A Study of Sulfur Dioxide in Photochemical Smog I. Effect of SO2 and Water Vapor Concentration in the 1-Butene/NOx/SO2 System

There is an appreciable chemical interaction between SO₂ and photochemical smog which depends on the concentration of SO₂ and water vapor. The rate of decay of SO₂ concentration is greatly increased in the presence of photochemical smog. With 0.75 ppm SO₂, a light-scattering aerosol is produced in dry systems and systems at 22 and 55% relative humidity (RH). Aerosol is not observed until after the NO₂ peak has been reached and the NO concentration has fallen to a very low value. The formation of aerosol corresponds in time to the region of most rapid decrease in the SO₂ profile. In systems at 65% RH or with smaller amounts of SO₂, no light scattering is observed, but the percentage of SO₂ disappearing is greater. In relatively dry systems the presence of SO₂ results in a general slowing down of the photochemical smog reactions. In systems containing water vapor concentrations comparable to those found in the atmosphere, the inhibiting influence of SO₂ on the smog reaction is less pronounced. However, the maximum concentration of oxidant produced by the photochemical smog reactions is significantly lower when SO₂ is present.     

Summary of the 1991 EPRI/EPA/DOE SO2 Control Symposium

The 1991 SO₂ Control Symposium was held December 3-6, 1991, in Washington, D.C. The symposium, jointly sponsored by the Electric Power Research Institute (EPRI), the U.S. Environmental Protection Agency (EPA), and the U.S. Department of Energy (DOE), focused attention on recent improvements in conventional sulfur dioxide (SO₂) control technologies, emerging processes, and strategies for complying with the Clean Air Act Amendments of 1990. Its purpose was to provide a forum for the exchange of technical and regulatory information on SO₂ control technology. Over 800 representatives of 20 countries from government, academia, flue gas desulfurization (FGD) process suppliers, equipment manufacturers, engineering firms, and utilities attended. In all, 50 U.S. utilities and 10 utilities in other countries were represented. In 11 technical sessions, a diverse group of speakers presented 111 technical papers on development, operation, and commercialization of wet and dry FGD, Clean Coal Technologies, and combined sulfur dioxide/nitrogen oxides (SO₂/NO_x processes.     

NH4+, NO3−, and SO42− in roadside and rural size-resolved particles and transformation of NO2/SO2 to nanoparticle-bound NO3−/SO42−

This study investigates ammonium, nitrate, and sulfate (NH₄⁺, NO₃^?, and SO₄^2?) in size-resolved particles (particularly nano (PM_0.01–0.056)/ultrafine (PM_0.01–0.1)) and NO_x/SO₂ collected near a busy road and at a rural site. The average (mass) cumulative fraction of secondary inorganic aerosols (SO₄^2?+NO₃^?+NH₄⁺) in nano or ultrafine particles at the roadside was found to be three to four times that at the rural site. The above three secondary inorganic aerosol species were present in similar cumulative fractions in particles of size 1–18 μm at both sites; however, dissimilar fractions were observed for Cl^?, Na⁺, and K⁺. The nitrogen ratios (NRs: NR = NO₃^??N/(NO₃^??N + NO₂–N)), sulfur ratios (SRs: SR = SO₄^2??S/(SO₄^2??S + SO₂–S)), dNR/D_P (derivative of NR with respect to D_P (particle diameter)), and dSR/D_P (derivative of SR with respect to D_P) at the roadside were higher than those at the rural site for nano/ultrafine particles. At both sites (particularly the roadside), the nanoparticles had significantly higher dNR/D_P and dSR/D_P values than differently sized particles, implying that NO₃^?/SO₄^2? (from NO₂/SO₂ transformation or NO₃^?/SO₄^2? deposition) were present on these particles.     

Sensitivity of Native Desert Vegetation To SO2 and to SO2 and NO2 Combined

Interest in air pollution injury to native vegetation has been generated with the construction and planned construction of large coal-fired power plants near the coal reserves in the southwest desert areas of the United States. Since information on the effects of SO₂ on these native species was not available in the literature, fumigation studies were conducted with portable chambers placed over native species in the field with SO₂ and SO₂ + NO₂. Pollutant concentrations were measured and controlled with instruments located in a mobile laboratory. Each fumigation was of two hours duration and the concentration ranged from 0.5 to 11 ppm SO₂ and from 0.1 to 5 ppm NO₂. Concentrations of SO₂ above 2 ppm were required to cause injury to all but a few of the 87 species studied. Many of the native desert species proved to be highly resistant to injury from these gases.     

锅炉烟气联合脱硫脱氮技术

硫氧化物和氮氧化物是燃煤锅炉排放的主要污染物 ,传统分步脱硫脱氮设备昂贵且效率不高 ,而联合脱硫脱氮技术具有很大的优越性 ,如可以减小系统的复杂性、具有更好的运行性能、较低的成本及较小的占地面积 ,因此实现在一个系统内同时脱硫脱氮的工艺成为国内外烟气净化技术的研究重点。对近年来国内外各种联合脱硫脱氮技术的脱除原理、研究现状、应用情况和主要优缺点进行了论述 ,并对各工艺的经济技术指标给予了多方面的比较。通过对两类烟气联合脱硫脱氮技术 (炉内联合脱除和烟气中联合脱除 )的分析、综合和比较 ,找出了我国今后脱硫脱氮技术的研究重点 ,从而为脱硫脱氮技术的进一步开发和改进提供参考     

电化学法去除SO2/NOX的研究进展

本文对采用电化学方法去除SO2/NOx废气这一新的研究方法进行了综述.在用酞花青钴(CoPc)修饰的碳气体扩散电极上,SO2在空气中的体积百分数在20%以下时可以完全被氧化为硫酸,以连二硫酸盐(S2O2-4)作还原剂,Fe2+-EDTA作络合剂时,NO以90%以上的程度还原为NH+4与NH2(SO3H)等低价含氮化合物,产物中未见N2、N2O与NO2等气体,氧化产物SO2-3(或HSO-3)在Pb阴极上还原再生为S2O2-4.用Ce4+作氧化剂可将SO2/NO2氧化为相应的酸,还原产物Ce3+经电解氧化后循环使用.     

电化学法去除SO2/NOX的研究进展

本文对采用电化学方法去除SO2/NOx废气这一新的研究方法进行了综述.在用酞花青钴(CoPc)修饰的碳气体扩散电极上,SO2在空气中的体积百分数在20%以下时可以完全被氧化为硫酸,以连二硫酸盐(S2O2-4)作还原剂,Fe2+-EDTA作络合剂时,NO以90%以上的程度还原为NH+4与NH2(SO3H)等低价含氮化合物,产物中未见N2、N2O与NO2等气体,氧化产物SO2-3(或HSO-3)在Pb阴极上还原再生为S2O2-4.用Ce4+作氧化剂可将SO2/NO2氧化为相应的酸,还原产物Ce3+经电解氧化后循环使用.     

Tolerance to SO2, NO2 and their mixture in Plantago major L. populations

The possible evolution of tolerance to NO2, alone or in combination with SO2 was investigated in three populations of Plantago major L., originating from Hyde Park in central London (polluted site), Ascot (clean site) and The Netherlands. Screening for sensitivity to the pollutants was carried out by means of chronic fumigations with NO2 or NO2 plus SO2 and acute fumigations with SO2, NO2 or their mixture. The Hyde Park population showed smaller growth reductions induced by the pollutant mixture, than did the other populations. In contrast no differential response in terms of foliar injury was observed after an acute fumigation with SO2+ NO2, but the Hyde Park population was the most sensitive to NO2 alone. The results indicate that selection for tolerance to SO2 does not confer tolerance to NO2 alone or the pollutant mixture.     

大气二氧化硫浓度的光学测定方法

介绍了测定二氧化硫浓度的几种光学方法 ,指出了目前一些化学方法的局限性 ,特别对紫外荧光法的原理、二氧化硫的吸收光谱以及荧光光谱进行分析探讨 ,设计了实验分析系统 ,得出该方法具有操作简单、灵敏度高、可实时在线的智能化优点 ,将会成为今后研究的主导方向。     

固体超强酸SO4^2-／TiO2-SnO2／Ce^4＋光催化降解含酚废水

采用共沉淀-浸渍法制备了固体超强酸SO4^2-／TiO2-SnO2／Ce^4＋，并用XRD、SEM等方法对其结构进行了表征。以苯酚的光催化降解为反应模型，确定了最佳的工艺条件和催化剂再生方法。结果表明：在pH值为6，苯酚初始浓度为50mg／L，催化剂投加量4g／L，光照距离12cm，光照时间为150min，降解率达67．73％，添加助催化剂H2O2后，反应60min，苯酚降解率达到86．33％，催化剂的最佳再生方法是先用1mol／L的硫酸浸渍24h后，在450℃下焙烧6h。     

固体超强酸SO24-/TiO2-SnO2/Ce4+光催化降解含酚废水

采用共沉淀-浸渍法制备了固体超强酸SO42-/TiO2-SnO2/Ce4+,并用XRD、SEM等方法对其结构进行了表征.以苯酚的光催化降解为反应模型,确定了最佳的工艺条件和催化剂再生方法.结果表明:在pH值为6,苯酚初始浓度为50mg/L,催化剂投加量4 g/L,光照距离12 cm,光照时间为150 min,降解率达67.73％,添加助催化剂H2O2后,反应60 min,苯酚降解率达到86.33％,催化剂的最佳再生方法是先用1 mol/L的硫酸浸渍24 h后,在450℃下焙烧6h.     

La2O3-CeO2/γ-Al2O3催化剂还原脱硫耐氧特性及其反应机理研究

用浸渍法制备了一系列稀土催化剂,研究了其催化CO还原SO2为单质硫的耐氧特性及影响其耐氧性能的主要因素,运用XRD技术分析了催化剂物相的变化及脱硫产物成分.结果表明,12% La2O3-8% CeO2/γ-Al2O3复组分催化剂比其他La2O3-CeO2/γ-Al2O3催化剂具有更好的耐氧性能;脱硫温度、催化剂用量、SO2与CO的摩尔比等对催化剂的耐氧性能均有明显的影响.最后,探讨了稀土催化剂脱硫机理,并分析在有O2条件下,引起脱硫率下降的原因是反应过程中O2与CO、S发生了竞争性反应.     

中国SO_2排放对日本SO_2浓度及硫沉降的影响

利用相关文献及来自酸沉降网的中、日两国各观测站点的SO2监测资料,分析了近十年来中国SO2的污染现状、趋势及排放量对下风向日本各观测站点SO2浓度及硫沉降量的影响。结果表明,通过文献分析可知,2001—2009中国的SO2年均质量浓度分布在40~50μg/m3,总体呈下降趋势;中国部分城市的SO2年均浓度与中国SO2排放量的相关性总体高于日本各观测站点的SO2年均浓度与中国SO2排放量的相关性,中国的SO2排放对日本各观测站点的SO2年均浓度影响总体较小;情景模拟分析发现,中国SO2排放量对日本各观测站点SO2年均浓度的贡献率在7.5%~44.0%,平均贡献率为22.6%;中国SO2排放量对日本各观测站点硫沉降的贡献率在8%~41%,平均贡献率为22.1%。     

COS,CS2 and SO2 in aluminium smelter exhaust

Measurements of carbonyl sulfide (COS) and carbondisulfide (CS₂) were carried out on samples drawn from a smoke stack of an aluminium smelter. Volume mixing ratios of 6 ppm COS and 0.1 ppm CS₂ were measured for gases from the electrolysis unit that had previously passed an Al₂O₃ fluid bed reactor and electrostatic precipitators. Specific emissions of 1.6 kg COS and 0.03 kg CS₂ per ton of primary aluminium were found. Extrapolating from this particular smelter’s conditions to a world mix specific COS emissions of about 4 kg/t(Al) are calculated resulting in emissions of annually 0.08 Tg COS into the atmosphere due to electrolytic aluminium production in 1995. Besides the photochemical conversion of anthropogenic CS₂ aluminium production is established to be the second major industrial source of COS probably exceeding automotive tire wear’s and coal combustion’s contributions.     

Use of high-resolution MM5/CALMET/CALPUFF system: SO2 apportionment to air quality in Hong Kong

Recent research has highlighted the substantial health-related costs of air pollution in the Hong Kong Special Administrative Region (HKSAR) and the potential threat from air pollution to HKSARs economic competitiveness. In order to address the air pollution problems, this paper seeks to analyse the individual contributions of major sulphur dioxide (SO₂) sources in the Pearl River Delta Region (PRDR) (Pearl River Delta + HKSAR) on the air quality in the HKSAR. This study employed the coupling of the MM5/CALMET system with the CALPUFF, the multi-layer, non-steady-state puff dispersion model, where major power plants, marine vessels and vehicles, all in the PRDR, are taken into account. The observation data and simulation results at 11 Hong Kong Environmental Protection Department (HKEPD) general (non-road-side) stations are analyzed. Urban (in-zone) and Rural (out-zone) stations are defined in order to examine the SO₂ contribution of different emission sources in different regions of the HKSAR. The model results show that the contribution of the HKSAR marine sources is significant both in summer and in winter, especially for the locations around the in-zone stations (in general 60%, and 55% in summer and winter respectively). In addition, the contribution of the HKSAR power plants is slightly higher than that of the PRD power plants in early summer, with a contribution difference of up to 20% when the prevailing wind is from the south. However, in late summer, this situation reverses. In winter, the contribution of the PRD power plants is two to three times greater than that of the HKSAR power plants. Moreover, Yantian port affects the northern part of the HKSAR when a northeasterly wind dominates the HKSAR. In order to solve these air pollution problems, the main implication of these results suggests that the HKSAR government, in close co-operation with the Guangdong government, needs to take immediate action.     

在Ru/Al2O3催化剂上用H2对SO2选择性催化还原的研究

本文对用H2来使SO2选择性催化还原为单质硫在Ru/Al2O3催化剂上的行为进行研究.当物料比经过优化确定为SO2/H2=12.8时,在500℃下,SO2的转化率为90%以上,单质硫的产率为70%左右.比较于其他的催化还原SO2的催化剂,本催化剂采用金属而不是金属硫化物,这样既省去了催化剂预硫化的过程,同时也使在有氧条件下的选择性催化还原成为可能.实验考察了O2及水蒸气存在对过程的影响.在实验过程中发现,H2S作为中间产物生成,可推论该过程在催化剂上分两步进行SO2首先在催化剂金属上被H2深度还原为H2S,然后在Al2O3载体的酸性中心上SO2与H2S发生Claus反应产生单质硫.     

Na-Ba/γ-Al2O3的NO和SO2吸附性能研究

研究了Na-Ba/γ-Al2O3吸附催化剂上NO和SO2的吸附-脱附性能.Na、Ba质量分数分别为6.2%、5.4%,焙烧温度和焙烧时间分别为600 ℃和10 h,吸附温度为100 ℃,其对NO、SO2的最大吸附量分别为0.052 4、0.344 mmol/g.同时考察了添加第三活性组份的影响,结果表明,Fe最为有效,Na-Ba/Fe/γ-Al2O3的NO、SO2最大吸附量分别为0.062 4、0.486 mmol/g.漫反射红外光谱研究结果表明,Fe降低了硫酸盐分解温度,促进吸附催化剂的再生.