Apr 24, 2024
5:00pm - 7:00pm
Flex Hall C, Level 2, Summit
Donghyun Kim1,2,Bao Nguyen Truong1,Donghui Jo1,Ji woong Yoon1,Su-Kyung Lee1,Youn-Sang Bae2,Kyung-Ho Cho1,U-hwang Lee1
Korea Research Institute of Chemical Technology1,Yonsei University2
Donghyun Kim1,2,Bao Nguyen Truong1,Donghui Jo1,Ji woong Yoon1,Su-Kyung Lee1,Youn-Sang Bae2,Kyung-Ho Cho1,U-hwang Lee1
Korea Research Institute of Chemical Technology1,Yonsei University2
Single-step purification of the ternary C
2 hydrocarbon mixture to produce ethylene (C
2H
4) directly using adsorption-based technologies is desirable for reducing large energy consumption. However, it is challenging to develop an appropriate adsorbent, having preferential adsorption characteristics toward ethane (C
2H
6) and acetylene (C
2H
2) rather than C
2H
4 coupled with high adsorption capacity owing to their similar physicochemical properties. Herein, we present a highly stable, cheap, and scalable CAU-23 adsorbent, which enables single-step production of high-purity C
2H
4 (>99.9%) from the ternary C
2 hydrocarbon mixture. CAU-23 exhibited higher uptake capacity of C
2H
6 (4.0 mmol g
−1) and C
2H
2 (4.7 mmol g
−1) compared to that of C
2H
4 (3.8 mmol g
−1). Further, it showed the reasonable selectivity for both C
2H
6/C
2H
4 (1.54) and C
2H
2/C
2H
4 (1.5) with an equimolar binary mixture, indicating that the separation performance of CAU-23 is comparable to the benchmark porous materials for separating C
2 ternary gas mixture. The breakthrough experiments demonstrated its capability to produce high-purity C
2H
4 (>99.9%) with various C
2H
6/C
2H
4/C
2H
2 compositions at 298 K and 1 bar with high recyclability. The origin of the separation performance was further explored by using computational simulations of the grand canonical Monte Carlo (GCMC) and density functional theory (DFT).