首页> 外文期刊>Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications >Oxidative gas phase carbonylation of methanol to dimethyl carbonate over chloride-free Cu-impregnated zeolite Y catalysts at elevated pressure
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Oxidative gas phase carbonylation of methanol to dimethyl carbonate over chloride-free Cu-impregnated zeolite Y catalysts at elevated pressure

机译:在无氯的含铜沸石Y催化剂上,在高压下将甲醇氧化气相羰基化为碳酸二甲酯

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Incipient wetness impregnation of zeolite Y with copper(II) nitrate solution and inert activation at 650 degrees C led to active catalysts for the oxidative carbonylation of methanol to dimethyl carbonate in the gas phase. Activities were measured under elevated pressure (0.4-1.6 MPa) with feed compositions of CO/MeOH/O-2 = 40/20/6-1.5 vol.% (balanced by N-2) over zeolite Y loaded with 10-17 wt.% copper. It could be shown that inert activation at 650 degrees C enhanced the activity, and that Cu loading of 14-17 wt.% gave the best performance. By combined XRD, TEM, TPR and DRIFT characterization it was found that the inert activation initiated dispersion of crystalline CuO, auto-reduction of Cu2+ to Cu+ and redistribution of copper ions with enrichment inside the supercages of the zeolite. The O-2 content of the feed was found to control the selectivity to dimethyl carbonate. Dimethyl carbonate selectivities of 70-75% were achieved within the temperature range of 140-170 degrees C at an O-2 content of 1.5 vol.%. This allowed space-time yields of dimethyl carbonate up to 632 g l(cat)(-1) h(-1) at methanol conversions of 5-12%. Formation of the main side product, dimethoxy methane, was surprisingly affected by CO, which is not in line with suggested reaction pathways. A mechanism is proposed including formation of surface carbonate structures as common intermediate. (c) 2007 Published by Elsevier B.V.
机译:用硝酸铜(II)溶液对沸石Y进行初期湿润浸渍和在650℃下的惰性活化导致在气相中将甲醇氧化羰基化为碳酸二甲酯的活性催化剂。活性是在高压(0.4-1.6 MPa)下以负载了10-17 wt%的沸石Y的CO / MeOH / O-2进料组成为40/20 / 6-1.5 vol。%(由N-2平衡)测量的。% 铜。可以证明,在650℃下的惰性活化增强了活性,并且14-17wt。%的Cu负载给出了最佳性能。通过结合XRD,TEM,TPR和DRIFT表征,发现惰性活化引发了结晶CuO的分散,Cu2 +自动还原成Cu +以及铜离子在沸石超笼内富集的重新分布。发现进料中O-2的含量控制了对碳酸二甲酯的选择性。在140-170℃的温度范围内,当O-2含量为1.5vol。%时,碳酸二甲酯的选择性达到70-75%。在甲醇转化率为5-12%的条件下,碳酸二甲酯的时空产率高达632 g l(cat)(-1)h(-1)。主要副产物二甲氧基甲烷的形成出人意料地受到CO的影响,这与建议的反应途径不符。提出了一种机制,该机制包括形成表面碳酸盐结构作为共同的中间体。 (c)2007年由Elsevier B.V.

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