井下光谱多参数分析系统开发

本系统基于气体浓度光学分析方法理论朗伯-比尔(Lambert-Beer)定律、光谱气体检测技术开发,实现了对煤矿火灾与瓦斯灾害超前预警、灾害产生的有毒有害气体实时监测和煤矿环境气体爆炸危险性辨识,对于煤矿灾害防治、救灾过程中杜绝次生灾害,保障煤矿工人及救护队员的生命安全,促进煤矿安全生产具有重要意义。     

室内空气和灰尘中全(多)氟烷基化合物的研究进展

全(多)氟烷基化合物(per(poly)fluoroalkyl substances,PFASs)在环境各个介质及人体样品中广泛被检出,近年,在室内空气和灰尘中也普遍发现PFASs.研究表明,室内空气中PFASs的含量普遍高于室外空气,室内空气和灰尘中的PFASs可能是室外空气的污染来源及人体暴露源,因此室内环境中PFASs成为环境领域的又一个研究热点.但目前为止,我国还没有开展室内空气中PFASs的相关研究,室内灰尘中PFASs的研究也相对较少.本文就室内空气和灰尘中PFASs的采样与分析方法、污染现状、来源分析及人体暴露等4个方面进行了综合阐述,以期为我国室内环境中PFASs的研究提供参考.     

冲击水浴喷雾式除尘器的应用

介绍了冲击水浴喷雾式除尘器在柳钢焦化厂的应用试验情况，制作安装，调试运行后检测鉴定表明，冲击水浴喷雾式除尘器应用在冶金焦末粉尘上，不但操作简单，维护方便，除尘效率高，效果好，而且成本低廉，只有电除尘器或布袋除尘器的20%左右。     

MnO2/Al2O3催化剂-微气泡臭氧体系催化降解喹啉及其机理

制备了纳米MnO₂,并以Al₂O₃为载体制备了掺杂型MnO₂/Al₂O₃颗粒催化剂.催化剂焙烧温度和时间分别为500℃和4 h、MnO₂质量分数为8%时,催化剂具有最高的臭氧催化氧化活性.SEM分析表明,纳米MnO₂均匀分布于Al₂O₃载体表面.MnO₂/Al₂O₃催化剂的比表面积（BET）为183.22 m²·g^-1,平均孔容为0.27 cm³·g^-1,平均孔径为4.87 nm.建立了MnO₂/Al₂O₃催化剂-微气泡臭氧催化反应体系,研究了该体系对喹啉的降解去除效果及其机理.臭氧微气泡的平均粒径为61.7 μm.微气泡臭氧投量为30 mg·L^-1时,反应60 min后喹啉去除率能达到95%以上;反应20 min后,MnO₂/Al₂O₃催化剂-微气泡臭氧体系对实际煤化工废水二级出水的TOC去除率可达到55%以上.以叔丁醇作为分子探针,证明了羟基自由基（·OH）氧化作用在臭氧微气泡催化氧化体系中对喹啉的降解起到主导作用.     

Reactive uptake of NO2 on volcanic particles: A possible source of HONO in the atmosphere

The heterogeneous degradation of nitrogen dioxide (NO₂) on five samples of natural Icelandic volcanic particles has been investigated. Laboratory experiments were carried out under simulated atmospheric conditions using a coated wall flow tube (CWFT). The CWFT reactor was coupled to a blue light nitrogen oxides analyzer (NO_x analyzer), and a long path absorption photometer (LOPAP) to monitor in real time the concentrations of NO₂, NO and HONO, respectively. Under dark and ambient relative humidity conditions, the steady state uptake coefficients of NO₂ varied significantly between the volcanic samples probably due to differences in magma composition and morphological variation related with the density of surface OH groups. The irradiation of the surface with simulated sunlight enhanced the uptake coefficients by a factor of three indicating that photo-induced processes on the surface of the dust occur. Furthermore, the product yields of NO and HONO were determined under both dark and simulated sunlight conditions. The relative humidity was found to influence the distribution of gaseous products, promoting the formation of gaseous HONO. A detailed reaction mechanism is proposed that supports our experimental observations. Regarding the atmospheric implications, our results suggest that the NO₂ degradation on volcanic particles and the corresponding formation of HONO is expected to be significant during volcanic dust storms or after a volcanic eruption.     

Coupling mechanism of activated carbon mixed with dust for flue gas desulfurization and denitrification

To clarify the effect of coking dust, sintering dust and fly ash on the activity of activated carbon for various industrial flue gas desulfurization and denitrification, the coupling mechanism of the mixed activated carbon and dust was investigated to provide theoretical reference for the stable operation. The results show that coking dust had 34% desulfurization efficiency and 10% denitrification efficiency; correspondingly, sintering dust and fly ash had no obvious desulfurization and denitrification activities. For the mixture of activated carbon and dust, the coking dust reduced the desulfurization and denitrification efficiencies by blocking the pores of activated carbon, and its inhibiting effect on activated carbon was larger than its own desulfurization and denitrification activity. The sintering dust also reduced the desulfurization efficiency on the activated carbon while enhancing the denitrification efficiency. Fly ash blocked the pores of activated carbon and reduced its reaction activity. The reaction activity of coking dust mainly came from the surface functional groups, similar to that of activated carbon. The reaction activity of sintering dust mainly came from the oxidative property of Fe₂O₃, which oxidized NO to NO₂ and promoted the fast selectively catalytic reduction (SCR) of NO to form N₂. Sintering dust was activated by the joint action of activated carbon, and both had a coupling function. Sintering dust enhanced the adsorption and oxidation of NO, and activated carbon further promoted the reduction of NO_x by NH₃; thus, the denitrification efficiency increased by 5%-7% on the activated carbon.     

不同居民燃煤炉具大气污染物排放差异性及减排分析

为探究不同类型炉具的大气污染物排放差异,本研究选择5种常见的新式居民燃煤炉具（方型煤炉具、折流换热炉具、炕暖炊一体化炉具、气化正烧及气化反烧炉具）在实验室内进行模拟燃烧和大气污染物排放水平监测,定量评估不同炉具的环境效果,识别污染排放水平差异的影响因素及原因,从而提出炉具研发设计等污染减排的改进建议.结果表明：①不同炉具大气污染物排放差异较大,炕暖炊一体的炉具污染排放强度最大,3种大气污染物（SO₂、NO_x和颗粒物）的排放强度为2.9 kg ·t^-1,是平均值的1.6倍;应用方型煤技术的炉具大气污染物排放强度最低,是平均值的65%.②不同炉具在不同燃烧阶段其气态污染物排放也呈现出明显的差异和特征.旺火阶段方型煤炉具NO_x排放浓度为0.49mg ·m^-3,相较于其他类型炉具降低了45%~72%;气化反烧炉具的SO₂排放浓度为1.38mg ·m^-3,相较于其他类型炉具最高降低了28%.③影响炉具大气污染物排放因素包括应用技术及燃烧类型,采用方型煤及气化反烧技术的炉具环境效益较好,但两类炉具的经济成本分别达到2.0万元和1.8万元,明显高于其他类型炉具.④考虑不同炉具污染排放差异,建议采取差异化的经济政策和严格的排放和产品标准,推广使用节能环保型炉具,降低燃煤炉具大气污染物排放.     

海绵城市地块汇水区颗粒污染物的传输

目前我国海绵工程建设多集中在地块汇水区单元内开展,通过多个低影响开发(LID)设施协同完成地表径流水质水量的调控,但基于地块汇水区尺度下城市面源污染的产生和控制效果鲜有报道.本研究比较分析了不同硬化率地块汇水单元内的面源颗粒污染物晴天累积、降雨冲刷、地表径流及径流输出负荷状况.结果表明,地块汇水单元内硬质路面是面源颗粒污染物贡献的最主要的下垫面类型,中硬化率(61.1%)地块和高硬化率(73.6%)地块路面街尘累积量分别约占汇水区单元的88.4%(2.22～12.51 g·m~(-2))和90.1%(4.99～33.43 g·m~(-2)),对径流SS的输出贡献比率分别约为91.7%(0.97～7.34 g·m~(-2))和90.5%(0.92～18.77 g·m~(-2)),降雨径流SS污染负荷占比分别约为95.2%和83.1%,经LID设施处理后输出径流污染负荷约为地表径流的24.0%和40.2%.硬质路面的街尘晴天累积及降雨冲刷以150μm为主,地表径流及输出径流则以50μm粒径段为主,同时地块不透水比例的增加,细粒径(105μm)颗粒物的累积及冲刷分布增大(24.4%和106.4%),而粒径50μm的颗粒物在路面径流中的分布减小(12.4%).屋面的街尘累积、冲刷及降雨径流的粒径分布状况与硬质路面大致相似,但中硬化率地块(1 000μm)和高硬化率地块(250～450μm、45μm)在3个粒径段范围的颗粒物累积和冲刷相较于路面街尘粒径分布明显增加(1 000μm:58.1%和108.5%; 250～450μm:72.9%和41.8%;45μm:59.2%和64.8%).以上结果揭示了颗粒污染物在地块汇水区尺度下的污染全过程(累积-冲刷-输出)分布及LID设施对地块整体SS污染负荷的控制效果,可为地块汇水单元内LID设施工程绩效的科学评估提供重要参考.     

成都市施工扬尘排放特征研究

采用DustTRAK TM气溶胶（粉尘）监测仪对成都市112个不同类别的房建、市政工地施工扬尘进行测试,研究了不同类别施工扬尘的排放特征,分析了下风向扬尘浓度的变化趋势,并采用CALPUFF对成都市新都区某建筑工地的排放进行了模拟.结果表明：（1）成都市施工扬尘排放浓度约为0.13~2.91mg/m³,其中房建类施工平均浓度约为0.94mg/m³,高于市政施工;大型工地扬尘平均浓度约为0.61mg/m³,低于中型和小型工地;土方施工阶段平均浓度约为1.21mg/m³,远高于地基建设、主体建设、装饰阶段.（2）成都市施工扬尘呈现出高低浓度交替的周期性变化,其中房建工程土方施工阶段的高低浓度差值可达到0.6mg/m³以上.（3）施工扬尘在场界外下风向5~15m范围内会出现浓度增加的趋势,随后逐渐下降,在50m附近逐渐趋于稳定,稳定浓度介于0.1~0.2mg/m³.（4）CALPUFF模型能较好地从宏观角度来模拟成都地区施工扬尘的扩散趋势,但难以捕捉施工扬尘在下风向近距离的扩散特征.     

长治市沙尘天气污染特征及传输路径解析

以2018年3次沙尘天气为研究对象,分析了PM_2.5和PM₁₀浓度、水溶性离子组分、气象条件和气溶胶光学特征,研究了长治市沙尘天气的典型污染特征和传输路径.结果表明：长治市2018年共8d为受沙尘天气影响日,其中4月份最多（5d）,这与春季大气环流调整,冷暖空气活动频繁有关.沙尘污染发生前一般受西方或西北方冷空气影响,大气层结不稳定,大气环流转为经向环流,平均风速达4m/s以上;沙尘污染过程中PM_2.5/PM₁₀均低于0.3,环境空气中粗颗粒物占比较大,水溶性离子总浓度在PM_2.5中占比下降,Ca²⁺浓度为沙尘污染发生前的4倍以上.冬季沙尘为近地面扩散传输,春夏季沙尘为高空沉降传输,影响范围大,区域传输贡献明显.长治市沙尘重要潜在源区为蒙古国、哈萨克斯坦中部和新疆中北部的荒漠地区,传输路径主要为西北路径和正北路径,其中西北路径为哈萨克斯坦—新疆中北部—内蒙古西部—长治以及新疆中北部—内蒙古西部—长治两条路径,正北路径为蒙古国—内蒙古中部—山西北部—长治.