2011
DOI: 10.1016/s1003-9953(10)60183-1
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Study on the deactivation and regeneration of the ZSM-5 catalyst used in methanol to olefins

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Cited by 48 publications
(17 citation statements)
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“…ZSM-5 is known as an efficient catalyst for the MTP process because of its well-defined, three-dimensional 10ring microporous channel structure. However, the relatively narrow channel structure restricts the diffusion of products and the carbon precursor, thus leading to lower propylene selectivity and faster carbon deposition [5][6][7][8][9] . Zeolites could be used more efficiently if the diffusion path length of the micropore could be reduced by synthesis of nanocrystals or by mesopore formation in larger zeolite crystals, improving transport of molecules to and from the active sites [4,8,10] .…”
Section: Introductionmentioning
confidence: 99%
“…ZSM-5 is known as an efficient catalyst for the MTP process because of its well-defined, three-dimensional 10ring microporous channel structure. However, the relatively narrow channel structure restricts the diffusion of products and the carbon precursor, thus leading to lower propylene selectivity and faster carbon deposition [5][6][7][8][9] . Zeolites could be used more efficiently if the diffusion path length of the micropore could be reduced by synthesis of nanocrystals or by mesopore formation in larger zeolite crystals, improving transport of molecules to and from the active sites [4,8,10] .…”
Section: Introductionmentioning
confidence: 99%
“…Each of the applied templates affected the formation of special type of morphology which can afford additional evidence for the implementation of mixed template in the synthesis procedure. Surface of the catalytic particles of the CoS/TEA-DE and CoS/TEA-MO samples 10 are smoother than the surface of CoS/TEA-TE particles which can be attributed to their crystallinity. In other words, it seems that the samples with higher crystallinity appeared with much more smoother particles in FESEM micrographs.…”
Section: Fesem Analysismentioning
confidence: 96%
“…Among the leading candidate catalysts, silicoaluminophosphate SAPO-34 molecular sieve exhibits higher selectivity toward light olefin [18][19][20][21]. However, it suffers from rapid deactivation by the blockage of pore mouth arisen from the coke formation [10]. Hence, the MTO process will need frequent regeneration of the catalyst.…”
Section: Introductionmentioning
confidence: 99%
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“…There is general agreement that coke formation on acid sites (especially strong acid sites) of the MTP catalyst is the main reason for catalyst deactivation. 8,64 The micropore channels of the HZSM-5 catalyst cause the reaction-produced molecules whose sizes are larger than those of trapped ZSM-5 channels and thereby form a coke precursor. Thus, coke is deposited on the pores and blocks the active acid sites and finally accelerates the catalyst deactivation.…”
Section: Catalyst Stabilitymentioning
confidence: 99%