Mechanism of Hg oxidation in the presence of HCl over a commercial V2O5–WO3/TiO2 SCR catalyst

Experiments were conducted in a fixed-bed reactor containing a commercial V₂O₅/WO₃/TiO₂ catalyst to investigate mercury oxidation in the presence of HCl and O₂. Mercury oxidation was improved significantly in the presence of HCl and O₂, and the Hg⁰ oxidation efficiencies decreased slowly as the temperature increased from 200 to 400°C. Upon pretreatment with HCl and O₂ at 350°C, the catalyst demonstrated higher catalytic activity for Hg⁰ oxidation. Notably, the effect of pretreatment with HCl alone was not obvious. For the catalyst treated with HCl and O₂, better performance was observed with lower reaction temperatures. The results showed that both HCl and Hg⁰ were first adsorbed onto the catalyst and then reacted with O₂ following its adsorption, which indicates that the oxidation of Hg⁰ over the commercial catalyst followed the Langmuir–Hinshelwood mechanism. Several characterization techniques, including Hg⁰ temperature-programmed desorption (Hg-TPD) and X-ray photoelectron spectroscopy (XPS), were employed in this work. Hg-TPD profiles showed that weakly adsorbed mercury species were converted to strongly bound species in the presence of HCl and O₂. XPS patterns indicated that new chemisorbed oxygen species were formed by the adsorption of HCl, which consequently facilitated the oxidation of mercury.     

Mo-Mn-ATP催化剂的脱汞性能研究

以盐酸活化凹土(ATP)为载体,采用浸渍法和变温处理法制备Mo-Mn-ATP催化剂,考察了Mo和Mn的总负载量、Mo和Mn的摩尔比、焙烧温度、反应温度等对催化剂催化氧化模拟烟气中Hg0性能的影响,并讨论了催化剂的抗硫性能。结果表明,Mo和Mn的总负载量10%、Mo和Mn的摩尔比1∶3、焙烧温度400℃、反应温度120℃时,Mo-Mn-ATP催化剂的脱汞效果最好,达96%。     

微藻热化学转化制取生物质油催化剂的研究进展

微藻生物质能源被认为是可以有效解决能源危机的第三代生物质能源。以微藻为原料,通过热化学转化的方法制取生物质油是微藻能源利用的研究热点。综述了微藻热化学转化中催化剂的研究进展,包括碱金属盐催化剂、分子筛催化剂、过渡金属催化剂等,并提出了该研究的发展方向。     

MMT对汽油机催化前后微粒排放的影响

在一台自然吸气式PFI汽油机上,开展了甲基环戊二烯三羰基锰(MMT)汽油添加剂对发动机催化前后微粒数量浓度分布、粒径分布和质量浓度分布影响的试验,并研究了不同MMT含量对催化器催化效率的影响.结果表明,随着汽油添加剂MMT含量的增加,催化前后核态和积聚态的数量浓度均增加,MMT含量为12.5 mg·L-1和17.5 mg·L-1的燃油增加显著,相对于超细微粒,经催化器后细微粒和大微粒降幅比较明显.催化前后核膜态峰值粒径基本不变,催化后的积聚态峰值粒径明显大于催化前.随着MMT含量的增加,催化后积聚态峰值粒径向催化前移动.相比于基础油,随着MMT含量的增加,催化器对总数量浓度的催化效率有所降低,但MMT的增加大幅度提高了催化器对微粒总质量浓度的催化效率.     

处理垃圾渗滤液的Fe/C空气阴极MFC性能研究

用浸渍法制得硝酸铁/活性炭粉催化剂,通过吸附法将催化剂吸附到碳毡上制作Fe/C催化剂碳毡空气阴极电极.通过改变初始活性炭粉投加量和硝酸铁浓度,考察了两者对以垃圾渗滤液为燃料的MFC产电性能影响;通过循环伏安测试,对不同硝酸铁浓度下自制阴极电极性能进行了评价;在最佳催化条件下考察了装置运行稳定性;并对不同进水COD浓度下同步产电和污水净化性能进行了研究.结果表明,随着活性炭粉投加量或硝酸铁浓度的增加,MFC产电性能均呈现先升高后降低的趋势;当活性炭粉投加量为1 g且硝酸铁浓度为0.25 mol.L-1时,电池性能最佳,功率密度为4 199.8 mW.m-3,表观内阻为465Ω;在硝酸铁和活性炭粉最佳比范围内,MFC的内阻和功率密度分别随着催化剂量的增加而减小和增加;循环伏安测试进一步表明,硝酸铁浓度为0.25 mol.L-1时放电容量最大,且性能稳定;在最佳催化条件下,随着进水COD浓度的增加,MFC产电性能增加,功率密度达5 478.92 mW.m-3,同时COD去除量也增加,最大为1 505.2 mg.L-1,垃圾渗滤液的COD去除率最大达89.1%.     

La0.8Ca0.2FeO3/MgAl2O4丝网整体催化剂用于低浓度甲烷催化燃烧

开发了涂覆在金属丝网基体上的La_(0.8)Ca_(0.2)FeO_3/MgAl_2O_4复合整体催化剂,用于低浓度甲烷(0.5%,体积分数)催化燃烧反应.首先用沉积-沉淀法制备了La_(0.8)Ca_(0.2)FO_3(LCF)钙钛矿与Mg Al_2O_4尖晶石复合的粉末催化剂LCF/Mg Al2O4,用程序升温微反应器(TPRS)测定了粉末活性,结合XRD、BET、SEM、TPR的表征结果,筛选出了最佳复合物质的量比和最适焙烧温度.当LCF与Mg Al_2O_4复合后,抗烧结能力增强,以拟一级反应速率常数(k,L·g~(-1)·s~(-1))计的活性提高了1倍左右.然后采用浆料涂覆法,在表面改性的金属丝网蜂窝基体上分层涂覆了作为第二载体的MgAl_2O_4和LCF/Mg Al_2O_4复合粉体涂层,考察了复合粉体球磨前焙烧的温度、第二载体及活性层涂覆量的影响.最后在空速GHSV=40000 h~(-1)条件下测试了甲烷催化燃烧反应的活性.与陶瓷基体相比,涂覆在金属丝网基体上的LCF/MgAl_2O_4活性在600℃时提升了48.1%.500 h长运转试验发现,催化剂活性在初期的200 h下降了20.3%,然后基本保持稳定.     

Removal of VOCs from gas streams with double perovskite-type catalysts

Double perovskite-type catalysts including La2 CoMnO_6 and La_2 CuMnO_6 are first evaluated for the effectiveness in removing volatile organic compounds(VOCs), and single perovskites(La CoO_3, LaMnO_3, and La Cu O3) are also tested for comparison. All perovskites are tested with the gas hourly space velocity(GHSV) of 30,000 hr~(-1), and the temperature range of100–600°C for C_7H_8 removal. Experimental results indicate that double perovskites have better activity if compared with single perovskites. Especially, toluene(C_7H_8) can be completely oxidized to CO_2 at 300°C as La2 Co MnO_6 is applied. Characterization of catalysts indicates that double perovskites own unique surface properties and are of higher amounts of lattice oxygen,leading to higher activity. Additionally, apparent activation energy of 68 k J/mol is calculated using Mars-van Krevelen model for C7 H8 oxidation with La2 Co Mn O6 as catalyst. For durability test, both La2 Co Mn O6 and La_2 CuMnO_6 maintain high C7 H8 removal efficiencies of 100% and98%, respectively, at 300°C and 30,000 hr~(-1), and they also show good resistance to CO_2(5%) and H2 O(g)(5%) of the gas streams tested. For various VOCs including isopropyl alcohol(C_3H_8 O),ethanal(C_2H_4O), and ethylene(C_2H_4) tested, as high as 100% efficiency could be achieved with double perovskite-type catalysts operated at 300–350°C, indicating that double perovskites are promising catalysts for VOCs removal.     

烟气脱硝装置与电厂设备运行的相互影响

火电厂烟气脱硝装置中的二氧化硫、灰分、氨及催化剂中的各种重金属在高温烟气的作用下发生各种化学作用,生成的硫酸氢氨等产物对火电厂的各种设备均会产生不同影响.同时由于系统阻力及荷载的变化,也会对电厂其他相关设备产生影响,根据目前工程的运行经验,火电厂在增设脱硝装置后,均会对空气预热器、引风机、锅炉钢架等进行改造.通过综合分析烟气脱硝装置产生的影响原因及解决办法,为脱硝装置的设计提供参考.     

La2O3—ZrO2缺陷萤石型燃烧催化剂的制备

缺陷萤石型Ｌａ２Ｏ３－ＺｒＯ２固溶体的催化燃烧活性受制备条件的影响，本文通过对其共沉淀前体的表面结构和热分解过程的分析，发现共沸蒸馏的办法可以有效地控制前体表面羟基的缩合过程，减少团聚，保持前体中金属离子均匀分散，为生成缺陷有序的烧结石型的Ｌａ２Ｚｒ２Ｏ７复氧化物提供了可能。复合氧化物固溶体的表面阳离子配置情况与样品的催化氧化性能密切相关，软团聚前体的烧结产物对甲烷燃烧反应具有更高的催化活性。     

TiO2催化超声降解月桂醇聚氧乙烯(9)醚溶液

表面活性剂随废水、废物的排放进入水体或土壤等环境,会对环境造成严重的污染.因此,有必要在其排放之前采用既安全可靠又有效的方法对其进行处理.本文采用经过600℃高温处理的锐钛矿型TiO2作为催化剂,以超声催化降解月桂醇聚氧乙烯(9)醚(AEO9)反应为模型,研究各种因素对TiO2催化超声降解的影响.结果表明,在TiO2催化剂作用下超声降解AEO9是可行的,且效果明显.在超声波功率为600 W,经600℃活化的TiO2催化剂用量为0.5～0.7g/L,AEO9水溶液初始质量浓度为60 mg/L,初始pH值为4.0的条件下,降解2 h后,AEO9降解率可达99%以上.