屠宰厂项目环境防护距离的确定

综合考虑外界潜在污染源对屠宰厂的环境影响,从大气环境防护距离、卫生防护距离及外界潜在污染源的环境影响评价出发,分析污染评价因子的选取、标准值的确定、预测模式的选取和预测结果评价,实例探讨了屠宰厂项目环境防护距离的确定方法。结果表明,拟建化工项目未对屠宰厂的环境空气质量造成影响,TSP是外界污染源对屠宰厂影响最大的污染因子,综合计算大气环境防护距离值和卫生防护距离值得到屠宰厂的环境防护距离为300m。     

样品保存方法对阳极溶出伏安法测定时的影响

对海水中Cu、Pb、Zn、Cd的日常监测分析方法进行了调查,结果表明在调查范围内阳极溶出伏安法使用数量最高。通过实验研究了不添加保存剂、加浓HNO3、加浓HClO4对阳极溶出伏安法测定海水Cu、Pb、Zn、Cd的影响。发现不添加保存剂时4种金属峰电位变化范围大、出现频次分散,分析方法灵敏度下降。不同类型酸对阳极溶出伏安法测定Pb、Zn、Cd时的峰电位变化影响不大,加浓HNO3时Cu的峰电位变化小于加浓HClO4。根据实验结果,推荐使用保存剂为浓HNO3。     

Do Energy‐Based PET Models Require More Input Data than Temperature‐Based Models? — An Evaluation at Four Humid FluxNet Sites

It is well established that wet environment potential evapotranspiration (PET) can be reliably estimated using the energy budget at the canopy or land surface. However, in most cases the necessary radiation measurements are not available and, thus, empirical temperature‐based PET models are still widely used, especially in watershed models. Here we question the presumption that empirical PET models require fewer input data than more physically based models. Specifically, we test whether the energy‐budget‐based Priestley‐Taylor (P‐T) model can reliably predict daily PET using primarily air temperature to estimate the radiation fluxes and associated parameters. This method of calculating PET requires only daily minimum and maximum temperature, day of the year, and latitude. We compared PET estimates using directly measured radiation fluxes to PET calculated from temperature‐based radiation estimates at four humid AmeriFlux sites. We found good agreement between P‐T PET calculated from measured radiation fluxes and P‐T PET determined via air temperature. In addition, in three of the four sites, the temperature‐based radiation approximations had a stronger correlation with measured evapotranspiration (ET) during periods of maximal ET than fully empirical Hargreaves, Hamon and Oudin methods. Of the three fully empirical models, the Hargreaves performed the best. Overall, the results suggest that daily PET estimates can be made using a physically based approach even when radiation measurements are unavailable.     

白洋淀流域府河干流村落非点源负荷研究

村落非点源污染是白洋淀流域农业非点源污染的重要组成部分.现场调查府河干流临河村落生活污水、生活垃圾的排放情况及相应污染物含量,研究了其非点源污染特征.结果表明:临河村落生活污水与生活垃圾的人均排放量分别为26.3 L/d和0.41 kg/d;临河村落非点源氮、磷污染中,生活垃圾贡献极大,在TN、TP年潜在入河负荷和年入河负荷中所占比例均接近70%;生活污水中的氮、磷以可溶态为主;生活污水与人粪尿的CODCr年入河负荷分别为10.9和2.30 t,生活垃圾的TOC年入河负荷为26.9 t.      

抗滑桩加固三维多地层边坡最小势能稳定性分析

为了分析抗滑桩加固边坡的稳定性,基于最小势能原理,考虑桩土之间的相互作用和滑面储存的剪切势能,提出了抗滑桩加固多地层边坡的三维稳定性分析方法。将该方法与其他方法进行对比验证,并分析了抗滑桩相关参数对边坡稳定性的影响。结果表明:该方法是合理可行的;当抗滑桩位于边坡中部时,对边坡的稳定性更好;当抗滑桩的桩间距大于8 m时,抗滑桩间距的变化对边坡安全系数的影响较小。     

针对安全生产隐患的智能搜索引擎系统研究

为解决用户在现有搜索引擎上难以检索到专业和全面的安全生产隐患知识的问题,提出一种安全生产隐患数据的挖掘方法和针对安全生产隐患的智能搜索引擎系统的设计方法。结果表明:对于用户的搜索,系统能够直接反馈智能化查询结果,包括:隐患内容、隐患来源、隐患的行业,隐患场所、法规标准、事故信息等数据以及数据之间的关联关系。给出的示例和结果图表,说明了这种数据挖掘方法的有效性;对相关智能搜索引擎系统的组成、工作原理及实现方式的阐述,说明了系统设计方法的有效性,可为安全生产隐患智能搜索引擎系统的设计与开发提供参考。     

滇池沉积物内源氮释放风险及控制分区

采用淹水培养法测定了滇池20cm沉积物可释放态氮(EN)、潜在可释放态氮(MN)及稳定态氮(FN)含量,并分析了其空间分布特征,结合沉积物定年数据计算了不同形态氮蓄积量.依据沉积物-水界面氮释放通量、EN蓄积量及MN蓄积量对滇池沉积物内源氮污染状况进行分区,评估了不同区域滇池沉积物内源氮释放风险,并对不同分区提出了污染控制措施.结果表明,滇池沉积物内源氮释放风险:外海南部 >外海北部 >外海中部 >草海,潜在释放风险:外海南部 >外海中部 >草海 >外海北部;滇池沉积物氮污染有由北向南转移趋势;滇池全湖20cm沉积物蓄积TN5757.90t,EN637.72t,MN1320.76t,FN3799.42t.根据沉积物氮污染滇池可划分为高污染区、中度污染区、低污染区及安全区,分别占全湖面积的13.51%、15.02%、46.06%、25.42%,其中高污染区主要分布在草海、外海北部盘龙江附近;中度污染区主要分布在高污染区以下从宝象河到观音山区域及滇池出水口海口等区域;低污染区主要分布在中度污染区以下从广谱大沟到整个外海南部区域.高污染区可采取底泥环保疏浚技术,中度污染区可采取安全生态性高的原位控制技术,低污染区可采取覆盖技术,配合水生植被修复技术.     

石油炼化无组织VOCs的排放特征及臭氧生成潜力分析

选取我国光化学活跃的珠江三角洲地区(PRD)典型石油炼化工艺的炼油装置、化工装置和污水处理装置,采用离线和在线的多种先进仪器监测其VOCs的无组织排放特征,并采用间、对-二甲苯/苯(X/B)、甲苯/苯(T/B)、乙苯/苯(E/B)比值分析其VOCs的老化特征,采用最大增量反应活性法(MIR)、等效丙烯浓度法和OH自由基反应速率法(L_OH)3种方法综合评价其VOCs的化学反应活性及臭氧生成潜势(OFP).研究发现,炼油装置区和化工装置区总挥发性有机物(TVOC)浓度早晚高,中午低;污水处理区呈双峰趋势.3个装置区无组织排放的VOCs中烷烃浓度均占比最高,同一装置区内的不同装置VOCs排放特征不同.石化企业X/B、T/B和E/B值较城区和郊区的高,化工装置区的压缩碱洗装置区(CAW)T/B值最大.石化企业VOCs的活性较城区和郊区的强,其平均OH消耗速率常数为15.22×10^-12cm³/(mol·s),最大增量反应活性为4.21mol(O₃)/mol(VOC).化工装置区对石化企业OFP总量的贡献最高,为84.83%;其次是污水处理区,12.95%;炼油装置区最低,为2.22%.化工装置区的CAW对石化企业OFP贡献率最高,为34.26%;污水处理区的浮选池(FT)贡献率最低,为0.36%.     

Assessing the potential of crop residue recycling in China and technology options based on a bottom-up model

Crop residues are an important biomass, and are significant in the sustainable development of China. This paper uses the Grey-Markov modeling approach, the cost-benefit analysis method, and the constraint optimiza- tion method to establish the potential of crop residue recycling in China （CRRC） using a bottom-up analysis. Taking 2010 as the baseline year, the CRRC model is used to determine the quantity trends of crop residue resources, simulating the recycling potential and selecting key crop residue recycling technologies for operation between 2010 and 2030. The results illustrate that the total residue output from different crops will gradually increase to 1062 million tons in 2030. The proportion of crop residue for field burning is expected to decrease as a result of guidance and support from the government. Market mechanisms are also improving the development of the crop residue recycling industry. The economic benefit of crop residue recycling is expected to be worth 132 billion CNY in 2030 according to technology structure options. Key crop residue recycling technologies preferred such as liquefaction, amination, silo, co-firing straw power and composting will account for more than 85% of the total benefits.     

Effects of bicarbonate and cathode potential on hydrogen production in a biocathode electrolysis cell

A biocathode with microbial catalyst in place of a noble metal was successfully developed for hydrogen evolution in a microbial electrolysis cell （MEC）. The strategy for fast biocathode cultivation was demonstrated. An exoelectrogenic reaction was initially extended with an H2-full atmosphere to enrich Ha-utilizing bacteria in a MEC bioanode. This bioanode was then inversely polarized with an applied voltage in a half-cell to enrich the hydrogen-evolving biocathode. The electrocatalytic hydrogen evolution reaction （HER） kinetics of the biocathode MEC could be enhanced by increasing the bicarbonate buffer concentration from 0.05 mol·L-1 to 0.5 mol· L-1 and/or by decreasing the cathode potential from -0.9 V to - 1.3 V vs. a saturated calomel electrode （SCE）. Within the tested potential region in this study, the HER rate of the biocathode MEC was primarily influenced by the microbial catalytic capability. In addition, increasing bicarbonate concentration enhances the electric migration rate of proton carriers. As a consequence, more mass H＋ can be released to accelerate the biocathode-catalyzed HER rate. A hydrogen production rate of 8.44 m3. m 3. d1 with a current density of 951.6 A. m-3 was obtained using the biocathode MEC under a cathode potential of - 1.3 V vs. SCE and 0.4 mol· L-1 bicarbonate. This study provided information on the optimization of hydrogen production in biocathode MEC and expanded the practical applications thereof.