

Chance-constrained programming (CCP)abatement of SO_2 emission for acid deposition control in Liuzhou City

A deterministic linear programming model which optimizes the abatement of each SO2 emission source, is extended into a CCP form by introducing equations of probabilistic constrained through the incorporation of uncertainty in the source-receptor-specific transfer coefficients. Based on the calculation of SO2 and sulfate average residence time for Liuzhou City, a sulfur deposition model has been developed and the distribution of transfer coefficients have been found to be approximately log-normal. Sulfur removal minimization of the model shows that the abatement of emission sources in the city is more effective, while control cost optimization provides the lowest cost programmes for source abatement at each allowable deposition limit under varied environmental risk levels. Finally a practicable programme is recommended.     

湿式氧化技术处理炼油厂碱渣废水

考察了湿式氧化法处理运行过程 ,以及相关参数的控制方案。在实现装置出水、废气达标排放的前提下 ,稳定控制装置运行是可以实现的。如后续有酸化除酚工艺和SBR工艺进行再处理 ,则应选用温度 (14 5± 5 )℃ ,压力控制在 0 6～ 0 .7MPa的湿式氧化法     

藻类在大连湾的水环境行为数值模拟研究

应用三维水质模型对大连湾水体中的藻类碳浓度的时空变化规律以及其影响因素进行了研究,选择主要的模型参数进行了灵敏度分析。由空间分布的模拟结果可知,在大连湾,藻类主要集中在排污口附近区域。由季节变化模拟结果可知,在湾顶部的排污口区藻类生产显示明显的季节变化趋势,在夏季,主要受到磷酸盐浓度的限制。灵敏度分析显示,在排污口区水体的扩散能力对藻类生产的影响较大,在湾中部和湾口区主要受到磷酸盐负荷的影响。模拟结果可以为大连湾的污染控制、水质规划和管理提供科学依据。     

Methodological and Practical Considerations for Developing Multiproject Baselines for Electric Power and Cement Industry Projects in Central America

The Lawrence Berkeley National Laboratory (Berkeley Lab) and the Center for Sustainable Development in the Americas (CSDA) conducted technical studies and organized two training workshops to develop capacity in Central America for the evaluation of climate change projects. This paper describes the results of two baseline case studies conducted for these workshops, one for the power sector and one for the cement industry, that were devised to illustrate certain approaches to baseline setting. Multiproject baseline emission rates (BERs) for the main Guatemalan electricity grid were calculated from 2001 data. In recent years, the Guatemalan power sector has experienced rapid growth; thus, a sufficient number of new plants have been built to estimate viable BERs. We found that BERs for baseload plants offsetting additional baseload capacity ranged from 0.702 kgCO2/kWh (using a weighted average stringency) to 0.507 kgCO2/kWh (using a 10th percentile stringency), while the baseline for plants offsetting load-following capacity is lower at 0.567 kgCO2/kWh. For power displaced from existing load-following plants, the rate is higher, 0.735 kgCO2/kWh, as a result of the age of some plants used for meeting peak loads and the infrequency of their use. The approved consolidated methodology for the Clean Development Mechanism yields a single rate of 0.753 kgCO2/kWh. Due to the relatively small number of cement plants in the region and the regional nature of the cement market, all of Central America was chosen as the geographic boundary for setting cement industry BERs. Unfortunately, actual operations and output data were unobtainable for most of the plants in the region, and many data were estimated. Cement industry BERs ranged from 205 kgCO2 to 225 kgCO2 per metric ton of cement.