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丝光沸石催化二甲醚羰基化研究进展

赵生迎 耿海伦 徐冰 武雪梅 谭明慧 杨国辉 谭猗生

赵生迎, 耿海伦, 徐冰, 武雪梅, 谭明慧, 杨国辉, 谭猗生. 丝光沸石催化二甲醚羰基化研究进展[J]. 燃料化学学报. doi: 10.19906/j.cnki.JFCT.2021083
引用本文: 赵生迎, 耿海伦, 徐冰, 武雪梅, 谭明慧, 杨国辉, 谭猗生. 丝光沸石催化二甲醚羰基化研究进展[J]. 燃料化学学报. doi: 10.19906/j.cnki.JFCT.2021083
ZHAO Sheng-ying, GENG Hai-lun, XU Bing, WU Xue-mei, TAN Ming-hui, YANG Guo-hui, TAN Yi-sheng. Research progress on mordenite catalyzed carbonylation of dimethyl ether[J]. Journal of Fuel Chemistry and Technology. doi: 10.19906/j.cnki.JFCT.2021083
Citation: ZHAO Sheng-ying, GENG Hai-lun, XU Bing, WU Xue-mei, TAN Ming-hui, YANG Guo-hui, TAN Yi-sheng. Research progress on mordenite catalyzed carbonylation of dimethyl ether[J]. Journal of Fuel Chemistry and Technology. doi: 10.19906/j.cnki.JFCT.2021083

丝光沸石催化二甲醚羰基化研究进展

doi: 10.19906/j.cnki.JFCT.2021083
基金项目: 国家自然科学基金(21978312,21908235),中国科学院前沿科学重点研究项目(Grant No. QYZDB-SSW-JSC043),中国科学院国际伙伴计划(Grant No. 122214KYSB20170007),山西省留学回国人员科技活动择优资助项目和山西省省筹资金资助回国留学人员科研项目等基金资助
详细信息
    作者简介:

    赵生迎:zhaoshengying19@mails.ucas.ac.cn

    通讯作者:

    杨国辉 电话:0351-4044287 电子邮箱:yanggh@sxicc.ac.cn

  • 中图分类号: O643.36

Research progress on mordenite catalyzed carbonylation of dimethyl ether

Funds: The project was supported by the National Natural Science Foundation of China (21978312, 21908235), the Key Research Program of Frontier Sciences, CAS (Grant No. QYZDB-SSW-JSC043), as well as International Partnership Program of Chinese Academy of Sciences. (Grant No. 122214KYSB20170007), Research Project Supported by Shanxi Scholarship Council of China and Fund Program for the Scientific Activities of Selected Returned Overseas Professionals in Shanxi Province are also greatly appreciated
  • 摘要: 二甲醚羰基化反应是在二甲醚分子中定向插入一氧化碳的重要增碳反应,在工业生产中具有重要意义。近年来,研究发现廉价的丝光沸石可催化二甲醚羰基化反应,且具有较高的反应活性和十分优异的羰基化产物选择性,因此得到了广泛的研究。本文对丝光沸石催化二甲醚羰基化的研究进行综述,介绍了羰基化反应的机理,并总结丝光沸石内部酸性位点调控的各种方法以及对羰基化反应的影响。
  • 图  1  MOR在[001]方向的骨架结构(a)和孔道体系示意图(b)[13, 22]

    Figure  1  The framework structure viewed along the [001] direction (a) and schematic diagram of the channel system (b) of MOR zeolite[13, 22]

    图  2  沸石催化甲醇羰基化的反应路径[23]

    Figure  2  Reaction path of methanol carbonylation catalyzed by zeolite[23]

    图  3  DME在酸性沸石上发生羰基化反应机理[24]

    Figure  3  Proposed elementary steps for carbonylation of dimethyl ether on acidic zeolites[24]

    图  4  (a)在H-MOR催化剂上DME(■:0.5 MPa CO, 438 K;▲0.5 kPa H2O, 0.5 MPa CO, 438 K)和CO(◆:2–16 kPa DME, 438 K)的分压对MA生成速率的影响;(b)水对DME羰基化反应的影响[4, 26]

    Figure  4  (a) Effects of DME (squares: 0.5 MPa CO, 438 K; triangles: 0.5 kPa H2O, 0.5 MPa CO, 438 K) and CO (diamonds: 2–16 kPa DME, 438 K) concentration on the rate of methyl acetate formation on H-MOR (Si/Al=10:1); (b) The influence of water on the DME carbonylation catalytic performance[4, 26]

    图  5  在分子筛不同孔道中Brønsted酸性位点数量与MA生成速率的关系图。MOR(▲ 8-MR,● 12-MR),FER(◆ 8-MR),内嵌图为总酸量(■)[7]

    Figure  5  DME carbonylation rates per unit mass plotted against the number of H+ sites per unit mass in 8-MR channels of MOR (▲) and FER (◆) and 12-MR channels of MOR (●). Inset shows DME carbonylation rates plotted against the total number of H+ sites in these samples (■). Reprinted with permission.[7] Copyright 2007 American Chemical Society

    图  6  MOR的T3-O33位置(a)和8-MR道中其他位置(b)的Oframework-CH3键和孔道轴的相对取向示意图;H-MOR在c轴(c)和b轴(d)方向的骨架结构[34]

    Figure  6  (a, b) Schematic representation of the relative orientation of the Oframework-CH3 bond and the channel axis at the T3-O33 position of MOR and any other position in an 8-MR channel; (c, d) Structure of MOR in the (top) c and (bottom) b directions. Reprinted (adapted) with permission.[34] Copyright 2008 American Chemical Society

    图  7  MOR催化DME羰基化反应中主要结焦途径[38]

    Figure  7  Main coking pathway in the carbonylation of the DME reaction over MOR. Reprinted with permission.[38] Copyright 2021 American Chemical Society

    图  8  原位13C MAS NMR测量13CH3OH在13CO/13CH3OH反应中转化为乙酰基[50]

    Figure  8  Conversion of 13CH3OH to acetyls in the 13CO/13CH3OH reaction at 200 ℃ over H-Mordenite (H-MOR) and Cu-Mordenite (CuH-MOR), as measured by in situ 13C MAS NMR spectroscopy[50]

    图  9  不同催化剂反应前后的TEM图[52]

    Figure  9  TEM images of the fresh calcined and spent catalysts. Reprinted with permission.[52] Copyright 2016 American Chemical Society

    图  10  (a)Co2+在MOR中的催化反应过程;(b)MOR中Co2+可能发生交换的位点[58, 59]

    Figure  10  (a) Catalytic reaction process of Co2+ in MOR; (b) Possible positions that could be exchanged by metal cations in HMOR[58, 59]

    图  11  DME羰基化在不同催化剂上的转化率和MA的选择性[27]

    Figure  11  Conversion of DME and selectivities for MA during DME carbonylation over the HMOR-6 and Py-HMOR-6 catalysts. Reaction conditions: 473 K, 5% DME-50% CO-2.5% N2-42.5% He, 1250 ml/(g·h), 1.0 MPa[27]

    图  12  (a)MPD和MPD焙烧去除后的O位点变化;(b)不同环胺作有机模板剂合成的MOR时,8-MR孔道中的Brønsted酸浓度与MA收率的关系图[76]

    Figure  12  (a) Diagrams of M-MPD and OSDA removed M-MPD; (b) Correlation between the STYMA and the number of Brønsted acid sites in 8-MR[76]

    图  13  传统HMOR(a,b)和纳米MOR-N(c,d)催化剂的FE-SEM(a,b,c)和TEM(d)图像[83]

    Figure  13  FE-SEM (a, b, c) and TEM (d) images of the HMOR-C (a, b) and HMOR-N (c, d) catalysts[83]

    图  14  利用NH4F在不同温度下刻蚀MOR的TEM图[93]

    Figure  14  TEM image of etching MOR with NH4F at different temperatures. Reprinted with permission.[93] Copyright 2020 American Chemical Society

    图  15  加入不同浓度CTAB合成MOR的SEM和HRTEM图。(A) HMOR, (B) HMOR-C-0.5, (C) HMOR-C-1, (D) HMOR-C-3, and (E) HMOR-C-5[95]

    Figure  15  SEM and HRTEM images of samples: (A) HMOR, (B) HMOR-C-0.5, (C) HMOR-C-1, (D) HMOR-C-3, and (E) HMOR-C-5. The insets show the Fourier transform of the HRTEM images. Reprinted with permission.[95] Copyright 2020 American Chemical Society

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  • 收稿日期:  2021-07-28
  • 修回日期:  2021-09-04
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