丙烷在负载型催化剂上脱氢反应的研究——Ⅷ.丙烷在负载型金属催化剂上临氢脱氢

通过对丙烷在负载型金属催化剂上临氢脱氢反应性能的考察,发现除负载型Pt、Pd等具有脱氢活性外;负载型Cu也同样具有脱氢活性,并且随Cu载量增加而升高。对催化剂稳定性研究结果表明,载体与金属组分间相互作用是不容忽视的因素之一。催化剂选择性影响因素主要是加氢裂化或氢解反应。因此,对催化剂脱氢选择性的改善既可通过调变金属组分的脱氢加氢性能,也可通过改变载体酸性进行。     

载体组成对负载型PtSn/ZSM-5催化剂上丙烷脱氢反应性能的影响

用微型催化反应装置结合吡啶吸附的红外光谱、NH3-程序升温脱附、热重、H2化学吸附和程序升温还原等物理化学手段研究了载体组成对负载型PtSn/ZSM-5催化剂上丙烷脱氢反应性能的影响.结果表明,负载型PtSn/ZSM-5催化剂对丙烷脱氢的催化性能与载体组成密切相关.随着ZSM-5载体中SiO2/Al2O3比的增加,催化剂表面的酸中心总量和强酸中心量逐渐减少.当SiO2/Al2O3摩尔比从45增至108时,催化剂对丙烷脱氢反应的催化活性提高,并且催化剂的积炭量下降.当SiO2/Al2O3摩尔比增至304时,Sn组分与载体ZSM-5之间的相互作用减弱,经H2还原后催化剂中Sn0物种所占的比例增加,导致催化剂H2化学吸附量和丙烷脱氢反应活性下降.     

纳米碳材料负载铂催化剂在环己烷脱氢反应中的催化性能研究

制备了纳米碳材料负载铂的催化剂,通过N₂吸附、TEM、XRD技术分别对载体的BET比表面积和催化剂结构、形貌和粒径大小进行了表征。考察了不同催化剂在环己烷脱氢反应中的催化性能以及温度对纳米碳颗粒负载铂催化剂活性的影响。结果表明,锚定在不同碳载体上的铂有较好的分散性,粒径较小,粒度分布范围较窄并且具有相同的晶型结构。孔状纳米碳颗粒负载铂催化剂的活性高于碳纳米管和高比表面的活性炭负载铂催化剂,并且在低温条件下已经显示了较高的活性,尤其是中空碳颗粒负载铂催化剂在环己烷脱氢反应中显示了好的活性和稳定性。     

丙烷在负载型催化剂上脱氢反应的研究 Ⅲ.丙烷在氧化铝负载的铂-金属氧化物催化剂上的脱氢

第Ⅰ,Ⅱ报结果指出,氧化态锡对Pt/Al_2O_3具有助催化作用。本文通过对氧化脱氢过程类比分析,提出具有可变价态元素氧化物可替代Pt-Sn/Al_2O_3催化剂中氧化态锡组分,而与金属铂组分构成一系列具有良好催化性能的负载型双组分催化剂。对Al_2O_3负载的Pt-Ti,Pt-V,Pt-Cr,Pt-Mn及Pt-Fe催化剂评价结果表明,催化剂性能均随氧化态组分(Ti,V,Cr,Mn,Fe等)载量增加而逐步改善。     

水蒸汽对负载型催化剂丙烷脱氢性能的影响：Ⅰ.反应性能的研究

研究了ＭｇＡｌ２Ｏ４，ＺｎＡｌ２Ｏ４负载的Ｐｔ－Ｓｎ催化剂在氮气及水蒸汽中的丙烷脱氢性能。考察了还原温度，反应温度，催化剂载量对Ｐｔ－ＳＳｎ／ＭｇＡｌ２Ｏ４催化剂丙烷脱氢性能的影响。     

CO2催化加氢甲烷化负载型铁催化剂性能的研究

二氧化碳;CO2催化加氢甲烷化负载型铁催化剂性能的研究     

STN型液晶显示用聚酰亚胺表面取向材料的性能

倾斜角;STN型液晶显示用聚酰亚胺表面取向材料的性能     

不同活性炭上Pt催化剂的分散性及其在甲基环己烷脱氢反应中的催化性能

在不同方法处理的活性炭上采用传统浸渍方法制备了负载Pt催化剂,并考察了其在甲基环己烷脱氢反应中的催化性能.对炭载体的氮吸附和程序升温脱附的表征结果表明,活性炭经过硝酸氧化处理和氢气高温处理后,活性炭的孔结构基本不变,但表面含氧官能团的数量和种类发生了变化.这些不同的表面基团直接影响了Pt粒子在载体上的分散度,进而使催化剂在反应中表现出不同的活性.     

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.     

Catalytic Combustion of Methane over High Copper-Loading ZSM-5 Catalysts

Two series of Cu/ZSM-5 catalysts,loading from 5 to 20 wt% CuO,were prepared by the deposition-precipitation and impregnation methods,respectively.The catalysts prepared by the impreg- nation method showed better catalytic performances than those prepared by the deposition-precipitation method and the increase of copper loading favored methane conversion.20Cu(I)/ZSM-5 had the highest activity with T_(90%)of 746 K,and for 20Cu(D)/ZSM-5,T_(90%)was as high as 804 K.The characteriza- tion of X-ray diffraction(XRD),temperature-programmed reduction(TPR),temperature-programmed desorption(TPD),and X-ray photoelectron spectroscopy(XPS)revealed that the dispersion of cop- per species could be improved by using the deposition-precipitation method instead of the impregnation method,but the fraction of surface CuO,corresponding to active sites for methane oxidation,was larger on 20Cu(I)/ZSM-5 than 20Cu(D)/ZSM-5.The results of Pyridine-Fourier transform infrared spectrum (Py-FT-IR)showed that a majority of Lewis acidity and a minority of Brφnsted acidity were present on Cu/ZSM-5 catalysts.20Cu(I)/ZSM-5 presented more Lewis acid sites.The number of Lewis acid sites changed significantly with preadsorption of oxygen.Adsorption of methane and oxygen on acid sites was observed.The properties of Cu/ZSM-5 catalysts were correlated with the activity for methane oxidation.     

Characterization and Dehydrogenation Activity of SBA-15 and HMS Supported Chromia Catalysts

ＩｎｔｒｏｄｕｃｔｉｏｎＥｎｏｒｍｏｕｓｓｔｕｄｙｈａｓｂｅｅｎｄｅｖｏｔｅｄｔｏＭ4 1Ｓ ,ｔｈｅｆｉｒｓｔｆａｍｉｌｙｏｆｍｅｓｏｐｏｒｏｕｓｍｏｌｅｃｕｌａｒｓｉｅｖｅｓｒｅｐｏｒｔｅｄｉｎ1992 ,1,2 ｉｎｃｌｕｄｉｎｇｔｈｅｉｒｍｏｄｉｆｉｃａｔｉｏｎｓａｎｄａｐｐｌｉｃａｔｉｏｎｓｉｎｃａｔａｌｙｓｉｓ .Ｔｈｅａｔｔｒａｃｔｉｖｅｐｒｏｐｅｒｔｉｅｓｏｆｔｈｅｓｅｍａｔｅｒｉａｌｓａｒｅｔｈｅｉｒｈｉｇｈｓｐｅｃｉｆｉｃｓｕｒｆａｃｅａｒｅａ (>10 0 0ｍ2 /ｇ) ,ｗｅｌｌ ｄｅ ｆｉｎｅｄｓｔｒ…     

两段变温法水热合成多级孔ZSM-5分子筛及其催化裂化性能

以四丙基氢氧化铵（TPAOH）为单一模板剂,采用低温老化、高温晶化2段变温法合成出了球状多级孔ZSM-5分子筛。利用XRD、FT-IR、NH₃-TPD、SEM、TEM以及氮气吸-脱附等测试对合成样品进行了表征。结果表明：直径约为2 μm左右的球状多级孔ZSM-5分子筛颗粒内的晶间介孔和大孔主要由棒状纳米晶堆积而成的,该产品具有较大的比表面积和介孔孔容。同常规水热法一步合成的微孔ZSM-5分子筛相比,2段变温法合成的多级孔ZSM-5分子筛具有更高的B酸/L酸比例（C_BP/C_LP）、强酸/弱酸比例（C_s/Cw）以及活性位可接近性指数（ACI）。催化裂化评价结果显示,得益于活性位可接近性指数等指标的提高,球状多级孔ZSM-5分子筛比常规合成的微孔ZSM-5分子筛具有更高的转化率和丙烯收率等优异的催化性能。     

氨合成催化剂及其催化反应机理研究进展

本文综述了氨合成这一最重要的工业多相催化过程80 多年来的研究进展。介绍了氨合成熔铁催化剂、氨合成钌催化剂的发展以及对氨合成催化反应机理的不同看法。     

Au/MOF催化剂的制备、表征及其催化三组分偶联反应

采用后合成共价修饰法和一锅法分别制备了催化剂IRMOF-3-SI-Au(PS)和IRMOF-3-SI-Au(OP),运用X射线衍射、红外光谱、热重-差热分析、透射电镜以及程序升温还原对催化剂进行了表征,探索了这两种催化剂在醛、炔和胺三组分偶联反应中的催化性能,并推测了可能的反应机理.结果表明,两种催化剂对醛、炔和胺三组分偶联反应均具有较高的催化活性,产物炔丙基胺类选择性为100%,且可循环使用;结晶度较低的IRMOF-3-SI-Au(PS)的活性高于结晶度较高的IRMOF-3-SI-Au(OP);催化剂对芳香醛和脂肪醛以及环状胺均具有较高的催化活性,且对带有吸电子基团的芳香醛的活性高于带有供电子基团的.     

Understanding the Synthesis of Supported Vanadium Oxide Catalysts Using Chemical Grafting

The complexity of variables during incipient wetness impregnation synthesis of supported metal oxides precludes an in-depth understanding of the chemical reactions governing the formation of the dispersed oxide sites. This contribution describes the use of vapor phase deposition chemistry (also known as grafting) as a tool to systematically investigate the influence of isopropanol solvent on VO(OⁱPr)₃ anchoring during synthesis of vanadium oxide on silica. The availability of anchoring sites on silica was found to depend not only on the pretreatment of the silica but also on the solvent present. H-bond donors can reduce the reactivity of isolated silanols whereas disruption of silanol nests by H-bond acceptors can turn unreactive H-bonded silanols into reactive anchoring sites. The model suggested here can inform improved syntheses with increased dispersion of metal oxides on silica.