2013
DOI: 10.1007/s11244-013-0170-7
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Methanol Conversion to Hydrocarbons (MTH) Over H-ITQ-13 (ITH) Zeolite

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Cited by 22 publications
(17 citation statements)
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“…31,159,163,247,447,[512][513][514][515][516][517][518][519][520][521][522][523][524][525][526][527][528][529][530][531] Framework trivalent heteroatoms (Al, Fe, Ga, In, and B) are responsible for Brønsted activity (see Section 2) of different strengths. Other examples of isomorphic substitution of framework silicon atoms are iron, titanium, gallium, germanium, boron, vanadium and tin.…”
Section: Heteroatoms Substituted In Framework T Positionsmentioning
confidence: 99%
“…31,159,163,247,447,[512][513][514][515][516][517][518][519][520][521][522][523][524][525][526][527][528][529][530][531] Framework trivalent heteroatoms (Al, Fe, Ga, In, and B) are responsible for Brønsted activity (see Section 2) of different strengths. Other examples of isomorphic substitution of framework silicon atoms are iron, titanium, gallium, germanium, boron, vanadium and tin.…”
Section: Heteroatoms Substituted In Framework T Positionsmentioning
confidence: 99%
“…In full accordance with this observation, switching 12 The dual cycle concept has been considered the state of the art in the mechanistic understanding of the MTH reaction since 2007. Originally, it was proposed over H-ZSM-5, but the mechanism has been successfully used to explain the operation and product distribution of many other zeolitic structures in the MTH reaction [138][139][140][141][142][143][144][145][146][147][148][149]. Many studies have attempted to correlate the characteristics of the catalyst (especially topology and acidity) with the relative propagation of the two catalytic cycles, which is fundamental to understand the effluent product selectivities.…”
Section: Autocatalytic Stage Of the Mth Reactionmentioning
confidence: 99%
“…Recently, besides the CHA framework, other small-pore zeolites, such as LEV, DDR, AEI, RHO, KFI, ITH and AFX, have also been identified as interesting candidates for the MTO process. 6 14 Small differences in the framework topology of these small-pore zeolites can have a large effect on both product selectivity and the intermediate species involved in the MTO process. 6 , 15 , 16 For instance, DDR catalysts exhibit a high selectivity toward ethylene and propylene over C 2 and C 3 paraffins due to their pore structure.…”
Section: Introductionmentioning
confidence: 99%