己烷
材料科学
石油化工
选择性
吸附
碳氢化合物
辛烷值
萃取(化学)
扩散
工作(物理)
碳氢化合物混合物
精炼(冶金)
结构异构体
化学工程
热的
动力学
热力学
纳米技术
选择性吸附
金属有机骨架
分子动力学
吞吐量
分子
分子扩散
有机化学
热扩散率
化学物理
烷烃
作者
F. Wang,Ziming Ye,Haorong Li,Hongyu Lin,Shengchang Xiang,Banglin Chen,Fan Xi,Zhangjing Zhang
标识
DOI:10.1002/adfm.202528297
摘要
ABSTRACT The separation of hexane isomers remains one of the most demanding challenges in petrochemical refining due to their nearly identical physicochemical properties. Conventional vapor‐phase adsorption or liquid‐phase extraction using metal–organic frameworks (MOFs) is constrained by low throughput and sluggish kinetics. Here we introduce a heteroporous titanium–cobalt MOF, TiCo‐TPT , that harmonizes diffusion kinetics and thermodynamic selectivity through a dual‐cage framework design. The robust Ti─O─Co network endows exceptional chemical and thermal stability, while the coexistence of narrow and wide cages enables both rapid molecular transport and size‐selective adsorption. TiCo‐TPT exhibits record adsorption capacities for n ‐hexane (4.77 mmol/g) and 3‐methylpentane (4.47 mmol/g), outperforming all previously reported rigid MOFs capable of discriminating between mono‐ and dibranched isomers. More importantly, TiCo‐TPT achieves continuous‐flow liquid‐phase separation of hexane isomers under ambient conditions, yielding high‐purity 2,2‐dimethylbutane with >99.9% purity and significantly enhanced octane number. This work establishes a design paradigm for heteroporous MOFs, demonstrating how multiscale pore environments can overcome the kinetic–thermodynamic trade‐off that has long limited molecular separations, thereby opening new avenues for energy‐efficient hydrocarbon upgrading.
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