2023
DOI: 10.1021/acs.energyfuels.3c00356
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Better Performance in C2-Conversion to Aromatics by Optimized Feed and Catalysts

Abstract: We identify favorable parameters for the formation of aromatics from ethanol-based feeds over ZSM-5. An ethanol partial pressure of 0.3 bar, a reaction temperature of ∼700 K, a low weight hourly space velocity (WHSV), and a high Brønsted acid site density increase the content of aromatics, in the latter case, on the expense of lifetime. The aromatic fraction composition changes with the WHSV and n Si/n Al ratio. Water cofeed increases the content of aromatics in the C2:H2O stoichiometry of 1:0.5 (equals diethy… Show more

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Cited by 4 publications
(33 citation statements)
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“…With increasing BAS density we observe also a decreased lifetime of our catalysts. This is caused by the increased amount of aromatics formed that lead to deactivation and was already described for microporous ZSM‐5 catalysts [9,11e] . In desilicated samples, however, this effect is overshadowed by a longer lifetime as result of better transport properties [11f] .…”
Section: Resultsmentioning
confidence: 79%
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“…With increasing BAS density we observe also a decreased lifetime of our catalysts. This is caused by the increased amount of aromatics formed that lead to deactivation and was already described for microporous ZSM‐5 catalysts [9,11e] . In desilicated samples, however, this effect is overshadowed by a longer lifetime as result of better transport properties [11f] .…”
Section: Resultsmentioning
confidence: 79%
“…[8] The immediate dehydration of ethanol feed to ethylene makes also adjustments of the feed more promising, because unneeded water can be efficiently removed initially which enables longer lifetimes and higher aromatic yields. [9] Due to the mentioned chemical and mechanistic differences between ethanol and methanol feeds it is highly interesting if post-modifications that are frequently applied for ZSM-5 catalysts in methanol conversion have also beneficial effects on the ETA catalysts. Typical post-modifications applied to zeolites are the phosphatation, [10] dealumination, [11] both applied to alter the acidity of zeolites, and finally desilication, [10e,12] whereby both diffusion and acid properties of zeolite catalyst can be varied.…”
Section: Introductionmentioning
confidence: 99%
“…However, an application of solvent (CH 2 Cl 2 ) enables a soft, reproducible TPP distribution also on samples with low acid site density . TPP was used for the investigation of BAS on the external surface of amorphous silica-alumina, , H-MCM-22, , and hierarchical zeolites. , TPP is, with a diameter of 1.00 to 1.08 nm, rather voluminous and thus unable to access most intact zeolite micropores. Comparing the BAS density from TPP loading with the total BAS density of a sample (determined by loading with a smaller probe molecule) enables the quantification of the share of external sites and the quantification of BAS that were introduced by desilication (see Figure ).…”
Section: Families Of Solid-state Nmr Probe Moleculesmentioning
confidence: 99%
“…Comparing the BAS density from TPP loading with the total BAS density of a sample (determined by loading with a smaller probe molecule) enables the quantification of the share of external sites and the quantification of BAS that were introduced by desilication (see Figure ). ,, Also a larger homologue of TPP, tri-( p -methoxyphenyl)­phosphine (TMPP), is unable to access micropores and suited to quantify external BAS on zeolites . Noteworthy, the long T 1 times of free TPP (7.7 ± 0.4 s) and other pure phenylphosphines make far longer delay times in between scans necessary, if all peaks in the spectrum, not only those of TPP on BAS, shall be quantified. , …”
Section: Families Of Solid-state Nmr Probe Moleculesmentioning
confidence: 99%
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