改良SBR工艺实现生活污水除磷与半亚硝化

常温条件下(20~25℃),采用序批式反应器(SBR),应用改进后的运行策略:进水、厌氧搅拌、曝气搅拌、静置沉淀、排水、选择性排泥、污泥床缺氧搅拌,控制污泥龄为20d,溶解氧为0.2~0.5mg/L,实现单污泥系统同步除磷亚硝化的稳定运行.结果表明:总磷去除率为95.9%~97.1%,出水总磷浓度为0.1~0.4mg/L,好氧阶段氨氮去除容积负荷为0.242kg N/(m3·d),出水氨氮和亚硝酸盐氮的比值约为1:1,可以为后续的厌氧氨氧化提供合适的进水.     

Mass concentrations and temporal profiles of PM10, PM2.5 and PM1 near major urban roads in Beijing

Mass concentrations of PM₁₀, PM_2.5 and PM₁ were measured near major roads in Beijing during six periods: summer and winter of 2001, winter of 2007, and periods before, during and after the 2008 Beijing Olympic Games. Since the control efforts for motor vehicles helped offset the increase of emissions from the rapid growth of vehicles, the averaged PM_2.5 concentrations at roadsides during the sampling period between 2001 and 2008 fluctuated over a relatively small range. With the implementation of temporary traffic control measures during the Olympics, a clear “V” shaped curve showing the concentrations of particulate matter and other gaseous air pollutants at roadsides over time was identified. The average concentrations of PM₁₀, PM_2.5, CO and NO decreased by 31.2%, 46.3%, 32.3% and 35.4%, respectively, from June to August; this was followed by a rebound of all air pollutants in December 2008. Daily PM₁₀ concentrations near major roads exceeded the National Ambient Air Quality Standard (Grade II) for 61.2% of the days in the non-Olympic periods, while only for 12.5% during the Olympics. The mean ratio of PM_2.5/PM₁₀ near major roads remained relatively stable at 0.55 (±0.108) on non-Olympic days. The ratio decreased to 0.48 (±0.099) during the Olympics due to a greater decline in fine particles than in coarse-mode PM. The ratios PM₁/PM_2.5 fluctuated over a wide range and were statistically different from each other during the sampling periods. The average ratios of PM₁/PM_2.5 on non-Olympic days were 0.71.     

隧道半横向排烟模式下不同排烟口分布的温度场数值模拟研究

结合某过江盾构隧道,基于三维流体动力学模拟仿真软件平台,建立三维仿真模型,研究火灾发生在隧道盾构段典型区段时,排烟开口在火源上下游不同的分布模式时烟气层的温度场分布。通过分析模拟结果可知:随着火源上游排烟开口逐步增加,火源上游烟气逆流长度和蔓延速度都相对稳定而后又逐步增长,火源下游的烟气蔓延长度先减小而后又基本趋于稳定,下游烟气沉降高度则有所升高;火源位置处正上方温度则随着上游排烟开口的个数逐步增加而逐渐升高。而从其他的排烟开口变化模式模拟结果可知:随着排烟开口面积或者开口间距的逐步增大,烟气蔓延的速度先增加而后又逐步减小,且开口间距为30m左右时烟气蔓延速度相对较慢;排烟开口宽高比对烟气蔓延影响较小。所获得的结论将有助于相关类型工程的设计和管理。     

钻井井喷失控因素分析及预防对策

井喷失控是钻井中的灾难性事故,有必要开展井喷失控研究,找到井喷失控发生的原因和提出防止井喷失控的对策。在统计分析1970年到2009年间中石油发生在钻进过程中的48例井喷失控事故的基础上,通过对防喷器、节流压井管汇、套管、井喷后爆炸起火等井喷失控因素分析,并利用MLS法对上述各种井喷失控因素危险值进行评估。最后,根据井喷失控因素分析和危险值评估结果,结合现有的钻井井控设计,提出了防止钻井井喷失控的对策。     

矿井通风网络复杂度与风机控制力量化计算

为了探究矿井通风网络复杂度与风机控制力的关系,提出分支关联度、最小距离、通风网络复杂度和风机控制力的概念。利用vCad2.0进行数字实验,对网络复杂度与风机控制力的关系进行定量研究。结果表明:随着网络复杂度的增加,矿井通风系统的有效风量率减小,且认为该值减小到60%时,视为风机控制力的极限,此时网络拓扑结构为风机所能控制的最大网络复杂度。地面集中供风时,同时工作的中段数量存在上限,最大值为7。将结论用于某有色金属矿进行实证研究,找出该矿深部中段通风困难的原因,为矿井进一步整改提供理论依据。     

分层水库温度梯度对扬水曝气原位控藻效果的影响

基于计算流体力学(CFD)方法,数值模拟了不同温度梯度条件下扬水曝气器外围流场及藻类浓度场,并与实际工程运行数据进行对比.当水深为80m、水面下30m内的温度梯度从0.17℃/m增加到0.73℃/m时,核心控藻区域的半径从100m增加到150m,控藻区域百分比从25.16%增大到28.60%,藻类完全混合的时间分别从16d增加到24d.在稳定条件下,藻类在补偿点以下的停留时间均大于48h,基本不受温度梯度的影响,藻类生长受抑制.藻类浓度模拟结果与实际工程运行结果吻合良好.推荐水库中扬水曝气器合理设计间距为250m.     

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.     

日本琵琶湖污染源系统控制及其对我国湖泊治理的启示

琵琶湖富营养化全面有效的控制得益于对流域污染源的系统控制. 琵琶湖流域污染源系统控制包括通过立法与监管严格控制工厂与企业的污水排放、城镇污水管网与大型污水处理设施的高度覆盖、农业集落污水处理设施的全覆盖三部分,流域污水处理系统的全覆盖及高度处理技术的普及是其最为成功的经验之一. 琵琶湖流域城镇下水道普及率达86.4%,主要污染物——TN、TP及COD_Mn的去除率分别高达90.0%、98.7%及94.6%. 琵琶湖流域同时实施了净化槽普及、设置农业集落排水处理设施、初期雨水净化处理及农田循环灌溉等具有地方特色的面源治理对策. 通过综合治理,琵琶湖主要入湖污染负荷明显减少,与1985年相比,2012年COD_Mn点源污染负荷减少了76.8%,TN减少了45.5%,TP减少了65.6%. 与之比较,我国的湖泊治理存在的问题主要包括有针对性的地方排放标准的缺失及执法力度的不足、城镇污水深度处理及运营管理技术上的差距、面源污染对策的严重不足.      

A red water occurrence in drinking water distribution systems caused by changes in water source in Beijing,China: mechanism analysis and control measures

A red water phenomenon occurred in several communities few days after the change of water source in Beijing, China in 2008. In this study, the origin of this problem, the mechanism of iron release and various control measures were investigated. The results indicated that a significant increase in sulphate concentration as a result of the new water source was the cause of the red water phenomenon. The mechanism of iron release was found that the high-concentration sulphate in the new water source disrupted the stable shell of scale on the inner pipe and led to the release of iron compounds. Experiments showed that the iron release rate in the new source water within pipe section was over 11-fold higher than that occurring within the local source water. The recovery of tap water quality lasted several months despite ameliora- tive measures being implemented, including adding phosphate, reducing the overall proportion of the new water source, elevating the pH and alkalinity, and utilizing free chlorine as a disinfectant instead of chloramine. Adding phosphate was more effective and more practical than the other measures. The iron release rate was decreased after the addition of 1.5 mg. L-1 orthophosphate- P, tripolyphosphate-P and hexametaphosphate-P by 68%, 83% and 87%, respectively. Elevating the pH and alkalinity also reduced the iron release rate by 50%. However, the iron release rate did not decreased after replacing chloramine by 0.5-0.8 mg. L-1 of free chlorine as disinfectant.     

A review of atmospheric mercury emissions,pollution and control in China

Mercury, as a global pollutant, has significant impacts on the environment and human health. The current state of atmospheric mercury emissions, pollution and control in China is comprehensively reviewed in this paper. With about 500-800 t of anthropogenic mercury emissions, China contributes 25%-40% to the global mercury emissions. The dominant mercury emission sources in China are coal combustion, non-ferrous metal smelting, cement production and iron and steel production. The mercury emissions from natural sources in China are equivalent to the anthropogenic mercury emissions. The atmospheric mercury concentration in China is about 2-10 times the background level of North Hemisphere. The mercury deposition fluxes in remote areas in China are usually in the range of 10-50μg·m^-2·yr^-1. To reduce mercury emissions, legislations have been enacted for power plants, non-ferrous metal smelters and waste incinerators. Currently mercury contented in the flue gas is mainly removed through existing air pollution control devices for sulfur dioxide, nitrogen oxides, and particles. Dedicated mercury control technologies are required in the future to further mitigate the mercury emissions in China.