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501.
该废催化剂呈不规则凝聚体,比表面积大,重金属Ni占比0.49%,几乎可以全部消解溶出.国标法下Ni浸出浓度为19.862 mg/L,随着浸出液pH值的降低而迅速增加;Ni浸出量随浸出时间的增加而增大,在10 h后逐渐趋于平稳.NaH2PO4、人造沸石、NTA、乙基黄原酸钾四种稳定化药剂对重金属Ni均有较好的稳定化效果,废催化剂表面形貌特征有显著变化,乙基黄原酸钾因螯合作用而稳定化效果最佳.水泥稳定化产物中重金属Ni在酸性下容易浸出,增容比为1.18,高于药剂稳定化. 相似文献
502.
For the paper industry, the disposal and management of the yielded sludge are a considerable challenge. In our work, the paper mill sludge-derived magnetically separable heterogeneous catalyst (PMS-Fe-380) was prepared easily through a facile synthesis method. The morphology and structure of PMS-Fe-380 were fully characterized by means of X-ray diffraction, Fourier transform infrared spectroscopy, scanning electron microscopy, and Brunauer–Emmet–Teller analysis. The catalytic activity of PMS-Fe-380 was evaluated by degradation of Methylene Blue (MB). The reusability and stability of PMS-Fe-380 were evaluated in five repeated runs, which suggested that PMS-Fe-380 manifested excellent stability of catalytic activity. Moreover, leaching tests indicated that the leached iron is negligible (< 0.5 mg/L). This study provides an alternative environmentally friendly reuse method for paper mill sludge and a novel catalyst PMS-Fe-380 that can be considered as a promising heterogeneous Fenton-like catalyst. 相似文献
503.
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. 相似文献
504.
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506.
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. 相似文献
507.
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. 相似文献
508.
La2O3—ZrO2缺陷萤石型燃烧催化剂的制备 总被引:7,自引:0,他引:7
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。 相似文献
509.
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. 相似文献
510.
通过水热法合成盘状ZnO,并在其表面负载Cu得到Cu/盘状ZnO模型催化剂,将不同气氛下(5%CO/Ar、2.5%H_2/2.5%CO/Ar、5%H_2/Ar,分别记为CZ-5CO、CZ-2.5H_2-2.5CO、CZ-5H_2)还原的模型催化剂用于逆水煤气变换反应.对催化剂进行热重分析(TGA)、X射线衍射(XRD)、扫描电子显微镜(SEM)、X射线光电子能谱(XPS)、原位紫外拉曼光谱(in situ UV-Raman)表征.结果表明,不同的还原气氛可得到不同尺寸的Cu颗粒及不同缺陷浓度的Cu-ZnO界面.CO_2程序升温脱附(CO_2-TPD)结果表明,不同的Cu-ZnO界面具有不同的CO_2活化能力.其中CZ-5H_2形成的Cu-ZnO界面对CO_2活化能力最强,表现出最佳的逆水煤气变换反应活性;CZ-5CO具有更多的表面缺陷可能是由于存在Cu_3Zn合金,但Cu-ZnO界面上CO_2的吸附容量降低,导致逆水煤气变换反应活性低;CZ-2.5H_2-2.5CO的活性介于CZ-5H_2与CZ-5CO之间,界面对CO_2的活化量也介于两者之间. 相似文献