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丙烷在Ce-Fe/Al_2O_3/cordierite上选择性催化还原NO 被引量:3
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作者 李伉锴 周皞 +3 位作者 苏亚欣 袁旻昊 邓文义 赵兵涛 《燃料化学学报》 EI CAS CSCD 北大核心 2018年第1期99-109,共11页
利用凝胶溶胶法和浸渍法制备了Ce-Fe/Al_2O_3/cordierite催化剂,实验研究了其催化丙烷选择性还原NO的特性。结果表明,当铈的负载量从1%增加至5%时,Ce-Fe/Al_2O_3/cordierite的C_3H_8-SCR性能先增强后减弱,3.5Ce-Fe/Al_2O_3/cordierite... 利用凝胶溶胶法和浸渍法制备了Ce-Fe/Al_2O_3/cordierite催化剂,实验研究了其催化丙烷选择性还原NO的特性。结果表明,当铈的负载量从1%增加至5%时,Ce-Fe/Al_2O_3/cordierite的C_3H_8-SCR性能先增强后减弱,3.5Ce-Fe/Al_2O_3/cordierite具有最佳的脱硝性能,在有氧条件下,600℃时可实现96.5%的脱硝效率。Ce的加入能够提升Fe/Al_2O_3/cordierite催化剂的抗硫性能。烟气中通入0.02%的SO_2后,3.5Ce-Fe/Al_2O_3/cordierite催化丙烷还原NO的转化率始终维持在93%,而没有经过Ce修饰的Fe/Al_2O_3/cordierite的NO转化率从88%下降为80%左右。利用XRD、N_2吸附-脱附、SEM、H_2-TPR、吡啶吸附红外光谱等手段研究了催化剂的物理化学性质。结果表明,加入助剂铈能与Fe形成了固溶体,增加催化剂表面Lew is酸浓度和氧化还原能力,从而提高了催化丙烷还原NO的性能。过多的铈引入会减少Fe_2O_3结晶体的形成,不利于在C_3H_8-SCR反应中形成NO_2/NO_3^-物种,从而导致NO还原效率下降。 展开更多
关键词 选择性催化还原 No fe/al2o3/cordierite催化剂 丙烷
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Co/Fe/Al_2O_3/cordierite催化C_3H_6选择性还原NO的实验研究 被引量:5
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作者 刘欣 苏亚欣 +3 位作者 董士林 周皞 邓文义 赵兵涛 《燃料化学学报》 EI CAS CSCD 北大核心 2018年第6期743-753,共11页
采用溶胶凝胶法和浸渍法制备了负载于蜂窝陶瓷上的Co/Fe/Al_2O_3/cordierite催化剂,在陶瓷管流动反应器上对其催化C_3H_6选择性还原NO的性能进行了测试。结果表明,该催化剂表现出最优脱硝性能,在模拟烟气条件下,当反应温度为550℃时可实... 采用溶胶凝胶法和浸渍法制备了负载于蜂窝陶瓷上的Co/Fe/Al_2O_3/cordierite催化剂,在陶瓷管流动反应器上对其催化C_3H_6选择性还原NO的性能进行了测试。结果表明,该催化剂表现出最优脱硝性能,在模拟烟气条件下,当反应温度为550℃时可实现97%的脱硝效率。Co的引入可显著增强Fe/Al_2O_3/cordierite催化剂抗SO_2和H_2O的能力。在模拟烟气中同时引入0.02%SO_2和3%H_2O后,1.5Co/Fe/Al_2O_3/cordierite的脱硝性能受影响甚微,当反应温度高于500℃时1.5Co/Fe/Al_2O_3/cordierite催化C_3H_6还原NO的效率均可达到90%以上;相比之下,未经Co修饰的催化剂Fe/Al_2O_3/cordierite脱硝性能受到了严重的抑制,在整个反应温度区间(200-700℃)内,其催化C_3H_6还原NO的效率最高不足50%。XRD和SEM表征结果表明,经过适量的Co修饰后的1.5Co/Fe/Al_2O_3/cordierite表面变得更疏松,且形成了以钴铁和钴铝双金属氧化物为主要成分的球状晶粒。H_2-TPR结果表明,相比于Fe/Al_2O_3/cordierite,1.5Co/Fe/Al_2O_3/cordierite有更好的低温还原性能。PyFTIR结果表明,Co的引入可使催化剂表面的Lewis酸明显增加,且生成了Brnsted酸。N2吸附-脱附表征结果表明,Co可增大催化剂的比表面积。 展开更多
关键词 选择性催化还原 Co/fe/al2o3/cordierite催化剂 No 丙烯
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Experimental and Kinetic Study of Selective Catalytic Reduction of NO with NH_3 over CuO/Al_2O_3/Cordierite Catalyst 被引量:6
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作者 雷志刚 龙爱斌 +1 位作者 贾美如 刘学义 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2010年第5期721-729,共9页
The CuO/γ-Al2O3/cordierite catalyst, after being sulfated by sulfur dioxide (SO2) at 673 K, exhibits high activities for selective catalytic reduction (SCR) of nitrogen oxide (NO) with ammonia (NH3) at 573-723 K. The... The CuO/γ-Al2O3/cordierite catalyst, after being sulfated by sulfur dioxide (SO2) at 673 K, exhibits high activities for selective catalytic reduction (SCR) of nitrogen oxide (NO) with ammonia (NH3) at 573-723 K. The intrinsic kinetics of SCR of NO with NH3 over CuO/γ-Al2O3/cordierite catalyst has been measured in a fixed-bed reactor in the absence of internal and external diffusions. The experimental results show that the reaction rate can be quantified by a first-order expression with activation energy Eá of 94.01 kJ·mol-1 and the corresponding p re-exponential factor A′ of 3.39×108 cm3·g-1·s-1 when NH3 is excessive. However, when NH3 is not enough, an E ley-Rideal kinetic model based on experimental data is derived with Ea of 105.79 kJ·mol-1, the corresponding A of 2 .94×109 cm3·g-1·s-1, heat of adsorption-Hads of 87.90 kJ·mol-1 and the corresponding Aads of 9.24 cm3·mol-1. The intrinsic kinetic model obtained was incorporated in a 3D mathematical model of monolithic reactor, and the agreement of the prediction with experimental data indicates that the present kinetic model is adequate for the reac-tor design and engineering scale-up. 展开更多
关键词 kinetics selective catalytic reduction Cuo/γ-al2o3/cordierite catalyst monolithic honeycomb reactor mathematical model
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Influence of Fe_2O_3 Impurity on the Crystalline Structure of Cordierite Synthesized from Waste Aluminum Slag 被引量:3
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作者 WUWei-Qing RUANYu-Zhong YUYan 《Chinese Journal of Structural Chemistry》 SCIE CAS CSCD 北大核心 2005年第4期483-487,共5页
The influence of Fe2O3 impurity on the crystalline structure of cordierite synthesized from waste aluminum slag is discussed. XRD and SEM techniques were employed to characterize the crystalline structure and micros... The influence of Fe2O3 impurity on the crystalline structure of cordierite synthesized from waste aluminum slag is discussed. XRD and SEM techniques were employed to characterize the crystalline structure and microstructure of each specimen. Philips X’pert plus software was used to determine the lattice parameters of each specimen. The results show that the Fe2O3 content of 0.8~1.6wt% is beneficial to the formation of cordierite, with the cordierite amount reaching 90wt%. So 0.8~1.6wt% is considered as the allowable Fe2O3 content in the specimens and 0.8wt% is determined to be the best after overall analysis. Plus software analysis shows that the cordierite in each specimen has the same symmetrical hexagonal structure as the single crystal, and the lattice parameters as well as the lattice dimensions change slightly. 展开更多
关键词 aluminum slag cordierite fe2o3 impurity crystalline structure
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Fe_3O_4@UiO-66-NH_2 core–shell nanohybrid as stable heterogeneous catalyst for Knoevenagel condensation 被引量:6
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作者 张艳梅 戴田霖 +3 位作者 张帆 张静 储刚 权春善 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2016年第12期2106-2113,共8页
separation is an attractive alternative to filtration or centrifugation for separating solid catalysts from a liquid phase, Here, core-shell Fe3O4@UiO-66-NH2 nanohybrids with well-defined structures were constructed b... separation is an attractive alternative to filtration or centrifugation for separating solid catalysts from a liquid phase, Here, core-shell Fe3O4@UiO-66-NH2 nanohybrids with well-defined structures were constructed by dispersing magnets in a dimethylformamide (DMF) solution con- taining two metal-organic framework (MOF) precursors, namely ZrCI4 and 2-aminobenzenetricar- boxylic acid. This method is simpler and more efficient than previously reported step-by-step method in which magnets were consecutively dispersed in DMF solutions each containing one MOF precursor, and the obtained Fe304@UiO-66-NH2 with three assembly cycles has a higher degree of crystallinity and porosiW. The core-shell Fe3O4@UiO-66-NH2 is highly active and selective in Knoevenagel condensations because of the bifunctionality of UiO-66-NH2 and better mass transfer in the nano-sized shells. It also has good recycling stability, and can be recovered magnetically and reused at least four times without significant loss of catalytic activity and framework integrity. The effects of substitution on the reactivity of benzaldehyde and of substrate size were also investigated. 展开更多
关键词 Metal-organic framework Uio-66-NH2 fe3o4 Heterogeneous catalyst Knoevenagel condensation Magnetic separation
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Effect of Al_2O_3 Binder on the Precipitated Iron-Based Catalysts for Fischer-Tropsch Synthesis 被引量:6
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作者 Hai-Jun Wan Bao-Shan Wu +4 位作者 Xia An Ting-Zhen Li Zhi-Chao Tao Hong-Wei Xiang Yong-Wang Li 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2007年第2期130-138,共9页
A series of iron-based Fischer-Tropsch synthesis (FTS) catalysts incorporated with Al2O3 binder were prepared by the combination of co-precipitation and spray drying technology. The catalyst samples were characteriz... A series of iron-based Fischer-Tropsch synthesis (FTS) catalysts incorporated with Al2O3 binder were prepared by the combination of co-precipitation and spray drying technology. The catalyst samples were characterized by using N2 physical adsorption, temperature-programmed reduction/desorption (TPR/TPD) and MSssbauer effect spectroscopy (MES) methods. The characterization results indicated that the BET surface area increases with increasing Al2O3 content and passes through a maximum at the Al2O3/Fe ratio of 10/100 (weight basis). After the point, it decreases with further increase in Al2O3 content. The incorporation of Al2O3 binder was found to weaken the surface basicity and suppress the reduction and carburization of iron-based catalysts probably due to the strong K-Al2O3 and Fe-Al2O3 interactions. Furthermore, the H2 adsorption ability of the catalysts is enhanced with increasing Al2O3 content. The FTS performances of the catalysts were tested in a slurry-phase continuously stirred tank reactor (CSTR) under the reaction conditions of 260 ℃, 1.5 MPa, 1000 h^-1 and molar ratio of H2/CO 0.67 for 200 h. The results showed that the addition of small amounts of Al2O3 affects the activity of iron-based catalysts to a little extent. However, with further increase of Al2O3 content, the FTS activity and water gas shift reaction (WGS) activity are decreased severely. The addition of appropriate Al2O3 do not affect the product selectivity, but the catalysts incorporated with large amounts of Al2O3 have higher selectivity for light hydrocarbons and lower selectivity for heavy hydrocarbons. 展开更多
关键词 Fischer-Tropsch synthesis iron-based catalyst al2o3 binder fe-al2o3 interaction
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Preparation of Fe_2P/Al_2O_3 and FeP/Al_2O_3 catalysts for the hydrotreating reactions 被引量:3
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作者 Yamei Yuan Jiayou Zhang +2 位作者 Hui Chen Qiumei Hou Jianyi Shen 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2019年第2期116-121,共6页
A 60%Fe/Al_2O_3 catalyst was prepared by the co-precipitation method.It was reduced by H_2 to produce metallic Fe,which was then sulfided by CS_2 to Fe_(0.96) S and Fe_3S_4 or phosphided by triphenylphosphine(PPh3) in... A 60%Fe/Al_2O_3 catalyst was prepared by the co-precipitation method.It was reduced by H_2 to produce metallic Fe,which was then sulfided by CS_2 to Fe_(0.96) S and Fe_3S_4 or phosphided by triphenylphosphine(PPh3) in liquid phases to Fe2 P and Fe P.It was found that the iron sulfides(Fe0.96 S and Fe_3S_4) exhibited the low activity for the hydrodesulfurization(HDS) reactions.The HDS activity was also low on the Fe(metal)/Al_2O_3 and Fe_2 P/Al_2O_3 catalysts since they were converted into Fe0.96 S and Fe_3S_4 during the HDS reactions.In contrast,the FeP/Al_2O_3 was found to be stable and active for the HDS reactions.In particular,Fe P/Al_2O_3 possessed significantly smaller Fe P particles than Fe P/C,leading to the significant higher HDS activity of FeP/Al_2O_3 than Fe P/C. 展开更多
关键词 fe2P/al2o3 catalyst feP/al2o3 catalyst Liquid phase phosphidation PPh3 HYDRoTREATING REACTIoNS
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Effect of Alumina Particle Size on Ni/Al2O3 Catalysts for p-Nitrophenol Hydrogenation 被引量:5
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作者 陈日志 杜艳 +1 位作者 邢卫红 徐南平 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2007年第6期884-888,共5页
The catalytic hydrogenation of p-nitrophenol to p-aminophenol was investigated over Ni/Al2O3 catalyst on alumina support with different particle size. It is found that support particle size has significant influences ... The catalytic hydrogenation of p-nitrophenol to p-aminophenol was investigated over Ni/Al2O3 catalyst on alumina support with different particle size. It is found that support particle size has significant influences on physiochemical properties and catalytic activity of the resulting Ni/Al2O3 catalyst, but little influence on the selec-tivity. At a comparable amount of Ni loading, the catalytic activity of Ni/Al2O3 prepared with alumina support of smaller particle size is lower. The reduction behavior of the catalyst is a key factor in determining the catalytic activity of Ni/Al2O3 catalyst. The supported nickel catalyst 10.3Ni/Al2O3-3 improves the life span of the membrane by reducing fouling on the membrane surface compared to nano-sized nickel. 展开更多
关键词 P-NITRoPHENoL catalytic hydrogenation P-AMINoPHENoL Ni/al2o3 catalysts ceramic membrane filtration
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Effects of Cerium Oxide on Ni/Al_2O_3 Catalysts for Decomposition of CH_4 and C_2H_4 被引量:4
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作者 杨咏来 李文钊 徐恒泳 《Journal of Rare Earths》 SCIE EI CAS CSCD 2003年第4期427-429,共3页
Characteristics of carbon deposition of CH 4 and C 2H 4 decomposition over supported Ni and Ni Ce catalysts were studied by using a pulse reaction as well as BET, TPR, XPS and hydrogen chemisorption techniques. It... Characteristics of carbon deposition of CH 4 and C 2H 4 decomposition over supported Ni and Ni Ce catalysts were studied by using a pulse reaction as well as BET, TPR, XPS and hydrogen chemisorption techniques. It is found that there is a metal semiconductor interaction (MScI) in the Ni Ce catalyst, and the effect of MScI on the carbon deposition of CH 4 decomposition is opposite to that of C 2H 4. A novel model of carbon deposition of CH 4 or C 2H 4 decomposition was proposed. 展开更多
关键词 catalytic chemistry Ni/al 2o 3 catalyst cerium oxide METHANE ETHYLENE DECoMPoSITIoN rare earths
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Preparation and characterization of Fe_2O_3-CeO_2-TiO_2/γ-Al_2O_3 catalyst for degradation dye wastewater 被引量:5
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作者 LIU Yan SUN De-zhi CHENG Lin LI Yan-ping 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2006年第6期1189-1192,共4页
In order to develop a catalyst with high activity for catalytic wet oxidation (CWO) process at room temperature and atmospheric pressure, Fe2O3-CeO2-TiO2/γ-Al2O3 catalyst was prepared by consecutive impregnation me... In order to develop a catalyst with high activity for catalytic wet oxidation (CWO) process at room temperature and atmospheric pressure, Fe2O3-CeO2-TiO2/γ-Al2O3 catalyst was prepared by consecutive impregnation method and the prepared parameters were optimized. The structure of the catalyst was characterized by BET, XRF, SEM and XPS technologies, and the actual wastewater was used to investigate the catalytic activity of Fe2O3-CeO2-TiO2/γ-Al2O3 in CWO process. The experimental results showed that the prepared catalyst exhibited good catalytic activity when the doping amount of Ti was 1.0 wt% (the weight ratio of Ti to carriers), and the middle product, Fe2O3-CeO2-TiO2/γ-Al2O3, was calcined in 450℃ for 2 h. The CWO experiment for treating actual dye wastewater indicated that the COD, color and TOC of actual wastewater were decreased by 62.23%, 50.12% and 41.26% in 3 h, respectively, and the ratio of BOD5/COD was increased from 0.19 to 0.30. 展开更多
关键词 catalytic wet oxidation (CWo fe2o3-Ceo2-Tio2/γ-al2o3 catalyst dye wastewater treatment
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Effect of Fe_2O_3 Loading Amount on Catalytic Properties of Monolithic Fe_2O_3/Ce_(0.67)Zr_(0.33)O_2-Al_2O_3 Catalyst for Methane Combustion 被引量:2
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作者 刘志敏 陈耀强 +3 位作者 钟俊波 王健礼 闫生辉 龚茂初 《Journal of Rare Earths》 SCIE EI CAS CSCD 2007年第5期585-589,共5页
Ce0.67Zr0.33O2-Al2O3 solid solution was prepared by the co-precipitation method. Fe2O3-based catalysts supported on the solid solution were obtained by the impregnation method. The article revealed that the optimal lo... Ce0.67Zr0.33O2-Al2O3 solid solution was prepared by the co-precipitation method. Fe2O3-based catalysts supported on the solid solution were obtained by the impregnation method. The article revealed that the optimal loading amount of Fe2O3 on Ce0.67Zr0.33 O2-Al2O3 in our experimental condition for catalytic combustion of methane was 8% ( mass fraction). The prepared catalysts were characterized by BET, TPR, XRD analyses, and their catalytic activity was investigated after being calcined at 873 K and after being aged in water gas at 1273 K. When the loading amount of Fe203 was 8% ( mass fraction), the catalyst held the highest activity, and the best temperature speciality and thermal stability. The complete-conversion temperature of methane for fresh and aged sample was 788 and 838 K, respectively. The range between the light-off temperature and the complete-conversion temperature was only 15 K. The characterization results of XRD indicated that Fe2O3 was well dispersed on the Ce0.67Zr0.33O2-Al2O3 matrix. The results of BET and TPR were in good harmony with the catalytic activity results. 展开更多
关键词 Ce0.67Zr0.33o2 -al2o3 fe2o3-based monolithic catalyst catalytic methane combustion catalytic properties
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惰性载体Al_2O_3对Fe_2O_3及CuO氧载体煤化学链燃烧的影响 被引量:16
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作者 王保文 赵海波 +3 位作者 郑瑛 柳朝晖 郑楚光 晏蓉 《中国电机工程学报》 EI CSCD 北大核心 2011年第32期53-61,共9页
氧载体是煤化学链燃烧技术的基础,惰性载体则是其中的必要组成部分,起着重要的作用。以Al2O3作为典型惰性载体,采用热重分析仪、红外频谱仪、场发射扫描电镜和能谱分析仪以及X衍射仪,对六盘水贫煤与Fe2O3、CuO基氧载体的反应进行了详细... 氧载体是煤化学链燃烧技术的基础,惰性载体则是其中的必要组成部分,起着重要的作用。以Al2O3作为典型惰性载体,采用热重分析仪、红外频谱仪、场发射扫描电镜和能谱分析仪以及X衍射仪,对六盘水贫煤与Fe2O3、CuO基氧载体的反应进行了详细的研究。研究发现,Al2O3的引入,使得Fe2O3、CuO基氧载体表面积增大、孔径分布更为优化,而且对氧载体与六盘水贫煤一次热解产物的反应是有利的,能够促进氧载体中更多晶格氧的传递,Fe2O3基氧载体中有更多的Fe2O3还原为低于Fe3O4价态的氧化物,而CuO基氧载体中CuO除了还原为Cu、Cu2O外,其中的CuAl2O4也有一定的反应活性,被还原为CuAlO2。与LPS煤反应时,Fe2O3深度还原产物与部分Al2O3及煤中的SiO2反应生成Fe3Al2(SiO4)3,而CuO则与Al2O3及六盘水贫煤反应生成了(Cu0.215Mg1.785)(Al4Si5O18)复合物。 展开更多
关键词 Co2捕获 化学链燃烧 fe2o3、Cuo氧载体 惰性载体al2o3
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Conversion and reaction kinetics of coke oven gas over a commercial Fe-Mo/Al_2O_3 catalyst 被引量:1
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作者 屈一新 徐贺明 +2 位作者 赵见峰 王志彦 王亚涛 《Journal of Central South University》 SCIE EI CAS CSCD 2016年第2期293-302,共10页
Producing methanol from coke oven gas(COG) is one of the important applications of COG. Removal of sulfur from COG is a key step of this process. Conversion and reaction kinetics over a commercial Fe-Mo/Al2O3 catalyst... Producing methanol from coke oven gas(COG) is one of the important applications of COG. Removal of sulfur from COG is a key step of this process. Conversion and reaction kinetics over a commercial Fe-Mo/Al2O3 catalyst(T-202) were studied in a continuous flow fixed bed reactor under pressures of 1.6-2.8 MPa, space time of 1.32-3.55 s and temperatures of 240-360 °C. Though the COG contains about 0.6 mol/mol H2, hydrogenation of CO and CO2 is not significant on this catalyst. The conversions of unsaturated hydrocarbons depend on their molecular structures. Diolefins and alkynes can be completely hydrogenated even at relatively low temperature and pressure. Olefins, in contrast, can only be progressively hydrogenated with increasing temperature and pressure. The hydrodesulfurization(HDS) of CS2 on this catalyst is easy. Complete conversion of CS2 was observed in the whole range of the conditions used in this work. The original COS in the COG can also be easily converted to a low level. However, its complete HDS is difficult due to the relatively high concentration of CO in the COG and due to the limitation of thermodynamics. H2 S can react with unsaturated hydrocarbons to form ethyl mercaptan and thiophene, which are then progressively hydrodesulfurized with increasing temperature and pressure. Based on the experimental observations, reaction kinetic models for the conversion of ethylene and sulfur-containing compounds were proposed; the values of the parameters in the models were obtained by regression of the experimental data. 展开更多
关键词 coke oven gas CoNVERSIoN fe-Mo/al2o3 catalyst sulfur-containing compound KINETICS
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Ce_(0·67)Zr_(0·33)O_2对CH_4燃烧催化剂Fe_2O_3/Al_2O_3的改性作用 被引量:10
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作者 陈清泉 张丽娟 +2 位作者 陈耀强 王敏 龚茂初 《高等学校化学学报》 SCIE EI CAS CSCD 北大核心 2005年第9期1704-1708,共5页
固定n(Ce)/n(Zr)比为0·67/0·33,用共沉淀法制得一系列CeO2-ZrO2-Al2O3固溶体.采用这些固溶体作载体,以Fe2O3为活性组分,用浸渍法制备了一系列催化剂.BET结果显示,将适量Ce0·67Zr0·33O2引入到Al2O3载体中有助于催化... 固定n(Ce)/n(Zr)比为0·67/0·33,用共沉淀法制得一系列CeO2-ZrO2-Al2O3固溶体.采用这些固溶体作载体,以Fe2O3为活性组分,用浸渍法制备了一系列催化剂.BET结果显示,将适量Ce0·67Zr0·33O2引入到Al2O3载体中有助于催化剂保持较高的比表面积.TPR结果显示,载体中引入适量的Ce0·67Zr0·33O2可以改善催化剂的氧化还原性能.XRD结果表明,Fe2O3在CeO2-ZrO2-Al2O3载体上呈现出良好的分散状况,老化前后催化剂的晶相结构基本无明显变化.特别是当载体中m(Ce0·67Zr0·33O2)∶m(Al2O3)的值为1∶2时,Fe2O3/CeO2-ZrO2-Al2O3催化剂在甲烷催化燃烧中显示出最佳的催化性能和抗高温老化性能. 展开更多
关键词 Ceo2-Zro2-al2o3 fe2o3系整体式催化剂 甲烷催化燃烧 催化性能 抗高温老化 fe2o3/al2o3 燃烧催化剂 改性作用 CH4 氧化还原性能
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Fe_2O_3/Al_2O_3氧载体用于甲烷化学链燃烧:负载量与制备方法的影响 被引量:12
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作者 刘自松 魏永刚 +3 位作者 李孔斋 王华 祝星 杜云鹏 《燃料化学学报》 EI CAS CSCD 北大核心 2013年第11期1384-1392,共9页
以不同方法制备了系列Fe2O3/Al2O3氧载体,采用XRD、H2-TPR、CH4-TPR、O2-TPD和BET等分析技术对氧载体进行了表征。研究了不同Fe2O3负载量氧载体的甲烷化学链燃烧性能,考察了不同制备方法对Fe2O3/Al2O3氧载体结构、反应性和产物选择性的... 以不同方法制备了系列Fe2O3/Al2O3氧载体,采用XRD、H2-TPR、CH4-TPR、O2-TPD和BET等分析技术对氧载体进行了表征。研究了不同Fe2O3负载量氧载体的甲烷化学链燃烧性能,考察了不同制备方法对Fe2O3/Al2O3氧载体结构、反应性和产物选择性的影响。结果表明,Fe2O3负载量对氧载体活性及产物中CO2选择性的影响较大,负载量较低时氧载体活性较低且引起甲烷部分氧化产物CO含量增加。制备方法亦对氧载体与甲烷的反应活性有所影响,整体上共沉淀法制备的质量分数60%Fe2O3/Al2O3氧载体具有较高的氧化活性和化学链循环稳定性。其在反应温度850℃、反应时间15 min、30次循环后甲烷转化率及产物中CO2选择性均未见明显降低。 展开更多
关键词 甲烷化学链燃烧 fe2o3 al2o3氧载体 负载量 制备方法
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α-Fe_2O_3、γ-Al_2O_3、SiO_2混合体系的表面配位反应 被引量:8
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作者 刘嘉 张卫民 +3 位作者 黄佩佩 樊佳妮 孙仁贵 孙中溪 《物理化学学报》 SCIE CAS CSCD 北大核心 2011年第1期186-192,共7页
运用自动电位滴定技术分别研究了纳米α-Fe2O3、γ-Al2O3、SiO2单一体系及三组分混合体系中氧化物表面的酸碱性质和对重金属离子Cu2+、Pb2+、Zn2+的吸附行为.依据表面配位理论恒电容模式(CCM),计算了相应的表面酸碱配位常数.结果表明:α... 运用自动电位滴定技术分别研究了纳米α-Fe2O3、γ-Al2O3、SiO2单一体系及三组分混合体系中氧化物表面的酸碱性质和对重金属离子Cu2+、Pb2+、Zn2+的吸附行为.依据表面配位理论恒电容模式(CCM),计算了相应的表面酸碱配位常数.结果表明:α-Fe2O3/γ-Al2O3/SiO2三组分混合体系的表面化学反应并非是单一体系的简单叠加,而是存在着不同矿物表面间复杂的交互作用.三组分表面酸碱反应平衡式和相应的酸碱反应平衡常数分别为:≡XOH2+≡XOH+H+(lgKa1=-4.23),≡XOH≡XO-+H+(lgKa2=-8.41).根据重金属离子Cu2+、Pb2+、Zn2+在α-Fe2O3/γ-Al2O3/SiO2混合体系表面的吸附行为,计算得到Cu2+、Pb2+、Zn2+在混合体系表面配位反应及其平衡常数如下:≡XOH+M2+≡XOM++H+;lgK=-2.20,-1.90,-3.20(M=Cu,Pb,Zn). 展开更多
关键词 fe2o3 al2o3 SIo2 混合体系 表面配位 表面酸碱性
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Oxidative desulfurization of dibenzothiophene over Fe promoted Co–Mo/Al_2O_3 and Ni–Mo/Al_2O_3 catalysts using hydrogen peroxide and formic acid as oxidants 被引量:3
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作者 Yaseen Muhammad Ayesha Shoukat +2 位作者 Ata Ur Rahman Haroon Ur Rashid Waqas Ahmad 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2018年第3期593-600,共8页
This work reports the enhancing effect of a highly cost effective and efficient metal, Fe, incorporation to Co or Ni based Mo/Al2O3 catalysts in the oxidative desulfurization (ODS) of dibenzothiophene (DBT) using ... This work reports the enhancing effect of a highly cost effective and efficient metal, Fe, incorporation to Co or Ni based Mo/Al2O3 catalysts in the oxidative desulfurization (ODS) of dibenzothiophene (DBT) using H2O2 and formic acid as oxidants. The influence of operating parameters i.e. reaction time, catalyst dose, reaction temperature and oxidant amount on oxidation process was investigated. Results revealed that 99% DBT conversion was achieved at 60℃ and 150 min reaction time over Fe-Ni-Mo/Al2O3. Fe tremendously enhanced the ODS activity of Co or Ni based Mo/Al2O3 catalysts following the activity order:Fe-Ni-Mo/Al2O3 〉 Fe-Co-Mo/Al2O3 〉 Ni-Mo/Al2O3 〉 Co-Mo/Al2O3, while H2O2 exhibited higher oxidation activity than formic acid over all catalyst systems. Insight about the surface morphology and textural properties of fresh and spent catalysts were achieved using scanning electron microscopy (SEM), X-ray diffraction (XRD), energy dispersive X-ray (EDX) analysis, Atomic Absorption Spectroscopy (AAS) and BET surface area analysis, which helped in the interpretation of experimental data. The present study can be deemed as an effective approach on industrial level for ODS of fuel oils crediting to its high efficiency, low process/catalyst cost, safety and mild operating condition. 展开更多
关键词 oxidative desulfurization Fuel oil Dibenzothiophene fe promoted (Co/Ni)-Mo/al2o3 catalyst XRD
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超级铝热剂Al/Fe2O3的制备、表征及对环三亚甲基三硝胺热分解的影响 被引量:6
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作者 赵宁宁 贺翠翠 +4 位作者 刘健冰 马海霞 安亭 赵凤起 胡荣祖 《物理化学学报》 SCIE CAS CSCD 北大核心 2013年第12期2498-2504,共7页
采用水热法制备了中空短棒状纳米Fe2O3,并用超声分散法将其与纳米Al颗粒复合为单金属氧化基超级铝热剂.利用X射线粉末衍射(XRD)、傅里叶变换红外(FTIR)光谱、扫描电镜及能量散射光谱仪(SEM-EDS)对样品进行表征.并运用差示扫描量热法(DSC... 采用水热法制备了中空短棒状纳米Fe2O3,并用超声分散法将其与纳米Al颗粒复合为单金属氧化基超级铝热剂.利用X射线粉末衍射(XRD)、傅里叶变换红外(FTIR)光谱、扫描电镜及能量散射光谱仪(SEM-EDS)对样品进行表征.并运用差示扫描量热法(DSC)对比研究了超级铝热剂Al/Fe2O3、Al粉和纳米Fe2O3对环三亚甲基三硝胺(RDX)热分解特性的影响.结果表明:超级铝热剂的加入改变了RDX的热分解过程,并加剧了RDX的二次气相反应;随着超级铝热剂含量的增加,RDX的分解峰峰形发生了明显的改变;Al/Fe2O3、Al粉和Fe2O3对RDX热分解的作用主要表现为二次分解峰逐渐明显且峰温降低. 展开更多
关键词 纳米fe2o3超级铝热剂al fe2o3 环三亚甲基三硝胺 水热法 超声分散法 热分解
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Oxidation of Mercaptans from Light Oil Sweetening by Fe_2O_3/MgO/Al_2O_3 Supported CoPcS Catalyst 被引量:1
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作者 Mei Hua Liu Hui Sheng Kuang 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2010年第3期12-17,共6页
MgO/Al2O3 and Fe2O3/MgO/Al2O3 solid bases were prepared through mixing method. After sulfonated cobalt phthalocyanine (CoPcS) being supported on these solid bases, the catalytic performance of these catalysts was ev... MgO/Al2O3 and Fe2O3/MgO/Al2O3 solid bases were prepared through mixing method. After sulfonated cobalt phthalocyanine (CoPcS) being supported on these solid bases, the catalytic performance of these catalysts was evaluated by means of mercaptan oxidation reaction. The samples were characterized by X-ray diffraction (XRD), CO2 temperature-programmed desorption (CO2-TPD), FTIR spectroscopy, and X-ray photoelectron spectroscopy (XPS). Investigation was focused on the effect of Fe2O3 on activity, crystal structure, basicity, and stability of the catalyst and also on the role of Fe2O3 in the mercaptan oxidation processes. Test results have shown that the Fe2O3/MgO/Al2O3- CoPcS catalyst has a higher initial activity and a much longer service life than the MgO/Al2O3-CoPcS catalyst. The increased types of basic sites coupled with an enhanced oxidation ability resulted from the addition of Fe2O3 have contributed to the improvement of the catalytic activity of the MgO/Al2O3-CoPcS catalyst. 展开更多
关键词 mercaptan oxidation solid base fe2o3/Mgo/al2o3
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纳米Al_2O_3-Fe_3O_4/FeS固体润滑复合层减摩润滑机理 被引量:7
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作者 胡春华 杨春燕 +3 位作者 刘庆存 孙志杰 马世宁 乔玉林 《材料热处理学报》 EI CAS CSCD 北大核心 2013年第6期130-135,共6页
采用离子氮碳共渗与离子渗硫复合处理技术在45钢表面形成FeS固体润滑复合层,然后采用真空浸渍方法将纳米Al2O3和Fe3O4颗粒置入复合层的微纳孔隙中,制备成纳米Al2O3-Fe3O4/FeS固体润滑复合层。在10~60 N的载荷下,纳米Al2O3-Fe3O4/FeS固... 采用离子氮碳共渗与离子渗硫复合处理技术在45钢表面形成FeS固体润滑复合层,然后采用真空浸渍方法将纳米Al2O3和Fe3O4颗粒置入复合层的微纳孔隙中,制备成纳米Al2O3-Fe3O4/FeS固体润滑复合层。在10~60 N的载荷下,纳米Al2O3-Fe3O4/FeS固体润滑复合层表现出优良的减摩与耐磨性能。这是因为,一方面磨损表面生成的化学反应膜,起到了固体润滑和阻碍摩擦表面间金属直接接触的作用;另一方面在摩擦过程中,纳米Al2O3-Fe3O4/FeS固体润滑复合层中的纳米Al2O3和Fe3O4颗粒起到了'微纳滚珠'作用,微观上将'滑动摩擦'部分转变为'滚动摩擦',且纳米颗粒预先置入复合膜层中,在摩擦过程中不易流失,延长了其'微纳滚珠'的作用,从而使其摩擦因数(载荷60 N时)及体积磨损量比涂抹纳米Al2O3/Fe3O4复合添加剂润滑的FeS固体润滑复合层分别降低了7.2%和50%。 展开更多
关键词 feS固体润滑复合层 纳米al2o3-fe3o4 化学反应膜 减摩耐磨 润滑机理
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