分散法制备的CuCl/MCM-41上C3H6选择催化还原NO反应的研究

研究了由分散法制备的两种CuCl/MCM-41催化剂上丙烯在过量氧存在下选择催化还原NO反应, 发现所制备的CuCl/AlMCM-41催化剂的反应活性明显高于CuCl/SiMCM-41. XRD, IR, TPR及ESR的研究结果表明, CuCl/AlMCM-41催化剂上的主要活性中心是与骨架铝配位的铜离子(Cu2+/Cu+).     

分散法制备的CuCl／MCM—41上C3H选择催化还原NO反应的研究

研究了由分散法制备的两种CuCl/MCM-41催化剂上丙烯在过量氧存在下选择催化还原NO反应，发现所制备的CuCl/MCM-41催化剂的反应活性明显高于CuCl/SiMCM-41,XRD,IR,TPR及ESR的研究结果表明，CuCl/MCM-41催化剂上的主要活性中心是骨架铝配位的铜离子（Cu^2 /Cu^ ）。     

CuCl等在γ-Al_2O_3表面的分散及其对乙烯吸附的研究

本文研究了CuCl在γAl_20_3表面上的分散和乙烯在CuCl/γ-Al_2O_3上的吸附和程序升温脱附情况.X射线相定量法和紫外漫反射法都表明用烘烤法或浸渍法制备的CuCl/γ-Al_2O_3中CuCl在γ-Al_2O_3表面可达单层分散.X射线相定量法测得CuCl在γ-Al_2O_3表面上的最大分散量为0.095克CuCl/100米~2γ-Al_2O_3表面.吸附和程序升温脱附研究表明,分散在γ-Al_2O_3表面上的CuCl在室温常压下便可吸附乙烯,比纯CuCl吸附乙烯的能力提高千倍以上,分散后的CuCl吸附乙烯的分子比可高达0.19C_2H_4分子/Cu~ 离子.分散在γ-Al_2O_3表面上的CuCl可与C_2H_4,C_3H_6等形成表面π络合物,但要求有合适的几何环境.这些结果可供利用CuCl/γ-Al_2O_3分离含不饱和键分子时参考。     

CuCl/SiO2-TiO2 催化剂的结构及其催化甲醇氧化羰基化反应性能

 在微波辐射条件下, 将 CuCl 快速分散到载体表面制得 CuCl/SiO2-TiO2 催化剂, 利用 X 射线衍射、透射电镜、N2 吸附-脱附、热重、H2 程序升温还原和 CO 程序升温脱附对催化剂进行了表征. 结果表明, 微波辐射制备的催化剂中 CuCl 和载体发生了强相互作用, 比传统加热制备的催化剂中形成更多的易还原铜物种, 吸附 CO 的能力更强. 在甲醇液相氧化羰基化反应中, 微波辐射制备的催化剂上甲醇转化率为 11.7%, 碳酸二甲酯选择性达 96.5%, 高于相同条件下传统加热制备催化剂的活性.     

CuCl_2和HY分子筛的表面反应及Cu/Y分子筛的制备及其催化甲醇氧化羰基化（英文）

以CuCl2为前驱物与HY分子筛进行固相离子交换制备了Cu/Y催化剂,采用热重方法研究了CuCl2与HY分子筛的表面固相离子交换反应,结合活性测试表明催化剂中高度分散的CuCl和离子交换形式的Cu+物种是甲醇氧化羰基化合成碳酸二甲酯的催化活性中心.X射线光电子能谱表征和元素分析结果表明,活性金属Cu主要以CuCl形式存在于分子筛外表面,而在分子筛笼内则以交换的Cu+和少量吸附的CuCl形式存在.与以CuCl为交换铜源所制催化剂相比,以CuCl2为铜源制备的催化剂Cu含量低,催化活性更高.     

Pd(PPh3)2Cl2CuCl2/AC催化乙醇氧化羰化合成碳酸二乙酯

采用浸渍法制备了乙醇直接气相氧化羰化合成碳酸二乙酯的负载型催化剂，并在连续流动固定床反应装置上评价了催化剂的反应活性，考察了催化剂活性组分、载体、活性组分负载量等因素对催化反应活性的影响。结果表明，活性炭是较好的载体，CuCl2是较好的铜盐前驱体，添加了Pd(PPh3)2Cl2的CuCl2/AC催化剂活性更高。当Cu负载量为9.0%，Pd负载量为0.5%时，催化剂的活性较好。在优化的催化剂制备条件下，乙醇的转化率超过30%，碳酸二乙酯（DEC）的选择性达到95%。     

CuCl／SiO2-Al2O3催化剂的表面结构及甲醇氧化羰基化催化性能

通过掺杂Al对无定形层析硅胶进行表面改性,采用固体离子交换法制备了CuCl/SiO2-Al2O3催化剂,并考察了它在甲醇液相氧化羰基化合成碳酸二甲酯反应中的催化性能.结果表明,掺杂Al制备的SiO2-Al2O3载体仍保持了硅胶的无定形结构,比表面积降为200m2/g,但表面酸性明显增强,具有B酸中心.CuCl不仅分散于SiO2-Al2O3载体表面,而且与载体表面的B酸发生离子交换作用形成了表面Cu 物种,使催化剂比表面积降为148m2/g,且两种Cu 物种共同构成了催化活性中心.当CuCl/SiO2-Al2O3催化剂的Si/Al比为5,在500℃焙烧时,催化剂上甲醇氧化羰基化反应的碳酸二甲酯的选择性和时空收率分别达到74%和1.27g/(g.h).     

不同方法制备的Cu/HZSM-5催化剂上NO的催化分解反应

采用离子交换法、固相分散法和微波固相法等不同方法制备了Cu/HZSM-5催化剂,以BET、XRD和XPS等手段对催化剂样品进行了表征。结果表明,不同方法制备的Cu/HZSM-5催化剂上Cu物种的落位分布状态不同,离子交换法制备的催化剂Cu物种更多地落位于分子筛孔道内,微波固相法和固相分散法制备的催化剂Cu物种较多地落位分布在分子筛外表面。固相分散法制备的样品未能使铜物种完全分散于分子筛表面,在13.1°、16.8°、35.5°和38.0°等处仍存在CuO的晶相衍射峰。催化分解NO反应的活性考察结果表明,用微波固相法制备的催化剂催化分解NO的活性及稳定性明显超过另两种方法所制备的催化剂,在无氧条件下NO最初转化率高达89.2%,经反应25h后,转化率仍维持在70%以上;在富氧气氛下催化分解NO活性降低速率低于由离子交换法制备的催化剂。结合表征结果可以得出,落位于分子筛外表面以离子交换态形式存在的Cu物种对催化分解NO反应更为有利,而且催化稳定性更好。     

分散法制备的CuCl／ZSM—5分子筛催化上C3H6选择性催化还原NO …

研究了由分散法制备的ＣｕＣｌ／ＺＳＭ－５分子筛催化剂上丙烯在过量氧存在下选择催化还原ＮＯ反应，发现该法能使活性组份高度分散于载体上，且所制备的高负载量ＣｕＣ；／Ｈ－ＺＳＭ－５与离子交换法制备的Ｃｕ－ＺＳＭ－５相比在较低反应温度下具有更高的反应活性。     

CuCl2和HY分子筛的表面反应及Cu/Y分子筛的制备及其催化甲醇氧化羰基化

以CuCl₂为前驱物与HY分子筛进行固相离子交换制备了Cu/Y催化剂,采用热重方法研究了CuCl₂与HY分子筛的表面固相离子交换反应,结合活性测试表明催化剂中高度分散的CuCl和离子交换形式的Cu⁺物种是甲醇氧化羰基化合成碳酸二甲酯的催化活性中心。X射线光电子能谱表征和元素分析结果表明,活性金属Cu主要以CuCl形式存在于分子筛外表面,而在分子筛笼内则以交换的Cu⁺和少量吸附的CuCl形式存在。与以CuCl为交换铜源所制催化剂相比,以CuCl₂为铜源制备的催化剂Cu含量低,催化活性更高。     

Nanostructure Copper-exchanged ZSM-5 Catalytic Activity for Conversion of Volatile Organic Compounds (Toluene and Ethyl Acetate)

Gas phase catalytic oxidation of ethyl acetate and toluene was examined over copper modified ZSM‐5 catalysts under atmospheric pressure. Nanostructure of ZSM‐5 was characterized by XRD, SEM and TEM techniques. Elemental composition of ZSM‐5 was determined using EDX, ICP‐AES and XPS techniques. Results of catalytic studies showed better catalytic activity of Cu‐ZSM‐5 catalysts than those of parent ZSM‐5 and HZSM‐5, which revealed catalytic role of copper ions in the Cu‐ZSM‐5 catalysts. Effects of some parameters over catalytic conversion of these compounds were also studied. Ethyl acetate showed more reactivity than toluene over the Cu‐ZSM‐5 catalysts. Furthermore, the catalytic activity of Cu‐ZSM‐5 catalysts increased with increasing the copper loadings. The conversion behavior of a binary mixture of ethyl acetate and toluene was different from that of a single form. A promotive and inhibitive behavior was observed for conversion of ethyl acetate and toluene in the binary mixture, respectively. Water vapor as co‐feed had an inhibitive effect on conversion of organic compounds over the Cu‐ZSM‐5 catalysts.     

铜离子的引入对甲烷无氧芳构化催化剂Mo/CuH-ZSM-5中Mo物种化学状态的影响

对比考察了Mo/CuH-ZSM-5和Mo/H-ZSM-5催化剂的甲烷无氧芳构化性能,并用XRD,XPS,ESR等多种测试手段对反应前后催化剂上的Mo物种及铜助剂的价态变化进行了详细研究,发现Cu(Ⅱ)部分取代H-ZSM-5交换位上的H⁺后,抑制了活性组分MoO₃的还原,而Cu物种自身被还原,进而将这种价态变化与催化剂的活性进行了关联.     

以金属氧化物及钙钛矿结构化合物为活性组分的ZSM-5催化剂上NOx选择性还原研究

研究了在水蒸汽存在条件下,以ＮＨ３为还原剂,金属／ＺＳＭ－５催化剂和负载于ＺＳＭ－５上的钙钛矿结构催化剂上的ＮＯｘ选择性催化还原（ＳＣＲ）性能。实验结果表明,当反应气中通入水蒸汽时,各样品的催化活性均下降,同时伴随着Ｎ２选择性的增加。而Ｃｕ－ＺＳＭ－５样品却表现出独特的性能,在所有测定样品中具有最高的ＮＯｘ转化率（在４５０℃时达到６９％）,当有水蒸汽存在时,其活性没有下降,反而有所增加,４５０℃时     

NH3-SCR反应中Fe-ZSM-5的Fe物种分布和酸性位对其水热稳定性及抗硫和抗碳氢性能的影响

以Na+型和H+型ZSM-5为载体制备了Fe-ZSM-5催化剂并用于氨选择性催化还原(NH3-SCR)氮氧化物. Fe-H-ZSM-5在新鲜时和750 oC含10%水的空气中老化后,其SCR活性均优于Fe-Na-ZSM-5.表征结果显示, Fe-H-ZSM-5和Fe-Na-ZSM-5的Fe物种分布和酸性位有所不同.高温水热老化后Fe-H-ZSM-5分子筛骨架的脱铝较Fe-Na-ZSM-5严重.水和硫的存在对Fe-H-ZSM-5和Fe-Na-ZSM-5的SCR活性的影响相似,即降低了低温活性,略提高了高温活性. Fe-Na-ZSM-5表现出比Fe-H-ZSM-5更好的抗碳氢中毒性能.这两种催化剂的SO2和碳氢中毒是可逆的.     

含铜MFI分子筛的H2-TPT和O2-TPD研究

 采用H2－TPR和O2－TPD手段考察了不同金属离子交换的ZSM－5分子筛催化剂上的氢还原性能和氧脱附性能．发现Cu－ZSM－5催化剂的储氧能力及氧脱附性能优于Co－ZSM－5和Fe－ZSM－5催化剂;储氧能力强、低温下氧脱附性能好的催化剂,对NO分解反应的催化活性就高．铜离子是反应的活性中心．添加Ag和Ce可使Cu－ZSM－5催化剂上氧的脱附温度大大降低．Cu－ZSM－5／堇青石整体式催化剂上Cu的存在形式与单纯的Cu－ZSM－5有差异,整体式催化剂上的一价铜数量少,但较稳定．     

Au/Mn2O3/Al2O3催化剂的制备及其deNOx活性

由于燃煤烟气、汽车尾气的过度排放 ,大气中ＮＯｘ(其中ＮＯ占 90 %以上 )浓度已呈上升趋势。ＮＯ在阳光作用下 ,易形成光化学烟雾 ,危害人体的呼吸系统。ＮＯ还是破坏大气臭氧层和形成酸雨的前驱气体之一 ,破坏生态环境。催化分解和催化还原法是消除ＮＯ(ｄｅＮＯｘ)的主要方法。但由于实际环境中ＮＯ往往与某一种或几种还原性气体 (如ＣＯ、低碳烃 )共存 ,所以催化还原法是人们公认的有应用前景的ｄｅＮＯｘ 方法[1 ] 。近十几年来 ,国内外研究较多的ｄｅＮＯｘ 催化剂是Ｃｕ ＺＳＭ 5 ,其催化活性除受原料气中氧含量的影响外 ,很大程度上…     

Effects of Coke Deposits on the Catalytic Performance of Large Zeolite H‐ZSM‐5 Crystals during Alcohol‐to‐Hydrocarbon Reactions as Investigated by a Combination of Optical Spectroscopy and Microscopy

The catalytic activity of large zeolite H‐ZSM‐5 crystals in methanol (MTO) and ethanol‐to‐olefins (ETO) conversions was investigated and, using operando UV/Vis measurements, the catalytic activity and deactivation was correlated with the formation of coke. These findings were related to in situ single crystal UV/Vis and confocal fluorescence micro‐spectroscopy, allowing the observation of the spatiotemporal formation of intermediates and coke species during the MTO and ETO conversions. It was observed that rapid deactivation at elevated temperatures was due to the fast formation of aromatics at the periphery of the H‐ZSM‐5 crystals, which are transformed into more poly‐aromatic coke species at the external surface, preventing the diffusion of reactants and products into and out of the H‐ZSM‐5 crystal. Furthermore, we were able to correlate the operando UV/Vis spectroscopy results observed during catalytic testing with the single crystal in situ results.     

A Comparison of NO Reduction Over Mn–Cu/ZSM5 and Mn–Cu/MWCNTs Catalysts Assisted by Plasma at Ambient Temperature

Manganese–copper bimetal oxide catalysts supported on ZSM5 and acid-treated multi-walled carbon nanotubes (MWCNTs) were produced by incipient wetness impregnation for selective catalytic reduction of NO with dielectric barrier discharge plasma. Plasma can activate molecules even at ambient temperature, generating active oxygen species such as O, O₃, and HO₂ radicals, which can oxidize NO to NO₂ effectively. The SCR activity of Mn–Cu/MWCNTs was studied and compared to that of the Mn–Cu/ZSM5. The obtained samples were characterized by XRD, SEM, TEM, ICP, H₂-TPR, Raman spectroscopy, and XPS. The results show that Mn–Cu/MWCNTs catalyst possesses NO removal activity superior to that of the Mn–Cu/ZSM5 catalyst. MWCNTs-based catalyst attains NO removal efficiency of 88% at 480 J/L, while the ZSM5-supported catalyst achieves NO removal efficiency of 82% at the same energy density. The oxygen content increased from 3.33 to 19.07% on the nanotube surface after introducing Mn and Cu, which almost remained unchanged on ZSM5. The oxygen-containing functionalities are important for NO_x adsorption and removal. Moreover, the characterization revealed that CuO is the main phase of copper oxide, but copper dispersion decreases on Mn–Cu/ZSM5 surface because of the formation of copper dimer species. The manganese is well-dispersed on the catalysts, MnO₂ and Mn₂O₃ contents of Mn–Cu/MWCNTs are larger than that of Mn–Cu/ZSM5, MnO₂ is the predominant phase of manganese oxide.     

Catalytic Combustion of Ethyl Acetate over Nanostructure Cobalt Supported ZSM-5 Zeolite Catalysts

Gas phase catalytic combustion of ethyl acetate, as one of volatile organic compounds (VOC), was studied on nanostructure ZSM-5, HZSM-5 and Co-ZSM-5 with different cobalt loadings. Nanostructure of ZSM-5 was determined by XRD, SEM and TEM. Catalytic studies were carried out under atmospheric pressure in a fixed bed reactor. Results showed that the Co-ZSM-5 catalysts had better activity than others and at temperatures below 350 ℃, amount of Co loading was more effective on catalytic activity. The order of conversion of ethyl acetate over different Co loading is as follows: Co-ZSM-5 (0.75 wt%)＜Co-ZSM-5 (1.5 wt%)＜Co-ZSM-5 (15 wt%)＜Co-ZSM-5 (2.8 wt%). Besides the higher the inlet concentration of ethyl acetate, the lower the conversion yield, and oxygen concentration in catalytic oxidation conditions has not so large influence on conversion. Furthermore, the presence of water vapor in inlet gaseous feed has an inhibitive effect on ethyl acetate conversion and at the temperatures above 400˚C, the effect decreases.