溶胶-凝胶和浸渍法制备的铜催化剂在仲丁醇脱氢反应中的研究

采用溶胶-凝胶和浸渍法制备Cu/SiO2催化剂, 研究了不同制备方法对催化剂表面Cu物种的存在状态和其催化性能的影响. 采用BET, XRD, EPR和TPR等手段对催化剂进行了表征, 结果表明, 溶胶-凝胶法可制备高分散铜催化剂, 该催化剂中存在孤立的不可还原的Cu2+和可还原的Cu2+簇两种物种. 浸渍法制备的催化剂中含有可还原的Cu2+簇物种. 反应活性测试结果表明, 不可还原的孤立Cu2+呈高分散状态, 但其对仲丁醇脱氢反应没有活性; 可还原的Cu2+在反应过程中被还原成Cu0, Cu0是反应稳定脱氢的活性中心.     

溶胶-凝胶法制备铁酸盐超微粒子催化剂

采用溶胶－凝胶法制备了含Zn,Ni,Co的铁酸盐超微粒子催化剂，运用DTA－TG、IR、XRD以及BET比表面测试等手段对所制备的样品进行了表征。同时，考察了铁酸盐对二氧化碳选择性氧化乙苯制苯乙烯的催化性能。结果表明：制备的铁酸盐均为尖晶石型晶体，粒子的比表面积为31．9－36．3m^2/g，晶粒大小约为30－35nm，在由二氧化碳选择性氧化乙苯制苯乙烯的反应中表现出较好的催化活性。     

溶胶—凝胶法制备NiO／SiO2催化剂研究

分别以正硅酸乙酯、硝酸镍为硅源和镍源,采用溶胶－凝胶法,经超临界流体干燥和普通干燥制备了NiO-A-SiO2、NiO-G-SiO2催化剂;以气凝胶和干凝胶为载体,采用浸渍法制备了NiO/A-SiO2、NiO/G-SiO2催化剂。并用XRD、TEM、BET、TPR等手段,研究了制备方法对催化剂织构、结构和Ni物种存在形态的影响,发现NiO-A-SiO2和NiO-G-SiO2催化剂上高度分散的NiO簇团与SiO2之间有较强的相互作用,其顺酐液相选择加氢转化率低于10％;NiO/G-SiO2催化剂上,以单一物种形态存在的NiO与SiO2相互作用弱,顺酐转化率为42％;NiO/A-SiO2催化剂上,以多种形态存在的微量NiO与SiO2间的相互作用较复杂,其顺酐液相选择加氢的转化率和丁二酸酐的选择性分别可达100％和98％。     

溶胶—凝胶法制备超细SiO2

ＳｉＯ２气凝胶超细粉由ＴＥＯＳ（正硅酸乙酯）在乙醇溶液中水解聚合后经超临界流体干燥（ＳＣＦＤ）制得。本文考察了ＴＥＯＳ的浓度、水和ＴＥＯＳ护林经以及焙烧温度对超细分织构性能的影响。结果表明，超细ＳｉＯ２的比表面积、总孔容、孔分布、最可几孔径及表观堆密度均随制备参数而改变。而以ＳｉＯ２气凝胶超细粉估为基本载体材料的Ｃｏ／ＺｒＯ２－ＳｉＯ２催化剂显示出高的ＣＯ＋Ｈ２合成重质烃的活性和选择性。     

溶胶—凝胶法制备的铑基CO加氢制C2含氧化合物催化剂

用ＸＲＤ,ＦＴ－ＩＲ,吸附ＣＯ的程序升温脱附,吸附ＣＯ的程序升温表面加氢反应等技术,并结合高压下ＣＯ加氢反应研究了用溶胶－凝胶法制备的铑基催化剂。结果表明,用溶胶－凝胶方法制备的催化剂中,Ｒｈ以极高的分散状态存在。与文献报道了浸渍法催化剂不同,ＣｅＯ２的加入使甲醇选择性显著提高,但降低了催化剂的活性。     

溶胶-凝胶工艺制备发光薄膜研究进展

本文综述了通过深胶－凝胶工艺制备发光薄膜的基本过程、薄膜的表征方法、发光薄膜的当前发展及应用情况。依据组成特点,对溶胶－凝胶法制备的发光薄膜乾地了分类阐述,并预言了今后该法制备发光薄膜的发展趋势。     

溶胶-凝胶法制备还原态K-Co-Mo催化剂的合成醇性能

应用溶胶-凝胶法制备了还原态K-Co-Mo催化剂, 比较了不同的组分和不同的反应条件对合成醇性能的影响。实验结果表明，适量钾和钴助剂的添加能显著提高催化剂合成醇的性能，尤其是提高了C2+醇的选择性。此外，反应温度、压力以及空速对合成醇影响明显，升高温度可以提高催化反应中低碳醇的收率，但选择性下降；增加压力和空速可以提高低碳醇的收率和选择性，对合成低碳醇有利。在230 ℃，6.0 MPa，14 400 h－1条件下，催化剂合成低碳醇的收率为375.4 g/kg·h，选择性为70.2%，C1OH/C2+OH为0.48。     

低温溶胶-凝胶法制备高致密度碳化硅陶瓷工艺研究

以柠檬酸为螯合剂,用溶胶-凝胶法制备碳化硅陶瓷烧结前驱粉体,在烧结助剂含量6%、铝钇摩尔比5/3、1850℃低烧结温度烧结1h条件下,获得了体密度为3.219g/cm3、相对密度为98.3%的高致密烧结体,采用IR、XRD、TG/DTA、SEM/EDS等手段对前驱粉体及烧结体进行了表征,讨论了烧结助剂含量、烧结温度等对碳化硅陶瓷烧结体的收缩率、体密度、失重率等特性的影响。     

溶胶-凝胶法制备Ni-SiO2催化剂的表征与性能

以正硅酸乙酯和硝酸镍为原料,采用溶胶-凝胶法,将硝酸镍分别溶于水和乙醇制得凝胶,分别经超临界干燥和常规干燥制备了一系列Ni-SiO2气凝胶和干凝胶催化剂,运用BET、XRD、TPR、IR、H2-TPD和活性评价等方法对催化剂的物理化学性质和催化间二硝基苯加氢性能进行研究.结果表明,Ni-SiO2气凝胶催化剂均具有较高的比表面积,但由于金属镍烧结导致活性比表面积较小,加氢性能较差;以乙醇为溶剂制备的干凝胶催化剂的镍物种分散度较高,但镍与载体之间的相互作用过强,致使催化剂的还原度降低,活性组分利用率下降;以水为溶剂制备的干凝胶催化剂具有较高的活性比表面积,表现出很高的催化活性和选择性.     

Nickelmodifiedlarge poremesoporoussilicas ascatalysts for methanol decomposition

Summary Ni-modifiedlarge poremesoporous silicasarecharacterized by XRD, N₂physisorption and TPR with H₂. Theeffectof the supportpore structure on their catalytic behaviorin methanol decomposition to H₂, CO and CH₄is studied.     

Co-modified Pd/CeO2-ZrO2 catalysts for methanol decomposition

Pd/Ce0.8Zr0.2O2 catalysts modified by cobalt were prepared by a sequential impregnation method and characterized by X-ray powder diffraction(XRD), N2adsorption/desorption(Brunauer-Emmet-Teller), oxygen storage capacity(OSC), CO-chemisorption, H2-temperature-programmed reduction(H2-TPR) and X-ray photoelectron spectroscopy(XPS). The effect of Co on the performance of methanol decomposition was evaluated at a fixed-bed microreactor. The results showed that the addition of Co can improve the oxygen storage capacity of the catalyst and the dispersion of Pd. XPS results indicated that Pd was in a partly oxidized(Pdδ+, 1δ2) state and Co2+was present in Pd catalysts modified by Co. A 90% conversion of methanol was achieved at around 280°C over Pd-Co/Ce0.8Zr0.2O2 catalyst which was 20°C lower than that over Pd/Ce0.8Zr0.2O2, indicating that both Pdδ+and Co2+play an important role in improving the catalytic activity of methanol decomposition.     

Co-modified Pd/CeO2-Zr02 catalysts for methanol decomposition

Pd/Ce0.8Zro.202 catalysts modified by cobalt were prepared by a sequential impregnation method and characterized by X-ray powder diffraction （XRD）, N2 adsorption/desorption （Brunauer-Emmet-Teller）, oxygen storage capacity （OSC）, CO-chemisorption, H2-temperature-programmed reduction （H2-TPR） and X-ray photoelectron spectroscopy （XPS）. The effect of Co on the performance of methanol decomposition was eval- uated at a fixed-bed microreactor. The results showed that the addition of Co can improve the oxygen storage capacity of the catalyst and the dispersion of Pd. XPS results indicated that Pd was in a partly oxidized （Pd6＋, 1〈8〈2） state and Co2＋ was present in Pd catalysts modified by Co. A 90% conversion of methanol was achieved at around 280 ℃ over Pd-Co/Ceo.8Zro.202 catalyst which was 20 ℃ lower than that over Pd/Ceo.sZro.202, indicating that both pd6＋and Co2＋ play an important role in improving the catalytic activity of methanol decomposition.     

超细CuO/ZnO/TiO2-SiO2的表征和CO2加氢合成甲醇性能研究

用溶胶-凝胶法制备了铜、锌质量分数不同的超细Cu/ZnO/TiO2-SiO2催化剂。通过BET、TPR、XRD及FT-IR等方法对催化剂前驱体CuO/ZnO/TiO2-SiO2的物化性能进行表征。用固定床连续流动微反装置，考察催化剂CO2加氢合成甲醇的催化性能。研究结果表明，溶胶-凝胶法制备的CuO/ZnO/TiO2-SiO2催化剂比表面较大（240 m2/g～590 m2/g），孔径分布单一，晶相组成为CuO。随着铜、锌质量分数的增大，催化剂的比表面积减小，最可几孔径增大; CuO微晶结晶度增大,同时微晶尺寸逐渐增大至20 nm。催化剂具有较高的反应活性和选择性，当氧化铜、氧化锌质量分数各为25%时，在260 ℃，2 500 h－1，CO2∶H2=1∶3（mol比），2.0 MPa的反应条件下，甲醇时空收率为0.126g/(h·g)。     

Development of high performance Cu/ZnO-based catalysts for methanol synthesis and the water-gas shift reaction

Our groups studies on Cu/ZnO-based catalysts for methanol synthesis via hydrogenation of CO₂ and for the water-gas shift reaction are reviewed. Effects of ZnO contained in supported Cu-based catalysts on their activities for several reactions were investigated. The addition of ZnO to Cu-based catalyst supported on Al₂O₃, ZrO₂ or SiO₂ improved its specific activity for methanol synthesis and the reverse water-gas shift reaction, but did not improve its specific activity for methanol steam reforming and the water-gas shift reaction. Methanol synthesis from CO₂ and H₂ over Cu/ZnO-based catalysts was extensively studied under a joint research project between National Institute for Resources and Environment (NIRE; one of the former research institutes reorganized to AIST) and Research Institute of Innovative Technology for the Earth (RITE). It was suggested that methanol should be produced via the hydrogenation of CO₂, but not via the hydrogenation of CO, and that H₂O produced along with methanol should greatly suppress methanol synthesis. The Cu/ZnO-based multicomponent catalysts such as Cu/ZnO/ZrO₂/Al₂O₃ and Cu/ZnO/ZrO₂/Al₂O₃/Ga₂O₃ were highly active for methanol synthesis from CO₂ and H₂. The addition of a small amount of colloidal silica to the multicomponent catalysts greatly improved their long-term stability during methanol synthesis from CO₂ and H₂. The purity of the crude methanol produced in a bench plant was 99.9 wt% and higher than that of the crude methanol from a commercial methanol synthesis from syngas. The water-gas shift reaction over Cu/ZnO-based catalysts was also studied. The activity of Cu/ZnO/ZrO₂/Al₂O₃ catalyst for the water-gas shift reaction at 523 K was less affected by the pre-treatments such as calcination and treatment in H₂ at high temperatures than that of the Cu/ZnO/Al₂O₃ catalyst. Accordingly, the Cu/ZnO/ZrO₂/Al₂O₃ catalyst was considered to be more suitable for practical use for the water-gas shift reaction. The Cu/ZnO/ZrO₂/Al₂O₃ catalyst was also highly active for the water-gas shift reaction at 673 K. Furthermore, a two-stage reaction system composed of the first reaction zone for the water-gas shift reaction at 673 K and the second reaction zone for the reaction at 523 K was found to be more efficient than a one-stage reaction system. The addition of a small amount of colloidal silica to a Cu/ZnO-based catalyst greatly improved its long-term stability in the water-gas shift reaction in a similar manner as in methanol synthesis from CO₂ and H₂.     

Iron modified mesoporous carbon and silica catalysts for methanol decomposition

Iron modified silica and carbon mesoporous materials with similar textural characteristics are compared in methanol decomposition to H₂, CO and CH₄. The influence of the support on the phase composition and reductive properties of the catalysts is studied by M?ssbauer spectroscopy and TPR with hydrogen. This revised version was published online in June 2006 with corrections to the Cover Date.     

硅源对蒸氨法制备Cu/SiO2催化剂催化甲醇裂解制氢的影响

采用蒸氨法制备Cu/SiO₂催化剂,分别考察气相二氧化硅（SiO₂-aer）、硅胶（SiO₂-gel）和碱性硅溶胶（SiO₂-sol）对Cu/SiO₂催化剂催化甲醇裂解制氢性能的影响,并采用N₂吸附-脱附、N₂O化学吸附、电感耦合等离子体原子发射光谱法（ICP-AES）、X射线衍射（XRD）、H₂程序升温还原（H₂-TPR）、透射电子显微镜（TEM）和X射线光电子能谱（XPS）等方法对催化剂进行表征。结果表明,硅源对Cu/SiO₂催化剂的活性具有较大影响。以碱性硅溶胶作为硅源制得的Cu/SiO₂-sol催化剂比表面积较大,活性中心粒径较小且分散均匀,这些使得其制氢性能优于其他两种硅源为载体所制备的催化剂。在反应温度280 ℃,反应压力1 MPa,甲醇质量空速0.6 h^-1的条件下,相较于Cu/SiO₂-aer和Cu/SiO₂-gel催化剂,Cu/SiO₂-sol催化剂的甲醇转化率分别提高10％和7％,气相副产物CH₄和CO₂浓度也有所降低,该催化剂上的甲醇转化率和气体收率分别达到98.4%和96.7%。     

Preparation and evaluation of ammonia decomposition catalysts by high-throughput technique

The high-throughput technique has been successfully employed to investigate systematically NH₃ decomposition catalysts for COx-free hydrogen production. Supported γ-Mo₂N catalysts not only could be prepared and evaluated by the high-throughput experiment, but are also active for NH₃ decomposition luke supported Ni and Co catalysts. Additionally, the preparation process and support play important roles on the catalytic performance of supported γ-Mo₂N catalysts.     

浸渍型甲醇裂解Cu/Cr基催化剂

汽车尾气占整个大气污染的 42 % [1] .开发洁净的燃料已成为研究热点 .H2 是最干净的燃料 ,但运输和储存困难 .甲醇被认为是一种很有前途的高能燃料 ,因此出于节能和环保双重原因 ,甲醇裂解制 H2 用于汽车燃料电池或裂解成 H2 和 CO混合气直接用作内燃机燃料的研究和应用已引起广泛关注[2 ] .目前研究较多的是沉淀型 Cu/Zn基催化剂 ,但由于分散度不高、Cu晶易长大 ,因而活性和稳定性不好[3] .本文报道用共浸的方法制备Cu/Cr基催化剂 ,研究了它们的催化性能 ,并对催化剂的失活原因进行了初步探讨 .催化剂制备 :将 Cu( NO3) 2 · 3H2 O(…     

滑动弧放电等离子体分解甲醇制氢

对常温常压下滑动弧放电等离子体直接分解甲醇进行了研究,探讨了载气流量、甲醇浓度、电极间距、输入电压和气化室温度等实验参数的影响。结果表明,不同操作条件导致甲醇转化率由51%升高到81.7%,氢气和一氧化碳的选择性之比基本保持一个固定值。除了氢气和一氧化碳,产物中还检测到了少量的甲烷和C₂不饱和烃以及痕量二氧化碳。不同于传统的甲醇热分解机理,提出了滑动弧放电等离子体甲醇分解的制氢路径。