珠江三角洲机动车排放控制措施协同效应分析

预测了2015年珠江三角洲机动车空气污染物和温室气体排放量,设计了6类单一控制、技术控制、结构控制以及综合控制措施的情景,并运用基准线年排放清单编制和协同效应坐标系法分析了污染物与温室气体减排的协同效应.结果表明,按目前机动车保有量增长趋势,2015年污染物和温室气体将以18%~120%的幅度增加;各控制措施下污染物和温室气体排放量均有下降,且均具有正向的协同效应,但减排的贡献差异较大.6类单一控制措施中淘汰黄标车和结构性控制措施分别对各污染物和温室气体的削减效果最明显,减排幅度均在40%以上,且正向协同效应突出,但相比其他措施,结构性控制措施实施难度大.     

大气中持久性有机污染物在气相和颗粒相中的分配特征研究进展

大气中持久性有机污染物(POPs)的气(气相)-粒(颗粒相)分配是影响POPs在大气中分布、迁移和转化的一个重要因素,研究POPs的气-粒分配特征有助于提高POPs环境归趋预测的准确性,对区域范围内的大气POPs污染防治具有重要意义.本文简要介绍了两种经典的POPs气-粒分配理论及模型,总结了有关大气中几类典型POPs在气相和颗粒相中的分配特征研究的最新进展,讨论了不同种类POPs气-粒分配的一些差异性特征和可能的影响因素,并提出了大气中新型POPs气-粒分配特征研究中亟待解决的问题.     

矿化垃圾生物覆盖层减少垃圾填埋场CH4、N2O和CO2释放的效应研究

对利用矿化垃圾构建生物覆盖层以削减填埋场温室气体的释放问题进行了深入研究,分析了环境因素对CH4释放的作用,考察了作为生物覆盖层材料的矿化垃圾的厚度变化对CH4氧化的影响.结果表明,温度为5～45℃时,矿化垃圾对CH4的氧化速率平均值分别约为黏性土和砂性土的2.35和4.71倍,CH4氧化速率随温度的升高而增加,并在35℃时达到最大值.当含水率w为16％ ～ 24％时,纯矿化垃圾覆盖层、半矿化垃圾覆盖层和砂性土覆盖层CH4氧化能力均达到最大.砂性土覆盖层和半矿化垃圾覆盖层CH4释放通量平均值分别为纯矿化垃圾覆盖层的329.8倍（P＜0.05）和91.7倍（P＜0.05）,添加矿化垃圾填料会增加覆盖层N2O释放通量,纯矿化垃圾覆盖层N2O（以N计）释放通量平均值分别为半矿化垃圾覆盖层和砂性土覆盖层的2.1倍（P＜0.05）和3.5倍（P＜0.05）.     

典型电子垃圾拆解区二噁英污染特征、相分配及暴露风险

选取南方某典型电子垃圾拆解区不同作业区为研究对象,重点研究了拆解地大气中二噁英的污染特征、气相-颗粒相分配及呼吸暴露风险。通过对5个采样点（包括1个背景点）的研究发现,电子垃圾拆解作业区颗粒相ΣPCDD/Fs的质量浓度为：20.64-56.14 pg·m^-3,毒性当量为：I-TEQ 0.293-1.490 pg·m^-3;气相ΣPCDD/Fs的质量浓度为：3.861-19.29 pg·m^-3,毒性当量为：I-TEQ 0.384-2.150 pg·m^-3。背景点大气中二噁英浓度相对较低,颗粒相和气相样品中质量浓度值分别为：3.734 pg·m^-3和2.637 pg·m^-3,毒性当量仅为I-TEQ 0.176-0.267 pg·m^-3;要明显低于电子垃圾拆解区。基于污染物气相-颗粒相分配系数与蒸汽压的关系对二噁英的气-固分配行为研究显示,除了拆解混合作业区有较好的分配系数（-0.64）外,其它监测点位二噁英的气-固平衡状态较弱（-0.27--0.03）,更多的是以低分子量的单体化合物赋存于气相样品中。对拆解区二噁英呼吸暴露风险研究结果表明,儿童呼吸暴露风险要高于成年人;同时无论是儿童还是成年人,其二噁英的呼吸暴露量均要高于国内外城市报道的二噁英人体呼吸暴露量,说明本次监测的电子垃圾拆解区存在的潜在健康风险不容忽视。     

互花米草入侵盐沼湿地CH4和N2O排放日变化特征研究

甲烷（CH4）和氧化亚氮（N2O）是导致全球气候变暖的2种重要温室气体,探索其源汇及地域排放特征一直是全球变化研究领域的核心内容。CH4和N2O通量的日变化研究是正确估算大时间尺度下CH4和N2O排放量的基础。利用静态箱法原位观测了江苏沿海芦苇（Phragmites australis）、盐蒿（Suada salsa）、光滩、水面以及互花米草（Spartina alterniflora）入侵湿地CH4和N2O排放的日变化特征。结果表明,1）互花米草湿地地上部生物量为1.70 kg·m^-2,土壤有机碳质量分数为13.55 g·kg^-1;分别是芦苇和盐蒿湿地的2.50-3.43和2.15-4.15倍。2）互花米草和芦苇湿地土壤10 cm处氧化还原电位（Eh）有明显日变化,最低值出现在3：00,最高值出现在12：00;光滩和盐蒿湿地没有明显的日变化。3）互花米草湿地 CH4日平均排放通量为0.52 mg·m^-2·h^-1,是其他湿地的2.12-6.40倍;N2O日平均通量为-3.24μg·m^-2·h^-1,显著低于盐蒿湿地、光滩和水面（P＜0.05）。互花米草和芦苇湿地CH4排放通量最高值（0.73 mg·m^-2·h^-1和0.30 mg·m^-2·h^-1）出现在15：00,最低值（0.37 mg·m^-2·h^-1和0.17 mg·m^-2·h^-1）出现在3：00,均与土壤孔隙水中CH4浓度呈显著负相关（P＜0.05）。互花米草湿地CH4排放通量与10 cm土温、Eh和生态系统CO2净交换量（NEE）显著正相关（P＜0.05）。互花米草和芦苇湿地N2O通量9：00-18：00为负值,21：00—6：00为正值,均与NEE呈显著负相关（P＜0.05）。盐蒿湿地、光滩和水面CH4和N2O排放通量没有明显日变化特征。互花米草入侵提高了沿海湿地CH4排放,但降低了N2O排放,植物对CH4传输作用以及向根际传输O2和易分解有机物是导致互花米草和芦苇湿地CH4和N2O排放表现出日变化特征的原因。     

N2O emission from a sequencing batch reactor for biological N and P removal from wastewater

Nitrous oxide （N2O） is a greenhouse gas that can be released during biological nitrogen removal from wastewater. N2O emission from a sequencing batch reactor （SBR） for biological nitrogen and phosphorus removal from wastewater was investigated, and the aims were to examine which process, nitrification or denitrification, would contribute more to N2Oemission and to study the effects of heterotrophic activities on N2O emission during nitrification. The results showed that N2O emission was mainly attributed to nitrification rather than to denitrification. N2O emission during denitrification mainly occurred with stored organic carbon as the electron donor. During nitrification, NaO emission was increased with increasing initial ammonium or nitrite concentrations. The ratio of N2O emission to the removed ammonium nitrogen （N2O- N/NH4-N） was 2.5% in the SBR system with high heterotrophic activities, while this ratio was in the range from 0.14% to 1.06% in batch nitrification experiments with limited heterotrophic activities.     

Validation of the UN test method N.5

Many substances react with water in such a way that flammable gases are formed. For transport issues this reaction may possess a considerable hazard especially if the cargo is wetted by rain or by water from other sources. In the UN Recommendations on the Transport of Dangerous Goods these kinds of problems are addressed. The UN test N.5 “Test method for substances which in contact with water emit flammable gases” corresponds to this hazard. Classification according to the test method is done by measurement of the gas evolution rate of the flammable gas by any suitable procedure. At BAM a gravimetric approach is used to measure the gas evolution rate. In this paper we present the evaluation of the apparatus by means of an absolute calibration routine utilizing a reaction where a known amount of gas is produced as well as the evaluation of important parameters influencing the gas evolution rate using different substances. It can be shown that the apparatus is capable of measuring absolute gas volumes as low as 6 mL with an acceptable error of about 17% as determined from the reaction of Mg with demineralized water.     

Targeting for optimal grid-wide deployment of carbon capture and storage (CCS) technology

Carbon capture and storage (CCS) techniques are considered as one of the promising approaches to reduce carbon dioxide (CO₂) emissions from fossil fuel based power generation, which still accounts for a significant portion of greenhouse gas emissions in the world. CCS technology can be used to mitigate greenhouse gas emissions, with the additional advantage that it allows continuing use reliable and inexpensive fossil fuels. However, CCS retrofit entails major capital costs as well as a reduction of overall thermal efficiency and power output. Thus, it is essential for planning purposes to implement the minimal extent of CCS retrofit while meeting the specified carbon emission limits for the power sector. At the same time, it is necessary to plan for compensatory power generation capacity to offset energy losses resulting from CCS retrofit. In this paper, an algebraic targeting technique is presented for planning of grid-wide CCS retrofits in the power generation sector with compensatory power. The targeting technique is developed based on pinch analysis. In addition, the proposed methodologies are illustrated through case studies based on grid data in India and the Philippines. Sensitivity analysis is carried out to determine the suitable CCS technology and compensatory power source which satisfy emission limits.     

Environmental consequence analysis for resource depletion

Resource depletion is of concern to both present and future generations in terms of access to resources. It is a prominent impact category within life cycle assessment (LCA) and sustainability assessment. This paper examines existing resource depletion approaches and indicators in the context of natural gas depletion, and their limitations in modelling the wider environmental consequences of resource consumption. Some existing models assume substitution of scarce fossil fuels with an alternative fossil fuel or mix, but do not consider all of the subsequent change in impacts. An additional methodology is proposed to measure the impact changes when fossil fuel substitution occurs as a result of scarcity. The methodology will demonstrate the effect of resource scarcity for individual processes but also multiple processes which operate at different levels of resource consumption with varying degrees of impacts. The methodology is applied to a scarcity situation of natural gas in Australia, where black coal is substituted for gas. It is first applied to natural gas consumed for electricity generation only. In the second case, the methodology is applied to the substitution of natural gas for both electricity generation and hydrogen production. The varying impacts on emissions to air and water, together with solid waste generation and water depletion, as a result of the substitution are used to reflect the consequences of fossil fuel depletion. The indicators also provide information on the impacts of substitution in each product, thus enabling users to prioritise products based on the impacts produced during natural gas allocation.     

Thermodynamic investigation and hydrate inhibition of real gas flow through orifice during depressurization

A thermodynamic procedure has been proposed which can be used to predict the gas pressure, temperature and flow rate through orifice upon chock flow condition, using equation of state (EOS). The procedure applied for emergency depressurization operation incorporating the Peng-Robinson EOS and validated by comparing flow rates of a multi-component hydrocarbon gas mixture for thirteen experimental cases. The average absolute deviations of the predicted flow rates for orifice discharge coefficients of 0.85 and 0.9, are 7.36% and 2.03%, respectively. The corresponding error for API 520 (American Petroleum Institute Recommendation Practice 520) method is 6.91%. In this work, the hydrate formation temperature and hydrate inhibitor type and its required weight fraction for preventing the hydrate formation upon orifice and its upstream conditions are evaluated by the EZ-Thermo software using the Moshfeghian–Maddox method. The results qualitatively show that the hydrate prevention is essential for the safety of the operation due to low temperature condition.