吸附
乙炔
选择性
巴(单位)
材料科学
焓
化学工程
化学
热力学
有机化学
催化作用
工程类
物理
气象学
作者
Shuangqing Shang,Zhenwei Zhou,Hao Wang,Yanan Wang,Xing Liu,Zhenglong Zhu,Yong Chun Zeng,Cheng Liu,Hanting Xiong,Huan Liu,Fangxin Zhao,Jingwen Chen,Shixia Chen,Zhenyu Zhou,Jun Wang
标识
DOI:10.1002/anie.202503317
摘要
Integrating separation parameters such as high adsorption capacity and selectivity, moderate adsorption enthalpy (Qst), along with industrial factors including cyclic stability, cost‐effectiveness, and scalability into a single adsorbent remains highly challenging due to inherent trade‐offs among these properties. Herein, we strategically leverage the coordination modes of aliphatic ligands to significantly enhance C2H2/CO2 separation performance. The structure flexibility and pore metrics are finely modulated by hydroxylated aliphatic acid (DLmal). As a result, the rigid Zn‐bpy‐DLmal exhibits an exceptional C2H2 adsorption capacity of 1.4 mmol g‐1 at 0.01 bar, high C2H2/CO2 selectivity (49), and moderate C2H2Qst value (38.4 kJ mol‐1). Notably, it achieves record‐high C2H2 packing densities of 347 g L‐1 at 0.01 bar and 747 g L‐1 at 0.5 bar. Furthermore, the scale‐up production of Zn‐bpy‐DLmal to kilogram quantities has been successfully achieved at an estimated cost of $74 per kg. Dynamic breakthrough experiments confirm its practical C2H2/CO2 separation performance with excellent cyclability under high flow rates and both dry and humid conditions. Moreover, two‐bed pressure swing adsorption simulations demonstrate a high‐purity C2H2 (>99%) yield of 14.64 mol with a recovery of 88.2% per cycle.
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