K8-11耐硫变换催化剂使用前后性能测试及评价

采用常压微反色谱、原粒度加压评价装置和XRD等技术，对K8-11新鲜样和工业失活后样品的活性、杂质及毒物以及烧炭再生性能进行了测试和评价．得到了一点对工业催化剂的使用可能有参考价值的信息。     

阴离子-非离子共模板法制备Pt/K/TiO2-Al2O3催化剂

采用阴离子型表面活性剂SDS（十二烷基硫酸钠）和非离子型表面活性剂OP（聚乙二醇辛基苯基醚）做为共模板剂,采用柠檬酸络合-有机模板剂分解耦合法成功制备了介孔TiO2-Al2O3载体及其负载型NSR催化剂。BET测试结果表明：采用共模板剂法制备的TiO2-Al2O3载体比表面积高达398 m2/g,而使用单一模板剂CTAB或传统共沉淀法制备的载体其比表面积分别只有373和250 m2/g。H2-Chemisorption、XRD和NH3-TPD等表征结果显示,该载体同时具有更高的Pt分散度和表面酸量。负载后,所得Pt/K/TiO2-Al2O3催化剂表现出更高的NOx储存量（比传统共沉淀法样品提高62.1%）和抗硫性能（硫化再生效率达到91%）。     

A nickel tetra-coordinated complex as catalyst in heterogeneous hydrogenation

The [NiCl₂(NH₂(CH₂)₁₂CH₃)₂] complex supported on γ-Al₂O₃ produces a catalyst which is considerably more active and sulfur-resistant for the hydrogenation of cyclohexene carried out in mild conditions than a conventional catalyst obtained from acid solutions of NiCl₂ and even than the same complex unsupported. As determined by XPS, the active species is the complex itself, which is stable under the reaction conditions. The higher sulfur-resistance is attributed to electronic and geometrical effects. The catalyst system is considerably more resistant to poisoning with thiophene than with tetrahydrothiophene. © 1998 SCI     

四元复合氧化物La_(0.5)Sr_(0.5)Ni_(0.5)Cu_(0.5)O_3的抗硫性能

以SO2 为毒物 ,采用脉冲中毒方法 ,再以CO氧化反应为探针 ,对三元复合氧化物催化剂La0 .5Sr0 .5NiO3 与La0 .5Sr0 .5CuO3 以及四元复合氧化物催化剂La0 .5Sr0 .5Ni0 .5Cu0 .5O3 等三种催化剂样品的抗硫毒能力、失活曲线、中毒催化剂的再生性能以及毒物残留形态等进行了全面考察和对比分析。实验结果表明四元复合氧化物催化剂La0 .5Sr0 .5Ni0 .5Cu0 .5O3 在SO2 毒物含量是 1 2 2×10 -2 mmol时 ,特别是在高温 (≥ 30 0℃ )条件下 ,具有优异的抗硫性能     

Ni-Mo双金属催化剂的甲烷化性能与耐硫稳定性

采用沉淀-浸渍法合成一系列Ni-Mo基双金属催化剂,在固定床反应器中对其催化活性和耐硫性能进行评价,并辅以不同的表征手段阐释其作用机理。实验结果表明,以MCM-41分子筛为载体的催化剂活性和稳定性优于以NaY、γ-Al₂O₃和拟薄水铝石（PB）为载体的催化剂;反应前后催化剂的表征结果则说明Ni-Mo分子间适宜的相互作用是决定催化剂性能的关键。MCM-41载体催化剂中适宜的Ni-Mo分子间相互作用使得此催化剂中活性组分与载体间的相互作用适中,还原后的活性金属Ni能够均匀分散在载体表面,从而提高了催化剂的耐硫稳定性和抗积炭能力。不同Ni-Mo比同样会影响Ni-Mo分子间的相互作用,通过考察确定20Ni-10Mo/MCM-41的活性和稳定性最优。     

Thiophene Poisoning and reactivation of a supported nickel hydrogenation catalyst: The effect of temperature

The extent and type of poisoning of an 8 wt% Ni/γ-Al₂O₃ catalyst by thiophene has been examined in ethylbenzene hydrogenation reaction, between 403 and 523 K. The results suggest that at the higher temperatures the deactivation can take place through two different mechanisms. In one case, the formation of ‘Ni-S’ surface species on the more active sites at the beginning of the reaction, produces a slow and irreversible poisoning. In the other, the planar adsorption of thiophene on the other sites produces a fast and reversible deactivation. At lower temperatures, the second mechanism seems to be predominant due to the fact that the hydrogenolysis activity diminishes.