Xiao Jianfei, Zhu Zhenliang, Zhang Min, Huang Yaoqi, Zhang Tian Cheng, Yuan Shaojun
Low-carbon Technology & Chemical Reaction Engineering Laboratory, School of Chemical Engineering, Sichuan University, Chengdu 610065, China.
School of Engineering and Applied Sciences, Harvard University, Cambridge, Massachusetts 02138, United States.
ACS Appl Mater Interfaces. 2025 Apr 9;17(14):21630-21642. doi: 10.1021/acsami.4c21500. Epub 2025 Mar 29.
The separation of methanol-to-olefin (MTO) products to obtain high-purity ethylene (CH) and propylene (CH) is a challenging yet critical task, as these compounds are essential industrial raw materials for polymer synthesis. However, developing adsorbents with high selectivity and productivity for CH/CH remains a significant challenge and an urgent necessity. In this study, a porphyrinyl metal-organic framework (MOF), Al-TCPP, was developed for the simultaneous recovery of CH and CH through a one-step adsorption-desorption process. Benefiting from its well-developed microporous structure and abundant N- and O-accessible sites, Al-TCPP demonstrated exceptional adsorption capacities and selectivity for CH and ethane (CH) over CH under ambient conditions. The adsorption capacities (in cm·g) reached 162.4 for CH and 118.5 for CH at 298 K and 100 kPa. The ideal adsorbed solution theory (IAST) selectivity values for CH/CH and CH/CH were 10.1 and 1.8, respectively. Thermodynamic studies and theoretical calculations revealed stronger interactions between CH and CH molecules with the Al-TCPP framework than with CH. Systematic breakthrough experiments demonstrated outstanding separation performance for binary CH/CH and CH/CH mixtures, as well as ternary CH/CH/CH mixtures, achieving record productivities of 150.2 and 86.5 L·kg for polymer-grade CH (≥99.9%) and CH (≥99.5%), respectively. Notably, the separation performance remained stable under variable flow rates, temperatures, humidities, and multiple adsorption-desorption cycles. Overall, this study highlighted Al-TCPP as a highly competitive adsorbent for addressing the challenges in MTO product separation. Moreover, it offered valuable insights into the design of MOFs with heteroatom-rich accessible sites for efficient separation of low-carbon hydrocarbons.
将甲醇制烯烃(MTO)产物分离以获得高纯度乙烯(CH₂)和丙烯(C₃H₆)是一项具有挑战性但至关重要的任务,因为这些化合物是聚合物合成必不可少的工业原料。然而,开发对C₂H₄/C₃H₆具有高选择性和高生产率的吸附剂仍然是一项重大挑战且迫在眉睫。在本研究中,开发了一种卟啉基金属有机框架(MOF),即Al-TCPP,用于通过一步吸附-解吸过程同时回收C₂H₄和C₃H₆。得益于其发达的微孔结构和丰富的可利用N和O位点,Al-TCPP在环境条件下对C₂H₄和乙烷(C₂H₆)表现出优于C₃H₆的出色吸附容量和选择性。在298 K和100 kPa下,C₂H₄的吸附容量(以cm³·g⁻¹计)达到162.4,C₃H₆的吸附容量达到118.5。C₂H₄/C₃H₆和C₂H₆/C₃H₆的理想吸附溶液理论(IAST)选择性值分别为10.1和1.8。热力学研究和理论计算表明,C₂H₄和C₂H₆分子与Al-TCPP框架之间的相互作用强于与C₃H₆的相互作用。系统的穿透实验表明,对于二元C₂H₄/C₃H₆和C₂H₆/C₃H₆混合物以及三元C₂H₄/C₂H₆/C₃H₆混合物,具有出色的分离性能,聚合物级C₂H₄(≥99.9%)和C₃H₆(≥99.5%)的生产率分别达到创纪录的150.2和86.5 L·kg⁻¹。值得注意的是,在可变流速、温度、湿度和多次吸附-解吸循环下,分离性能保持稳定。总体而言,本研究突出了Al-TCPP作为解决MTO产物分离挑战的极具竞争力的吸附剂。此外,它为设计具有富含杂原子的可利用位点的MOF以有效分离低碳烃提供了有价值的见解。