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Updated: Jun 14, 2026

Ethylene Polymerizations Using Parallel Pressure Reactors and a Kinetic Analysis of Chain Transfer Polymerization
Published on: November 27, 2015
Benchmark Performance of One-Step Ethylene Separation: From Optimized Crystal Synthesis to Quantitative Mixture
Duo-Yu Lin1, Ding-Yi Hu1, Rong-Hua Wang1
1MOE Key Laboratory of Bioinorganic and Synthetic Chemistry, School of Chemistry, Sun Yat-Sen University, Guangzhou 510275, China.
None:
As highlighted by the development of C2H6-selective adsorbents for one-step separation of C2H4, adsorption is promising for chemical separation; however, the field still suffers from the lack of benchmark adsorbents and quantitative evaluation protocols. In this work, an amorphous-recrystallization method is developed to control the crystal size and morphology of the pioneering C2H6-selective adsorbent MAF-49. At the optimal crystal size, the C2H4 kinetic selectivity is negligible, enabling the highest productivity of 3.1 mmol cm-3 for one-step C2H4 purification from the 15:1 C2H4/C2H6 mixture. Larger crystals exhibit higher C2H4 kinetic selectivity, which sharply decrease the C2H4 purification performance and can even lead to apparent C2H4 selectivity. Switching the column breakthrough experiment from the conventional outlet concentration mode to the outlet flow-rate mode and modifying the RUPTURA simulation code enable the quantitative evaluation and prediction of key parameters for gas mixture adsorption and separation, such as purification productivity, adsorption amount, and selectivity.
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