2019
DOI: 10.1016/j.apcatb.2018.11.023
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Modulation of b-axis thickness within MFI zeolite: Correlation with variation of product diffusion and coke distribution in the methanol-to-hydrocarbons conversion

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Cited by 86 publications
(60 citation statements)
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“…The in situ XRD demonstrated that the crystallization process was a solid-state transformation through aS iF 6 2À intermediate. [18] Therefore, coke formation was retarded, and the catalytic lifetime of the catalyst was prolonged. Based on these results, ar eaction pathway was proposed, as illustrated in Scheme 1: the bulk zeolite crystals were first dissociated into smalls egments by NH 4 Fe tching.T hen, with the help of a template and NH 4 F, the segments recrystallizedo nt he silica substrate and formed sheet-like crystals.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…The in situ XRD demonstrated that the crystallization process was a solid-state transformation through aS iF 6 2À intermediate. [18] Therefore, coke formation was retarded, and the catalytic lifetime of the catalyst was prolonged. Based on these results, ar eaction pathway was proposed, as illustrated in Scheme 1: the bulk zeolite crystals were first dissociated into smalls egments by NH 4 Fe tching.T hen, with the help of a template and NH 4 F, the segments recrystallizedo nt he silica substrate and formed sheet-like crystals.…”
Section: Resultsmentioning
confidence: 99%
“…Significantly,D S-HZSM-5 had am uch longerl ifetime;f or methanol conversionh igher than 90 %, the lifetimeo f DS-HZSM-5 was 610 hw hereas that of Conv-HZSM-5 was only 220 h. Specifically,o ur DS-HZSM-5 zeolite with sheet-like crystals had as hort b-axis length,w hich significantly improved the mass transfer by reducing the diffusionp ath. [18] Therefore, coke formation was retarded, and the catalytic lifetime of the catalyst was prolonged. Furthermore, the unique hollow-spherelike stacked morphology of DS-HZSM-5 endowed an abundant intercrystallite porosity,w hich increased the coke capacity and heat transfer and thus improved the stability of the catalyst.…”
Section: Resultsmentioning
confidence: 99%
“…are small enough to diffuse randomly through the network of two intersecting channel systems without configuration limitations [15][16][17] . However, as the size of guest molecules further increasing, such as long chain hydrocarbons (C3, C4) or aromatic molecules, an anisotropic diffusion would occur, where the escape rates of the adsorbate in the intersecting pores of ZSM-5 zeolites are diverse in different channels segments (scheme 1b) 9,15,18,19 . Therefore, differentiating diffusivities in straight and sinusoidal channels for these anisotropic molecules over H-ZSM-5 zeolites are benefit to the understanding of activity, stability or product distribution in catalysis and the guidance of catalyst design with designated morphology.…”
Section: Schame 1 Amentioning
confidence: 99%
“…2 unexpectedly point out an obviously opposite result that enlarging the size along c-axis in H-ZSM-5 catalyst can result in a higher OCC catalytic activity and a better stability. It is well known that many factors in H-ZSM-5 crystal can influence the catalysis properties, such as acidities 26,29 , textural structures 27 and morphology [9][10][11][12] . On one hand, the influence of the textural structures and acid sites in our disquisitive catalysts can be excluded due to the similarity in these zeolites, as presented in Fig.…”
Section: Catalytic Behaviors Over H-zsm-5 Catalysts With Various Morpmentioning
confidence: 99%
“…Previous studies on zeolite ZSM-5 in the MTH reaction have concentrated on either designing materials/reactors for kinetic studies [11,16,20,22,[24][25] or gaining spatial insights by using advanced characterization techniques. [17,18,[26][27][28][29][30][31] However, none of these studies have been capable of disentangling the structure-reactivity relationships for specific zeolite-channel orientations under operando conditions.…”
mentioning
confidence: 99%