At present, the dominant technology for olefin/ paraffin separations is cryogenic distillation, which is extremely energy-intensive. Developing advanced adsorbent materials would be a first step toward cost-effective alternatives such as pressure swing adsorption or temperature swing adsorption. In this work, we report a silver-decorated hafnium metal−organic framework, NUS-6(Hf)-Ag, as a C 2 H 4 -selective adsorbent for C 2 H 4 /C 2 H 6 separation. NUS-6(Hf)-Ag was synthesized by the modulated hydrothermal approach followed by ion-exchange reactions. The successful introduction of Ag(I), confirmed by X-ray photoelectron spectroscopy and energy-dispersive spectroscopy, increased the ideal C 2 H 4 /C 2 H 6 selectivity of the resultant NUS-6(Hf)-Ag material to 6, which was 5 times that of NUS-6(Hf). Breakthrough experiments further confirmed the C 2 H 4 / C 2 H 6 separation performance of NUS-6(Hf)-Ag, indicating coadsorption C 2 H 4 /C 2 H 6 selectivities greater than 3. In addition, NUS-6(Hf)-Ag was found to maintain its crystallinity and the oxidation state of Ag(I) after recyclability tests. This study clearly demonstrates the promising potential of Ag-decorated metal−organic frameworks as adsorbent materials in adsorption-based C 2 H 4 /C 2 H 6 separations.
■ INTRODUCTIONShort-chain olefins are among the most important feedstocks for the chemical industry. 1 Currently, light olefins are mainly obtained from the steam cracking of naphtha or ethane, involving extensive operations for olefin/paraffin separation. 2,3 Owing to the similar physical properties between olefins and paraffins, the industrial separation of their mixtures is performed by cryogenic distillation using distillation towers with more than 150 trays operating at high pressures (7−28 bar) and low temperatures (183−258 K). 4 Such energyintensive processes constitute about 20% of the energy consumption of the overall cracking process, whose energy cost is 26−31 GJ/t (in terms of ethylene) for naphtha cracking and 17−21 GJ/t for ethane cracking. 1,5 Considering the huge market for short-chain olefins, even a small improvement in the olefin/paraffin separation process to reduce energy consumption can make a significant difference in terms of reducing the operating costs and carbon footprint. 6 Several alternative processes for olefin/paraffin separation with lower energy consumption and operating costs have been studied, 7−9 one of which is membrane-based separation using facilitated-transportation membranes. 10−14 The essential working principle of this type of membrane is the double bonding between metal ions (e.g., silver ion) and olefin molecules. The σ components of these bonds are formed by the overlap of the full π molecular orbitals of the olefins with the vacant outermost s orbitals of the metal, whereas the π components result from the back-donation of electrons from the full outer d orbitals of Ag(I) to the vacant π* orbitals of the olefins. 5,11 Another approach is adsorption-based separation such as pressure swing adsorption (PSA), ...