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The effect of FER zeolite acid sites in methanol-to-dimethyl-ether catalytic dehydration

机译:FER沸石酸位在甲醇制二甲醚催化脱水中的作用

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摘要

In this paper,the effect of acidity of zeolites with FER framework was studied in the methanol dehydration to dimethyl ether reaction,by comparing catalysts with different Si/Al ratios (namely 8,30 and 60).The aim of this work was to investigate how the acid sites concentration,strength,distribution and typology (Brφnsted and Lewis) affect methanol conversion,DME selectivity and coke formation.It was found that the aluminium content affects slightly acid sites strength whilst a relevant effect on acid sites concentration and distribution (Brφnsted /Lewis) was observed as 24% of Lewis sites were found on Alrichest samples,whilst less than 10% of Lewis acid sites were observed on FER at higher Si/Al ratio.All the investigated catalyst samples showed a selectivity toward DME always greater than 0.9 and samples with the lowest Si/Al ratio exhibit the best performances in terms of methanol conversion,approaching the theoretical equilibrium value (around 0.85) at temperatures below 200℃.Turnover-frequency analysis suggests that this result seems to be related not only to the higher amount of acid sites but also that the presence of Lewis acid sites may play a significant role in converting methanol.On the other hand,the presence of Lewis acid sites,combined with a high acidity,promote the formation of by-products (mainly methane) and coke deposition during the reaction.As final evidence,all the investigated catalysts exhibit very high resistance to deactivation by coke deposition,over 60 h continuous test,and a GC-MS analysis of the coke deposited on the catalyst surface reveals tetra-methyl benzene as main component.
机译:本文通过将催化剂与不同Si / Al比的催化剂(即8,30和60)进行比较,研究了沸石与FER框架的酸性与FER框架的影响。这项工作的目的是调查酸性位点如何浓缩,强度,分布和类型(Brφnsted和Lewis)影响甲醇转化,DME选择性和焦炭形成。发现铝含量影响略微酸的位点,同时对酸性位点浓度和分布的相关影响(Brφnsted / Lewis)被观察到在Alrichest样品上发现了24%的Lewis位点,而在较高的Si / Al比的FER上观察到少于10%的路易斯酸部位。所研究的催化剂样品对DME表示选择性总是大于0.9和具有最低Si / Al比的样品在甲醇转化方面表现出最佳性能,在温度低于200℃的温度下接近理论平衡值(约0.85).turn过频分析表明,该结果不仅与较高量的酸性位点有关,而且还存在路易斯酸性位点的存在在转换甲醇中可能在转化甲醇中发挥重要作用。另一方面,Lewis酸部位的存在结合高酸度,促进副产品的形成(主要是甲烷)和焦沉积在反应过程中。最终证据,所有研究的催化剂都表现出非常高的焦炭沉积耐去激活,超过60小时连续测试,和沉积在催化剂表面上的焦炭的GC-MS分析显示了四 - 甲基苯作为主要成分。

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  • 来源
    《天然气化学(英文版)》 |2017年第3期|406-415|共10页
  • 作者单位

    Department of Environmental and Chemical Engineering University of Calabria, Via P.BucciCubo 42a, I-87036 Rende, CS, Italy;

    Department of Environmental and Chemical Engineering University of Calabria, Via P.BucciCubo 42a, I-87036 Rende, CS, Italy;

    Department of Environmental and Chemical Engineering University of Calabria, Via P.BucciCubo 42a, I-87036 Rende, CS, Italy;

    Department of Environmental and Chemical Engineering University of Calabria, Via P.BucciCubo 42a, I-87036 Rende, CS, Italy;

  • 收录信息 中国科学引文数据库(CSCD);中国科技论文与引文数据库(CSTPCD);
  • 原文格式 PDF
  • 正文语种 eng
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  • 入库时间 2022-08-18 18:12:05
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