2022
DOI: 10.1016/j.ces.2022.117425
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Kinetic model of ethylene oxidation in the presence of both ethylene dichloride (1,2-dichloroethane) and carbon dioxide over a highly selective silver catalyst

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Cited by 5 publications
(2 citation statements)
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“…Therefore, exploring more costeffective catalytic materials with high H 2 O 2 utilization efficiency, as alternatives to Re, could enhance process viability and economic feasibility. 6 As a consequence, there is a need for more research efforts to explore alternative heterogeneous epoxidation catalysts. [7][8][9] In this pursuit, prior investigations have focused on catalysts composed of transition metals in higher oxidation states, which are supported on mesoporous silica materials (MSM), particularly MCM-41 and SBA-15.…”
Section: Introductionmentioning
confidence: 99%
“…Therefore, exploring more costeffective catalytic materials with high H 2 O 2 utilization efficiency, as alternatives to Re, could enhance process viability and economic feasibility. 6 As a consequence, there is a need for more research efforts to explore alternative heterogeneous epoxidation catalysts. [7][8][9] In this pursuit, prior investigations have focused on catalysts composed of transition metals in higher oxidation states, which are supported on mesoporous silica materials (MSM), particularly MCM-41 and SBA-15.…”
Section: Introductionmentioning
confidence: 99%
“…Ethylene, as the cornerstone of numerous important manufacturing businesses, is mainly produced through steam cracking and dehydrogenation of ethane in the petrochemical industry and inevitably contains trace amounts of C 2 H 6 impurities, which may cause safety and health concerns in the finished polymer. Therefore, further purification is required to obtain high-purity C 2 H 4 products. However, similar physical and chemical properties such as the kinetic diameter (4.443 Å for C 2 H 6 and 4.163 Å for C 2 H 4 ), boiling point (184.55 K for C 2 H 6 and 169.42 K for C 2 H 4 ), and condensability make the separation process of the C 2 H 4 /C 2 H 6 mixture one of the most challenging processes. At present, cryogenic distillation is the main technology for industrial separation of C 2 H 6 /C 2 H 4 mixtures, but this high-energy thermal drive is an extremely costly and energy-intensive process.…”
Section: Introductionmentioning
confidence: 99%