Sanchez-Castillo Marco A, Madon Rostam J, Dumesic James A
Department of Chemical Engineering, University of Wisconsin, Madison, Wisconsin 53706, USA.
J Phys Chem B. 2005 Feb 17;109(6):2164-75. doi: 10.1021/jp0489875.
Reaction kinetics data were collected for isobutane conversion over a series of ultra stable Y (USY) zeolite catalysts with and without rare earth cations and subjected to various extents of dealumination by steaming. We conducted these reaction studies at low temperatures (523-573 K) using isobutane feed streams containing known levels of isobutylene (100-400 ppm) so that the kinetics were controlled by bimolecular hydride transfer and oligomerization/beta-scission processes with little or no participation of monomolecular initiation reactions. These experimental conditions led to stable catalyst performance with the main products of isobutane conversion being propane, n-butane, and isopentane, with smaller amounts of propylene, trans-2-butene, and cis-2-butene. The rates of formation of these products per Brønsted acid site (as counted by pyridine adsorption) depended exponentially on Brønsted acid site density, regardless of whether the catalyst contained rare earth cations. Kinetic modeling showed an exponential dependence of hydride transfer and oligomerization/ beta-scission reaction rates on Brønsted acid site density which translated into composite activation energies for these reactions having a linear relationship with site density. Based on results in the literature from theoretical calculations, we suggest that increasing Brønsted acid site density in zeolite Y leads to larger zeolite elasticity, increased stabilization of cationic transition states, and lower composite activation barriers for hydride transfer and beta-scission steps. The role of rare earth cations, therefore, is to ensure the retention of high Brønsted acid site density under hydrothermal conditions, such as in fluid catalytic cracking (FCC) regenerators, where steam would dealuminate the Y zeolite framework and reduce this site density. It is for this reason that hydride transfer reaction rates are high in the presence of rare earth cations and lead to higher yields of less olefinic gasoline during FCC.
收集了一系列有或没有稀土阳离子的超稳Y(USY)沸石催化剂上异丁烷转化的反应动力学数据,这些催化剂通过蒸汽处理进行了不同程度的脱铝。我们在低温(523 - 573 K)下使用含有已知水平异丁烯(100 - 400 ppm)的异丁烷进料流进行这些反应研究,以便动力学由双分子氢化物转移和齐聚/β-断裂过程控制,单分子引发反应很少或没有参与。这些实验条件导致催化剂性能稳定,异丁烷转化的主要产物是丙烷、正丁烷和异戊烷,还有少量的丙烯、反-2-丁烯和顺-2-丁烯。每个布朗斯台德酸位(通过吡啶吸附计数)的这些产物生成速率与布朗斯台德酸位密度呈指数关系,无论催化剂是否含有稀土阳离子。动力学建模表明氢化物转移和齐聚/β-断裂反应速率与布朗斯台德酸位密度呈指数关系,这转化为这些反应的复合活化能与酸位密度呈线性关系。基于理论计算的文献结果,我们认为增加Y型沸石中的布朗斯台德酸位密度会导致更大的沸石弹性、阳离子过渡态稳定性增加以及氢化物转移和β-断裂步骤的复合活化能降低。因此,稀土阳离子的作用是确保在水热条件下,如在流化催化裂化(FCC)再生器中,保持高布朗斯台德酸位密度,在该条件下蒸汽会使Y型沸石骨架脱铝并降低酸位密度。正是由于这个原因,在稀土阳离子存在下氢化物转移反应速率很高,并导致FCC过程中烯烃含量较低的汽油产率更高。