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使用铜沸石将甲烷催化转化为甲醇。

Catalytic conversion of methane to methanol using Cu-zeolites.

作者信息

Alayon Evalyn Mae C, Nachtegaal Maarten, Ranocchiari Marco, van Bokhoven Jeroen A

机构信息

ETH Zurich, Institute for Chemical and Bioengineering, Zurich, Switzerland.

出版信息

Chimia (Aarau). 2012;66(9):668-74. doi: 10.2533/chimia.2012.668.

Abstract

The conversion of methane to value-added liquid chemicals is a promising answer to the imminent demand for fuels and chemical synthesis materials in the advent of a dwindling petroleum supply. Current technology requires high energy input for the synthesis gas production, and is characterized by low overall selectivity, which calls for alternative reaction routes. The limitation to achieve high selectivity is the high C-H bond strength of methane. High-temperature reaction systems favor gas-phase radical reactions and total oxidation. This suggests that the catalysts for methane activation should be active at low temperatures. The enzymatic-inspired metal-exchanged zeolite systems apparently fulfill this need, however, methanol yield is low and a catalytic process cannot yet be established. Homogeneous and heterogeneous catalytic systems have been described which stabilize the intermediate formed after the first C-H activation. The understanding of the reaction mechanism and the determination of the active metal sites are important for formulating strategies for the upgrade of methane conversion catalytic technologies.

摘要

在石油供应日益减少的情况下,将甲烷转化为高附加值的液体化学品是满足对燃料和化学合成材料迫切需求的一个有前景的解决方案。当前技术在合成气生产方面需要高能量输入,且总体选择性较低,这就需要 alternative reaction routes。实现高选择性的限制因素是甲烷中碳氢键的高强度。高温反应体系有利于气相自由基反应和完全氧化。这表明用于甲烷活化的催化剂应在低温下具有活性。受酶启发的金属交换沸石体系显然满足了这一需求,然而,甲醇产率较低,尚未建立起催化工艺。已经描述了均相和非均相催化体系,它们能稳定首次碳氢键活化后形成的中间体。理解反应机理和确定活性金属位点对于制定甲烷转化催化技术升级策略很重要。

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