Gounder Rajamani, Iglesia Enrique
Department of Chemical Engineering, University of California at Berkeley, Berkeley, California 94720, USA.
J Am Chem Soc. 2009 Feb 11;131(5):1958-71. doi: 10.1021/ja808292c.
The location of Brønsted acid sites within zeolite channels strongly influences reactivity because of the extent to which spatial constraints determine the stability of reactants and of cationic transition states relevant to alkane activation catalysis. Turnover rates for monomolecular cracking and dehydrogenation of propane and n-butane differed among zeolites with varying channel structure (H-MFI, H-FER, H-MOR) and between OH groups within eight-membered ring (8-MR) side pockets and 12-MR main channels in H-MOR. Measured monomolecular alkane activation barriers depended on catalyst and reactant properties, such as deprotonation enthalpies and proton affinities, respectively, consistent with Born-Haber thermochemical cycles that define energy relations in acid catalysis. Monomolecular alkane cracking and dehydrogenation turnovers occurred with strong preference on acid sites contained within smaller 8-MR pockets in H-MOR, while rates on sites located within 12-MR channels were much lower and often undetectable. This strong specificity reflects transition states that are confined only partially within 8-MR pockets; as a result, entropic gains compensate for enthalpic penalties caused by their incomplete containment to give a lower free energy for transition states within small 8-MR side pockets. These effects of entropy are stronger for dehydrogenation, with a later and looser transition state, than for cracking in the case of both propane and n-butane; therefore, selectivity can be tuned by the selective positioning or titration of OH groups within specific environments, the number of which was assessed in H-MOR by rigorous deconvolution of their infrared spectra. Specifically, cracking-to-dehydrogenation ratios for propane and n-butane were much smaller and terminal-to-central C-C bond cleavage ratios for n-butane were much larger on 8-MR than on 12-MR acid sites as a result of partial confinement, a concept previously considered phenomenologically as pore mouth catalysis. These marked effects of spatial constraints and of entropic factors on acid site reactivity and selectivity, also inferred for MFI from titration of OH groups by Na(+), have not been previously proposed or recognized and appear to be unprecedented in hydrocarbon catalysis. These findings and their conceptual interpretations open opportunities for the design of microporous solids by the rational positioning of acid sites within specific channel locations and with predictable consequences for catalytic rates and selectivities.
由于空间限制决定反应物和与烷烃活化催化相关的阳离子过渡态稳定性的程度,沸石通道内布朗斯特酸位点的位置对反应活性有强烈影响。丙烷和正丁烷的单分子裂解和脱氢转化率在具有不同通道结构的沸石(H-MFI、H-FER、H-MOR)之间以及H-MOR中八元环(8-MR)侧袋内的OH基团与12-MR主通道内的OH基团之间存在差异。测得的单分子烷烃活化能垒分别取决于催化剂和反应物的性质,如去质子化焓和质子亲和力,这与定义酸催化中能量关系的玻恩-哈伯热化学循环一致。单分子烷烃裂解和脱氢转化在H-MOR中较小的8-MR袋内的酸位点上有很强的偏好,而位于12-MR通道内的位点上的速率要低得多,且常常无法检测到。这种强烈的特异性反映了过渡态仅部分限制在8-MR袋内;因此,熵增补偿了由于其不完全容纳而导致的焓罚,从而使小8-MR侧袋内的过渡态具有更低的自由能。对于脱氢反应,由于过渡态更靠后且更松散,熵的这些影响比丙烷和正丁烷裂解时更强;因此,可以通过在特定环境中选择性地定位或滴定OH基团来调节选择性,在H-MOR中通过对其红外光谱进行严格的反卷积来评估OH基团的数量。具体而言,由于部分限制,丙烷和正丁烷在8-MR上的裂解与脱氢比率要小得多,正丁烷在8-MR上的端基与中心C-C键裂解比率比在12-MR酸位点上大得多,这一概念以前在现象学上被视为孔口催化。空间限制和熵因素对酸位点反应活性和选择性的这些显著影响,从通过Na(+)滴定OH基团也可推断出对MFI的影响,以前尚未被提出或认识到,在烃类催化中似乎也是前所未有的。这些发现及其概念性解释为通过在特定通道位置合理定位酸位点来设计微孔固体提供了机会,并对催化速率和选择性产生可预测的影响。