火花放电条件下CS_2转化为COS的反应

利用火花放电技术模拟研究了自然界闪电作用下CS₂转化为COS的反应. 结果表明, 放电条件(电压3000 V)下CS₂(初始分压为1.33×10³ Pa)能与空气(25 ℃, 10³ Pa)中的氧气、水蒸气作用, 转化为COS以及其他含硫含碳产物(CO、CO₂、SO₂等); CS₂初始分压、水蒸气和放电时间等因素对COS生成量有明显的影响. 并在实验基础上结合多种理论, 探讨了相关过程的大气闪电反应机理. 这些结果可为自然界闪电条件下的硫循环、碳循环过程的研究提供重要依据.     

CeO2-La2O3/γ-Al2O3稀土氧化物混合物催化还原SO2的实验研究

在La₂O₃ 中加入变价稀土氧化物CeO₂,组成一种稀土氧化物的混合物,以这种混合物作为CO还原SO₂的催化剂.采用连续流动固定床反应器,在反应气体SO₂和CO按SO₂∶CO = 1∶3,载流气体为N₂,气体流量为1000 mL/min的条件下,实验研究了该催化剂的活化过程以及温度和反应物浓度配比对活化反应的影响,用XRD和XPS对反应前后催化剂进行了表征,分析了相结构的变化.结果表明:CeO₂和La₂O₃ 2种稀土氧化物的混合物,在CO还原SO₂的催化反应中,活化温度比单个的CeO₂或La₂O₃氧化物下降了50℃～100℃,而且具有更高的活性.这可能是CeO₂和La₂O₃氧化物之间存在着某种协同作用所致.     

小麦田中有机硫气体的释放

采用密闭箱法对不同施肥条件下小麦田中羰基硫(COS)、二硫化碳(CS₂)和二甲基硫(DMS)的释放情况进行了监测.结果表明,小麦生长过程对COS、CS₂和DMS释放影响显著,小麦对COS有明显吸收作用,DMS和CS₂是麦田中释放的主要含硫气体.COS和CS₂释放速率昼夜变化明显.仅施用有机肥的麦田,硫释放总量高于其它田块.不同施肥条件的田块,硫释放总量范围在-1.40～0.79mg·ml^-2之间.     

CO2和O3浓度倍增及复合效应对大豆生长和产量的影响

利用OTC-1型农田开顶式气室,模拟研究了大气中CO₂、O₃浓度倍增及其复合效应对大豆生长、根瘤和产量形成的影响.结果表明,CO₂浓度倍增促进根系生长,固氮能力增强,植株高度和基部粗度增加,对发育期、绿叶数和绿叶面积影响不大.O₃浓度倍增抑制大豆根系和茎的生长,固氮能力下降,叶片伤害使绿叶数和绿叶面积显著下降, 衰老提前.在CO₂和O₃的复合试验中,CO₂浓度增加明显缓解O₃浓度增加对大豆伤害和抑制作用,CO₂、O₃浓度持续倍增处理下大豆生长和固氮能力与CK的数量差异明显小于单一O₃浓度倍增与CK 的数量差异,逐渐增加CO₂、O₃浓度的刺激作用和剂量效应使大豆生长后期伤害加重,绿叶数、绿叶面积显著下降,而根系固氮能力有所提高.     

铜锰镧铈复合催化剂的制备及其降解对二甲苯的机制

采用溶胶凝胶法制备了镧掺杂的铜锰镧铈催化剂,研究了其对对二甲苯的催化性能.通过BET、SEM、H₂-TPR、XRD和XPS等对不同元素比例的催化剂进行表征,探讨了催化剂结构和性能的关系;同时,研究了不同影响因素（初始浓度、空速、O₂含量和混合物）对其催化氧化性能的影响;最后,利用FT-IR、XRD和 GC-MS对降解产物进行分析,探究了其催化降解对二甲苯的机理.结果表明,La掺杂增加了催化剂的比表面积和孔体积,以及表面氧含量,抑制了晶体形成,增强了催化活性.Cu-Mn-La-Ce（1：2：1：1）催化剂性能最好,在初始浓度为600 mg·m^-3,空速为15000 h^-1,20% O₂的条件下,其T₉₀为230 ℃.对二甲苯的降解率随着初始浓度、空速的增加而降低,随着O₂含量的增加而增加.气流中混入苯提高了对二甲苯的降解率.对二甲苯催化反应后催化剂表面的 O—H、C＝O、C—H和金属—氧键都相应减少,降解中间产物主要为对甲基苯甲醛和对甲基苯甲酸.降解反应涉及MVK机理,对二甲苯先氧化成对甲基苯甲醛,再氧化成对甲基苯甲酸,最终生成CO₂、H₂O.     

柴油表征燃料在高浓度CO2氛围下燃烧机理的分析

为研究高浓度CO₂在高温高压情况下对柴油燃烧特性的影响,提出了柴油表征燃料在CO₂/O₂氛围下的燃烧反应机理.通过量子化学计算了化学反应路径并对反应路径进行分析,最后进行柴油表征燃料燃烧的仿真.通过搭建定容燃烧弹试验台架和可视化系统进行试验与仿真分析,结果表明：在50% CO₂+50% O₂氛围下,对仿真与实验的火焰燃烧极限长度和火焰纵截面面积进行对比,最小误差分别为0.39%和0.64%,最大误差分别为8.54%和4.94%,说明此机理适用于高浓度CO₂氛围下柴油燃烧特性的研究;CO₂的化学效应在柴油表征燃料燃烧时具有促进作用,CO₂在2600 K时发生热解,热解产物CO与H自由基等发生反应可以生成着火促进剂·OH;柴油在50% CO₂+50% O₂、43% CO₂+57% O₂和35% CO₂+65% O₂氛围下的燃烧效率比空气氛围分别提高了28.2%、30.4%和33.3%.     

夏季东海挥发性硫化物的空间分布与释放通量研究

挥发性硫化物（volatile sulfur compounds,VSCs）是大气中一类重要的痕量活性气体,对全球硫循环和气候变化有着重要的影响.于2018年6—7月运用冷阱捕集气相色谱和气-质联用法测定了东海海水与大气中3种重要的VSCs即羰基硫（carbonyl sulfide,COS）、二甲基硫（dimethyl sulfide,DMS）、二硫化碳（carbon disulfide,CS₂）的浓度,分析了其与相关环境因子的相关性,并估算了它们的海-气通量.研究结果表明,夏季东海表层海水中COS、DMS和CS₂的浓度平均值分别为（0.47±0.33）、（4.46±4.52）和（0.13±0.07） nmol·L^-1,海水中COS和CS₂的高值区出现在长江口附近海域,DMS在东海南部海域的浓度远低于北部海域.大气中COS、DMS和CS₂的浓度平均值分别为（564.0±37.5）×10^-12、（70.7±83.5）×10^-12和（177.6±232.3）×10^-12（以体积分数计）,COS分布均匀,CS₂的分布呈现近岸高远海低的特点,而DMS的分布受海-气扩散的影响.相关性分析表明,夏季东海海水中COS和CS₂与海水中的营养盐存在正相关关系,这可能是因为营养盐能促进浮游植物生长,而浮游植物生长过程中能释放COS和CS₂的前体进入水体,从而促进COS和CS₂的生产.此外,夏季东海中COS、DMS和CS₂的海-气通量平均值为（1.05±1.13）、（9.21±9.49）和（0.24±0.22）μmol·m^-2·d^-1,表明夏季东海是大气中3种VSCs的源.     

DBD技术脱除恶臭气体H2S和CS2的可行性

采用DBD技术脱除工业废气中的H₂S和CS₂.12kV的电压下,分压为4kPa的H₂S,放电5s,去除率接近100%;分压为1.33kPa的CS₂,放电15s,其去除率可达80%.H₂S和CS₂的去除率都随其浓度的增加而下降.在实验室研究的基础上,设计了废气处理量为420m³/h、流速为10m/s的DBD净化装置,进行了实际含H₂S和CS₂的工业废气净化研究,H₂S去除率可达89%,能量消耗为5.2W·h/m³.结果表明DBD技术对于处理含硫恶臭工业废气,具有实际应用价值.     

Radioactive tracer of the photochemical reaction of 14CS2 with OH in the presence of O2

The photochemical reaction of¹⁴CS ₂ with OH has been studied．The results indicated that the main products of the reaction were¹⁴COS and ¹⁴CO with a small amount of ¹⁴CO₂ in the reaction system(¹⁴CS₂-H₂O₂-C₃H₈-N₂-O₂>)．The reaction was promoted by oxygen．¹⁴COS and ¹⁴CO had the similar kinetic curves while ¹⁴CO₂ got a different kind of Curve．The overall rate constant increased with the increasing of oxygen partial pressure．The rate constant for the removal of ¹⁴CS₂ was K=3.4×10^-12cm³/(mO1.s) at 33330 Pa 0₂．The conversion of ¹⁴CS₂ to ¹⁴CO₂ at room temperature was observed and the possible mechanism of the photochemical reaction was disscussed．     

水质对UV/H2O2降解17α-乙炔基雌二醇（EE2）的影响

采用UV/H₂O₂间歇式光氧化反应器,研究了溶液pH值、腐殖酸及水中常见阴离子HCO₃^-、NO₃^-、CO₃^2-、Cl^-和SO₄^2-对UV/H₂O₂工艺降解17α-乙炔基雌二醇(EE2)的影响.结果表明,UV/H₂O₂工艺可以有效地去除水中的EE2,光降解过程符合一级反应动力学模型.双氧水投加量为5 mg/L时,在14W低压汞灯照射下,EE2在自来水和蒸馏水中的光降解一级反应速率常数为0.063 0min^-1和0.132 4min^-1.溶液中的腐殖酸和阴离子HCO₃^-、NO₃^-、Cl^-、SO₄^2-对EE2的光降解反应有抑制作用,4种阴离子浓度为5 mmol/L时,抑制作用依次为HCO₃^->SO₄^2->Cl^->NO₃^-,HCO₃^-可使光降解速率常数降低到50%.自来水中的光降解速率常数低于蒸馏水中的光降解速率常数是水中多种离子影响的结果.     

在氧化和还原氛围下脉冲电晕法降解二硫化碳废气

采用线-筒式脉冲电晕反应器对二硫化碳(CS2)模拟废气的去除效果进行了实验研究.实验以氩气为载气,考察了氧气和氢气对CS2去除效果的影响.结果表明CS2的去除率随脉冲电压升高而增大;氧气能够促进CS2的氧化分解,CS2去除率可达97%;有氧气存在时,CS2的最终氧化分解产物为CO、CO2、COS和SO2;当添加氢气时,反应产物主要为H2S和CH4.当反应器内筒表面加Ca(OH)2吸收剂时,CS2去除率有小幅度提高,同时气体产物中未检测到SO2和H2S,表明CS2的分解产物SO2和H2S气体被反应器中的Ca(OH)2吸收.实验还发现水汽的存在不利于CS2的氧化分解     

外源含硫化合物对土壤挥发性有机硫化合物交换通量的影响

通过静态箱采样和Entech7100预浓缩仪-GC-MS分析了半胱氨酸、硫化钠和硫酸钠对土壤吸收或释放羰基硫（COS）、二甲基硫醚（DMS）、二硫化碳（CS2）和二甲二硫醚（DMDS）等4种挥发性有机硫化合物（VOSCs）的影响.结果表明,添加半胱氨酸后,土壤由COS和CS2汇转变为源,DMS和DMDS通量显著增加,且...     

基于碳捕集的富氧燃煤烟气联合脱硫脱硝试验研究

富氧燃煤烟气压缩液化CO2的高压低温工况为NO氧化为易溶于水的NO2提供了十分有利的条件.基于小型高压吸收试验装置,采用配制的富氧燃煤模拟烟气,在高压常温下进行了NO、SO2、O2与H2O的吸收反应试验.根据反应前后的气液产物分析,测定了不同组分比例与不同压力下混合气体中NO与SO2的转化率.NO氧化与吸收试验表明,NO转化为HNO3的比率随压力升高而增加,在0.5 ～2 MPa之间增加很快,在2 ～3 MPa之间增速趋丁平缓,压力达3 MPa以上时,90％以上的NO均转化为稀硝酸,且初始NO浓度越高,NO的转化率越大.混合气体中同时存在5O2与NO的联合吸收试验发现,只有少量的NO转化成了NO3-,SO2向H2SO4的转化率随压力升高而增加,初始SO2浓度越大,转化率越高.分析表明,SO2与NO同时存在时SO2先行转化为SO3,NO充当了催化剂,但SO2转化为SO3的一次转化率小于35％,反应酸液产物的多次循环能使SO2的转化率达到90％以上.建议的工艺流程中需采用两座吸收反应塔顺序脱除SO2与NO并回收稀酸溶液,有望在富氧燃煤发电捕集CO2系统中降低脱硫脱硝成本,部分地弥补富氧燃烧机组发电成本的增加.     

过氧化氢存在下HCFC－22光解特性

模拟大气条件研究了ＨＣＦＣ－２２＋Ｈ２Ｏ２在有氧或无氧存在下用低压相进行辐照,在２０ｍ的长光程池中用富里叶红外光仪测量其化学产物,结果表明在没有氧情况下产物为ＣＯＦ２,ＣＯ２,ＨＦ和ＨＣｌ;有氧存在时产物为ＣＯ２,Ｈ２Ｏ,ＨＦ和ＨＣｌ。从这些产物推广其可能的光解机理。     

Vertical distributions of COS,CS2, DMS and other sulfur compounds in a loblolly pine forest

Measurements of atmospheric COS, CS₂, DMS, SO₂ and aerosol sulfate and methanesulfonate (MSA) concentrations were conducted in a loblolly pine forest in central Georgia between July and September 1990. The daytime profiles obtained for the reduced sulfur gases (COS, CS₂, DMS) often showed significantly higher concentrations at the canopy level than above the forest canopy, indicating a net emission of these gases from the tree tops. No evidence was found for a net uptake of COS by the canopy during daytime. With one exception, all COS concentrations measured during the day were significantly higher than corresponding nighttime values. These results appear to be in conflict with recent studies suggesting a net uptake of atmospheric COS by plants during photosynthetic activity. Possible explanations for these different findings are discussed. Nighttime profiles indicated no major biosphere-atmosphere exchange of COS, CS₂ or DMS. Nighttime DMS concentrations were significantly higher than corresponding daytime values. A clear inverse relationship between the diel variations of DMS and MSA was observed, consistent with rapid photochemical oxidation of DMS under the given conditions.     

放射示踪法研究O2存在时14CS2与OH的光化学反应

用放射示踪法研究~(14)CS_2和OH的光化学反应,指出氧对反应有促进作用,在反应体系中(~(14)CS_2-H_2O_2-C_3H_8-N_2-O_2)主要产物为O~(14)CS,~(14)CO及少量~(14)CO_2。O~(14)CS和~(14)CO有相似的动力学曲线,~(14)CO_2则是另一种情况。总反应速率常数随氧压增加而增大,在氧压为33330Pa时,~(14)CS_2消失的总速率常数可高达3.4×10~(-12)cm~3mol~(-1)S~(-1)。在实验中观察到~(14)CS_2能在室温下转变为~(14)CO_2的现象。讨论了光化学反应的历程。     

Photochemical production of carbonyl sulfide, carbon disulfide and dimethyl sulfide in a lake water

Photochemical production of carbonyl sulfide(COS),carbon disulfide(CS_2) and dimethyl sulfide(DMS) was intensively studied in the water from the Aohai Lake of Beijing city.The lake water was found to be highly supersaturated with COS,CS_2 and DMS,with their initial concentrations of 0.91 ± 0.073 nmol/L,0.55 ± 0.071 nmol/L and 0.37 ± 0.062 nmol/L,respectively.The evident photochemical production of COS and CS_2 in the lake water under irradiation of 365 nm and 302 nm indicated that photochemical production of them might be the reason for their supersaturation.The similar dependence of wavelength and oxygen for photochemical production of COS,CS_2 and DMS implied that they might be from the same precursors.The water cage effect was found to favor COS production but inhibit CS_2and DMS formation,indicating that COS photochemical production was mainly from direct degradation of the precursors and the formation of CS_2 and DMS needed intermediates via combination of carbon-centered radicals and sulfur-centered radicals.The above assumptions were further confirmed by simulation experiments with addition of carbonyls and amino acids(cysteine and methionine),and the photochemical formation mechanisms for COS,CS_2 and DMS in water were derived from the investigations.     

Removal of phosphorus and sulfur from yellow phosphorus off-gas by metal-modified activated carbon

In order to provide comprehensive utilization of high concentration CO for mono-carbon (C1) chemical industry, the purification of yellow phosphorus off-gas is of great concern. In this research, activated carbon (AC) modified by different impregnants were used for removal of PH₃, H₂S, SO₂, COS, and CS₂ in yellow phosphorus off-gas. For the removal of PH₃, AC impregnated with 0.10 mol L⁻¹ CuAc₂ was proved to be the best adsorbent. And removal efficiency of H₂S could be significantly enhanced by AC impregnated with 7% Na₂CO₃. The results of plant experiments suggested that the total concentration of the impurities in yellow phosphorus off-gas was less than 1 mg Nm⁻³ after purification operation. The metal-modified activated carbon (MMAC) was systematically characterized in terms of XPS, TGA, and DTA. The adsorption reaction mechanism was also investigated. As a result, the yellow phosphorus off-gas purified in this study can be used as a raw material gas in the C1 chemical industry.     

Influence of SO2 in incineration flue gas on the sequestration of CO2 by municipal solid waste incinerator fly ash

The influence of CO2 content and presence of SO2 on the sequestration of CO2 by municipal solid waste incinerator(MSWI) fly ash was studied by investigating the carbonation reaction of MSWI fly ash with different combinations of simulated flue gas.The reaction between fly ash and 100% CO2 was relatively fast;the uptake of CO2 reached 87g CO2/kg ash,and the sequestered CO2 could be entirely released at high temperatures.When CO2 content was reduced to 12%,the reaction rate decreased;the uptake fell to 41g CO2/kg ash,and 70.7% of the sequestered CO2 could be released.With 12% CO2 in the presence of SO2,the reaction rate significantly decreased;the uptake was just 17g CO2/kg ash,and only 52.9% of the sequestered CO2 could be released.SO2 in the simulated gas restricted the ability of fly ash to sequester CO2 because it blocked the pores of the ash.