Ru-La2O3/Al2O3催化剂上CO选择氧化本征反应动力学

采用浸渍法制备了用于CO选择氧化的Ru-La2O3/Al2O3催化剂,研究了CO在Ru-La2O3/Al2O3催化剂床层上的CO选择氧化本征动力学.结果表明,在消除内外扩散的条件下,CO在Ru-La2O3/Al2O3催化剂床层的本征反应是一个表面反应控制的一级反应,反应的活化能为76.24kJ/mol.     

Ni/Al_2O_3及La改性Ni/Al_2O_3催化CO浆态床甲烷化性能

采用等体积浸渍法制备了Ni/Al2O3及La改性的Ni-La/Al2O3催化剂,并考察了其浆态床CO甲烷化反应性能。借助XRD、H2-TPR、CO-TPD、H2-TPD等对催化剂进行了表征。结果表明,La助剂改性制备的Ni-La/Al2O3催化剂较Ni/Al2O3催化剂具有更高的CO甲烷化活性,La助剂的添加促进了Ni物种在载体表面的分散,降低了还原温度,增强了催化剂对CO和H2的吸附能力。La助剂的添加次序对甲烷化活性影响较大,采用共浸渍法制备的催化剂具有最佳的甲烷化活性,CO转化率达到96.3%,CH4选择性和时空收率分别达到87.1%和179.6 m L·kg-1·h-1,优于先浸渍Ni后浸渍La或先浸渍La后浸渍Ni制备的催化剂。     

高活性PtMo_2C/Al_2O_3催化剂的研究进展

叙述了高活性PtMo2C/Al2O3催化剂的制备、性能和在水气位移反应中的应用。由于制备出的PtMo2C/Al2O3催化剂中,其铂离子呈几个纳米分散态显微结构,分布十分均匀,它比传统的催化剂如CuZn/Al2O3、Pt/C、Pt/Al2O3和PtCeO2等的催化活性高,选择性好,WGS速率高,反应温度低。     

Al_2O_3La_2O_3Y_2O_3/Cu复合材料的电弧侵蚀特性研究

采用喷射沉积和内氧化法制备出Al2O3La2O3Y2O3/Cu复合材料,研究该材料在直流20 V/20 A的工作条件下触点的电弧侵蚀特性,并与Al2O3/Cu材料进行了对比分析.利用电子天平、扫描电镜等方法分析电弧侵蚀后触点的质量变化和表面微观结构.结果表明,通过添加Y2O3、La2O3稀土氧化物颗粒,可有效降低触头材料的材料转移量.Al2O3La2O3Y2O3/Cu材料的抗熔焊性和抗烧损性优于Al2O3/Cu材料的性能.在直流阻性负载条件下Al2O3La2O3Y2O3/Cu阳极触头表面形成凹坑,阴极触头表面形成凸起,触点表面显示出浆糊状凝固物和喷发坑等电弧侵蚀形貌特征.     

热压反应合成Al_2O_3-Ho_2O_3/TiAl复合材料

利用Al-Ti-TiO2-Ho2O3体系原位反应合成了Ho掺杂Al2O3/TiAl复合材料。采用DTA结合XRD分析对体系反应过程进行了探讨。借助XRD、EDS和SEM等手段,对放热体系的物相组成及晶粒微观形貌进行了分析表征。结果表明:Al-Ti-TiO2-Ho2O3系原位合成的Al2O3/TiAl复合材料由TiAl、Ti3Al、Al2O3以及HoAl3相组成;Ho2O3的引入对基体相生成比例(TiAl:Ti3Al)有一定的调控作用,并使得基体晶粒和Al2O3晶粒均有所细化且逐渐分布均匀。力学性能测试表明:当Ho2O3的引入量为6%时,材料的抗弯强度达到最大值,约为593.5MPa;断裂韧度达到最大值,为8.74MPa.m1/2,具有可接受的力学性能。     

机械合金化3Y_2O_3-5Al_2O_3粉末的研究

研究了转速,球磨时间等球磨工艺对3Y2O3-5Al2O3机械合金化过程的影响。结果表明:在较低的转速下(250r/min),提供的球磨能量很低,只会细化粉体颗粒;提高转速(400r/min),会促使Y2O3发生晶型转变,由稳定的立方晶转变成非稳态的单斜晶;继续提高转速(500r/min),还会使混合粉体发生合成反应,生成YAlO3(YAP)。在转速为500r/min,球料比为20∶1的球磨条件下,3Y2O3-5Al2O3粉体发生固相反应的过程可分为两个阶段:第一阶段,Al2O3颗粒晶格畸变,快速细化;同时,高能球磨促使Y2O3发生了晶型转变。第二阶段,Y2O3晶型转变基本完成,并呈无定形化,Y2O3和Al2O3发生合成反应,生成YAlO3(YAP)。但在球磨条件下,难以合成Y3Al5O12(YAG)、Y4Al2O9(YAM)。     

AgO/Al_2O_3催化剂选择还原氮氧化物的研究

对浸渍法和水热共沉淀法制备的AgO/Al2O3催化剂进行了选择还原氮氧化物的研究。结果表明:催化剂制备方法对催化剂的催化效果起重要作用,水热共沉淀法制备的AgO/Al2O3催化剂要比浸渍法制备的更有活性;引入不同的还原剂表现出不同的还原性能,水热共沉淀法制备的AgO/Al2O3催化剂具有更强的抗水抗硫性能。AgO与高比表面积Al2O3之间的强相互作用是水热共沉淀法制备的AgO/Al2O3催化剂具有高选择还原活性的原因所在。催化剂表面吸附的氧气很大程度上促进了氮氧化物的选择性氧化过程。     

La_2O_3/La_2O_2CO_3纳米复合材料的凝胶燃烧法合成

采用燃烧法合成了纳米La2O3/La2O2CO3复合材料,以六水合硝酸镧和一水合柠檬酸分别为镧源和络合剂,以氨水调节p H值,p H=2~4、柠檬酸与硝酸镧的摩尔比在1.0~1.2∶1.0之间,将得到的凝胶加热到一定温度发生自蔓延燃烧反应,燃烧反应产物在600~700℃煅烧1~2 h,得到膨松粉末状纳米La2O3/La2O2CO3复合产物。煅烧温度和恒温煅烧时间不同,得到不同粒径和组分比例的纳米La2O3/La2O2CO3复合材料。利用X射线衍射(XRD)、差热-热重分析(TG-DTA)和透射扫描电镜(TEM)等测试方法对凝胶热分解过程产物及最终形成的纳米La2O3/La2O2CO3复合产物粉体进行了分析和表征,产物的平均粒径在30~100 nm之间可控。纳米La2O3/La2O2CO3复合产物中的纳米La2O3在空气中具有不稳定性,极易与空气中的H2O发生反应生成La(OH)3,生成了La(OH)3/La2O2CO3复合产物,而产物在650℃煅烧2 h后即可完全转化为La2O3/La2O2CO3复合产物,说明这个过程是可逆的。     

CaO-SiO_2-Na_2O-CaF_2-Al_2O_3-MgO保护渣系的Al_2O_3吸收速率和粘度

采用CaO -SiO2 -Na2 O -CaF2 -Al2 O3-MgO渣系 ,通过测定熔渣的粘度和Al2 O3吸收速率 ,研究连铸保护渣的Al2 O3吸收速率与粘度及化学成分之间的关系。在一定条件下 ,当CaO SiO2 为1 .2左右时 ,粘度达到最小值 ,Al2 O3吸收速率达到最大值 ,分别为 0 .1 0Pa·s、8.4 0 3× 1 0 - 4 kg·m- 2 ·s- 1 。随着渣中Na2 CO3含量、CaF2 含量和MgO含量的增加 ,粘度减小 ,Al2 O3吸收速率增大。随着渣中Al2 O3含量的增加 ,粘度增大 ,Al2 O3吸收速率减小。粘度为Al2 O3吸收速率的主要控制因素。随着熔渣粘度的增加 ,连铸保护渣的Al2 O3吸收速率逐渐减小。     

Al_2O_3预包覆尖晶石LiMn_2O_4的电化学性能

将Li2CO3和电解二氧化锰混合球磨,得到尖晶石(LiMn2O4,简称为LMO)的前驱体,采用化学沉积法在前驱体的预烧产物表面包覆Al(OH)3,然后在750℃/6h条件下煅烧,得到Al2O3/LiMn2O4复合粉末(称为Al2O3预包覆,包覆粉末记为P-LMO);同时采用传统方法,在前驱体的煅烧产物(LiMn2O4粉末)表面包覆Al(OH)3,然后在300℃/3h条件下热处理,得到Al2O3/LiMn2O4复合粉末(称为煅烧包覆,复合粉末记为C-LMO),对这2种包覆法制备的Al2O3/LiMn2O4复合粉末的物相结构、形貌、包覆层的厚度与粒度分布等进行对比分析,并对包覆粉末进行电化学性能测试。结果表明,Al2O3均匀地包覆在LiMn2O4的表面,包覆层厚度约为10nm;Al2O3/LiMn2O4复合粉末的晶格常数随Al2O3包覆量增加而增加;预包覆粉末颗粒呈类球形,平均粒径(0.3μm)明显小于煅烧包覆的平均粒径(0.5μm);预包覆粉末的Al2O3包覆层能有效减少循环过程中电荷转移阻抗的增加,并减少Mn的溶解,其循环性能优于煅烧包覆粉末。在3.2~4.5V的充放电区间内,Al2O3包覆量(摩尔分数)为2%的预包覆LiMn2O4材料显示出优良的电化学性能,55℃下0.1C的首次放电容量为114.0(mA·h)/g,0.5C倍率下50次循环后容量保持率为87.3%。     

CeO2-Co3O4 Catalysts for CO Oxidation

CeO2-Co3O4 catalysts for low-temperature CO oxidation were prepared by a co-precipitation method. In combination with the characterization methods of N2 adsorption/desorption, XRD, temperature-programmed reduction （TPR）, and FT-IR, the influence of the cerium content on the catalytic performance of CeO2-Co3O4 was investigated. The results indicate that the prepared CeO2-Co3O4 catalysts exhibit a better activity than that of pure CeO2 or pure Co3O4. The catalyst with the Ce/Co atomic ratio 1 ： 16 exhibits the best activity, which converts 77% of CO at room temperature and completely oxidizes CO at 45 ℃.     

Catalytic Synthesis of Tert-Butyl Acetate by Nd2O3/Al2O3-Nd2O3/ZnO

Nd2O3 was used to support Al2O3 and ZnO to prepare a supported solid base catalyst and investigate the effect of catalyst and reaction conditions on the synthesis of tert-butyl acetate. The composited oxide of Nd2O3/Al2O3-Nd2O3/ZnO exhibited excellent catalytic activity for the synthsis of tert-butyl acetate. The molar ratio of tert-butanol to acetic anhydride is 31, the catalyst in total amount of reactant nearly 0.5%, and reaction time 6 h. With the above conditions, yield of the reaction could reach to 65%. The structure of product were verified by the FT-IR, Element analysis, and MS, which proved that the product was tert-butyl acetate.     

Catalytic Incineration of Acrylonitrile with Platinum Supported on Al2O3

The catalytic decomposition of acrylonitrile with catalysts was investigated in a bench scale fixed bed reactor in this study. Two catalysts, including Pt/γ-Al2O3 and Cr2O3/α-Al2O3, were tested to study their catalytic activity in the complete oxidation of acrylonitrile. The results show that the Pt/γ-Al2O3 catalyst has better performance. The operating parameters such as operating temperature, acrylonitrile concentration, space velocity, and oxygen concentration were conducted in a series of experiments on the Pt/γ-Al2O3 catalyst. The results indicate that decomposition efficiency increases with temperature and oxygen concentration and decreases with the increases of space velocity and acrylonitrile concentration. With a regression model, the operating temperature is the most effective parameter on the decomposition of acrylonitrile. Carbon dioxide is the dominant product and carbon monoxide is an insignificant product of the decomposition of acrylonitrile. Material balance on carbon is good for the experiments. According to the BET and elemental analyzer analysis, major factors that cause the deactivation effect may result from nitrogen poisoning and carbon masking on the catalyst surface, especially at lower temperatures.     

Preferential Oxidation of Carbon Monoxide in Excess Hydrogen over Au/Co3O4-CeO2 Catalysts

Fuel cells are considered to be the propulsionsystem of the near future,since they can produceelectricity without pollutingthe environment,and pos-sess the necessary specific power,power density anddurability to replace conventional internal combustioneng…     

O2/N2与O2/CO2气氛下Fe2O3与K2CO3对无烟煤催化燃烧反应性的影响

利用综合热分析仪研究了O2/N2与O2/CO2气氛下Fe2O3与K2CO3对无烟煤催化燃烧反应性的影响。结果表明,在O2/CO2气氛下,Fe2O3与K2CO3均可以催化无烟煤粉的燃烧,但其催化作用要弱于O2/N2气氛,且在低氧气浓度的O2/CO2气氛下对Fe2O3与K2CO3的抑制作用大于高氧气浓度。氧气浓度为20%~80%时,K2CO3在O2/N2气氛下催化煤粉前期燃烧使燃烧由反应控制转变为扩散控制,Fe2O3则只在氧气浓度为20%时能改变煤粉前期燃烧的控制步骤;而Fe2O3与K2CO3在O2/CO2气氛下均只能在氧气浓度为20%时改变煤粉前期燃烧的控制步骤,由反应控制转变为扩散控制。     

Preferential Oxidation of CO in H2 over CuO／CeO2 Catalysts

Over the past few years, the design and researchon fuel cells have been made a great development. Avariety of fuel cells for different applications has beenunder development[1,2]: solid polymer fuel cells(SPFC), also know as proton exchange …     

Influence of V2O5 Addition on Reduction of NO by C3H6 over Pt/V2O5/Al2O3 Monolithic Catalyst

Pt/V2O5/Al2O3 and Pt/Al2O3 monolithic catalysts were prepared by wet impregnation method, and the influence of V2 O5 addition on the catalytic activity for NO reduction by C3 H6 under lean burn condition was investigated in detail.The results show that Pt/V2O5/Al2O3 has better activity of NO reduction than Pt/Al2O3 , adding V2O5 to Pt catalyst makes the temperature window of NO reduction shift further to a lower temperature region.The activity of NO reduction decreases and there is a similar degree of deactivation over the two catalysts in the presence of SO2 in feed gas.Moreover, adding V2 O5 to Pt catalyst resulted in improvement of resistance to SO2 oxidation, which decreases the emission of sulfate particulate.Thermal aging treatment counteractes the promoting effect of V2O5 on NO reduction.     

Catalytic Reduction of SO2 on CeO2-La2O3 Rare Earth Mixed Compounds

Adding rare earth oxide CeO2 with variable valences to La2O3 formed a mixture of rare earth oxides. By means of dipping CeO2, La2O3 and their mixture, whose carriers were all γ-Al2O3, were used as the catalyst for the reduction of SO2 by CO. The activation process of this catalyst and the impact of temperature and reactant concentration on the activation process were investigated. Using X-ray diffraction, the structure characteristics of catalyst before and after reaction were analyzed to reveal the change of phase structure. The result shows that the rare earth oxide mixtures composing of CeO2 and La2O3, as the catalyst for the reduction of SO2 by CO, diminish activation temperature 50～100℃ less and have higher activity than a single oxide CeO2 or La2O3. The reason possibl is that La2O3 goes into in the lattice of CeO2 to form solid phase complex CeO2-La2O3 and increases the capability of CeO2-La2O3/γ-Al2O3 catalyst to store oxygen, which supplies the redox of CeO2 reaction with a better condition. At the same time, elemental sulfur formed in the redox reaction impels La203 to be transformed to activation phase La2O2S in a lower temperature, which can be explained with the synergism between redox reaction and COS intermediate mechanism reaction.     

Partial Oxidation of Methane to Syngas over Monolithic Ni/γ-Al2O3 Catalyst——Effects of Rare Earths and Other Basic Promoters

A series of monolithic Ni/γ-Al2O3 catalysts with and without basic promoters (Na, Sr, La, Ce) were prepared. Partial oxidation of methane (POM) to syngas was carried out in a continuous-flow, fixed-bed reactor. The influences of reaction conditions, including temperature, CH4/O2 ratio and space velocity, on the performance of the catalyst were investigated. The results show that at a high space velocity of 1×105 h-1, optimal CH4 conversion can be obtained. Effects of promoters such as Na, Sr, Ce, La were also investigated, and the catalyst samples were characterized by means of temperature-programmed reduction and XRD techniques. XRD suggests that the addition of promoters has no influence on the crystal structure of Ni/γ-Al2O3 catalyst. The results show that the addition of a small amount of promoters improves the reducibility and activity of the catalyst. The side reaction CH4 2 O2→CO2 H2O, is fully restrained and 100% H2 selectivity is achieved when Ce and La are used as promoters, respectively.     

稀土在负载型非晶态NiB/Al2O3合金上作用研究

本文采用脉冲技术研究了稀土氧化物对负载型非晶态 Ni B/Al2 O3合金催化剂苯加氢活性和抗硫性能的影响。用 XRD鉴定了非晶态结构 ,用 TPR、TPD表征了催化剂的表面性质 ,用 CO化学吸附法测定了活性镍表面积。实验结果表明 ,非晶态合金催化剂上至少有两种吸附中心 ,稀土氧化物能明显地提高催化剂的苯加氢活性和抗硫性能 ,其原因是稀土氧化物有助于氧化镍的还原 ,从而在反应温度下有更多的活性镍物种被还原 ,稀土氧化物还能使镍物种颗粒细化 ,提高了活性镍面积。