Abstract:We
report synthetic protocols to independently influence composition
and crystallite sizes of MFI zeolites, properties that contribute
to Thiele moduli, and the proximity of Al heteroatoms at fixed composition
(Si/Al ∼ 50). Crystallite sizes decrease with the addition
of non-catalytic B heteroatoms in B–Al–MFI zeolites.
Using only tetra-n-propylammonium (TPA+) as a structure-directing agent (SDA) leads to occlusion of one
TPA+ per channel intersection and a finite percentage of
framework Al atoms (20–40%) in p… Show more
“…In methanol to propene process, this Al-B-ZSM-5 sample showed higher propene selectivity, lower aromatics, and alkanes selectivity and longer catalyst lifetime than the materials prepared without the assistance of boron [304]. In the case of MFI synthesis systems where TPA and Si/Al ratio were kept constant (≈ 50) and B content varied, 20-40% of Al sites were paired, independently on the boron quantity added [305]. On the other hand, in analogous experiments where a mixture of tetrapropylammonium cations and ethylenediamine (EDA) is used as OSDA, the obtained B-Al-MFI zeolites contain less than 5% of Al in paired configurations, irrespectively of the Si/B ratio.…”
Section: Boron-containing Zeolitesmentioning
confidence: 90%
“…First-order rate constants of methanol dehydration to dimethylether over B-Al-MFI indicate acid sites are confined within smaller voids. Given this, the Al distribution within the zeolite framework is directed by the widespread impact of the organic molecules over the boron atoms present within the synthesis mixture [305]. The boron-containing zeolite Beta materials were prepared in the presence of seeds (Si/B = 4-38; Si/Al = 170-90).…”
The exceptional catalytic performance of zeolites is due to the presence of active sites in a shape-selective environment, i.e., in micropores with molecular dimensions. The present review provides a comprehensive analysis of active sites in zeolite frameworks. It is focused on the active sites generated by the Al incorporation in the framework. The inclusion of other heteroatoms in the zeolite framework is also addressed. After the introduction of zeolite-type materials and a discussion of the structure-properties relationship in zeolites the central part of the review is devoted to i) the analytical methods and their complementarity for the evaluation of the number, strength, and position of active sites and ii) the in situ and post-synthesis methods of acid sites assessment and control. The data presented herein provide guidelines for making zeolite materials by design in terms of acidity.
“…In methanol to propene process, this Al-B-ZSM-5 sample showed higher propene selectivity, lower aromatics, and alkanes selectivity and longer catalyst lifetime than the materials prepared without the assistance of boron [304]. In the case of MFI synthesis systems where TPA and Si/Al ratio were kept constant (≈ 50) and B content varied, 20-40% of Al sites were paired, independently on the boron quantity added [305]. On the other hand, in analogous experiments where a mixture of tetrapropylammonium cations and ethylenediamine (EDA) is used as OSDA, the obtained B-Al-MFI zeolites contain less than 5% of Al in paired configurations, irrespectively of the Si/B ratio.…”
Section: Boron-containing Zeolitesmentioning
confidence: 90%
“…First-order rate constants of methanol dehydration to dimethylether over B-Al-MFI indicate acid sites are confined within smaller voids. Given this, the Al distribution within the zeolite framework is directed by the widespread impact of the organic molecules over the boron atoms present within the synthesis mixture [305]. The boron-containing zeolite Beta materials were prepared in the presence of seeds (Si/B = 4-38; Si/Al = 170-90).…”
The exceptional catalytic performance of zeolites is due to the presence of active sites in a shape-selective environment, i.e., in micropores with molecular dimensions. The present review provides a comprehensive analysis of active sites in zeolite frameworks. It is focused on the active sites generated by the Al incorporation in the framework. The inclusion of other heteroatoms in the zeolite framework is also addressed. After the introduction of zeolite-type materials and a discussion of the structure-properties relationship in zeolites the central part of the review is devoted to i) the analytical methods and their complementarity for the evaluation of the number, strength, and position of active sites and ii) the in situ and post-synthesis methods of acid sites assessment and control. The data presented herein provide guidelines for making zeolite materials by design in terms of acidity.
“…Most recent studies on short-range Al distributions have deduced 'thermodynamic' synthesis outcomes based on localized charge balances at the cage level between a positively charged (organic) structure-directing agent (O)SDA and the negatively charged framework from either aluminum or defect sites. [8][9][10][11][12][13][14][15] Furthermore, Al separation rules such as Löwenstein rule 16 or Dempsey's rule 17 and the intrinsic thermodynamic preference of Al for particular T-sites (framework dependent) 18 also seem to influence the short-range Al distribution in synthesized zeolites, despite the strong influence of kinetic processes during zeolite crystallization. 19,20 The use of alternative Si and Al sources −and other recipe alterations− may provoke Al distribution outcomes unexpected from a charge-balancing perspective.…”
The performance of zeolite catalysts depends not only on the strength and number of Brønsted acid (or exchange) sites but also on synergistic effects derived from their proximity, in particular, and their distribution, in general. Little is known on the genesis of acid sites and site distributions in hydrothermal zeolite synthesis. By an extensive study of five crystallization systems yielding ZSM-5 (MFI) and SSZ-13 (CHA), with a focus on interzeolite conversion (IZC) methods, several synthesis factors and mechanisms that are key in determining the output acid site distribution have been identified. Key in this study were temporal synthesis profiles while probing the distribution and evolution of proximal acid sites with divalent cation capacity measurements. Over the course of different crystallizations, changing local charge distributions are detected, notably within crystalline materials upon prolonged exposure (maturation). Aluminum is clearly the key driver in IZC syntheses, from charge, dissolution, concentration, and mobility points of view. Quasigeneric principles for IZC syntheses are proposed, distinguishing between Al-loving and Al-averse systems, enabling a new degree of control over the acidity and ion-exchange properties of zeolites, of use to tailoring catalytic activity.
“…Over the past few years, ZSM-5-based catalysts have been paid considerable attention in the petrochemical industry due to their excellent selectivity properties. , However, conventional ZSM-5 zeolite still suffers from the problem of diffusion limitation because of its sole and narrow pore structure. The diffusion limitation can be partially solved by reducing the path length through zeolite crystals .…”
HZSM-5 crystals with short straight
channels possess the advantages
of easier diffusion and less coke formation in petrochemical processes.
In this work, aggregated ZSM-5 zeolite assembled by regularly stacked
nanosheet-like crystals with a b-axis thickness of
60 nm was synthesized using specially designed silicate-1 as seed.
Silicate-1 (S-2) was synthesized using relatively lower cost silica
sol as a silica source, tetrapropylammonium bromide (TPABr) as a structure-directing
agent (SDA), and ethylamine as an assistant compared with traditional
silicate-1 (S-1: tetraethyl orthosilicate (TEOS) as a silica source
and tetrapropylammonium hydroxide (TPAOH) as an SDA). When S-2 seeds
were added into the synthesis system, the seeds could limit the crystal
growth along the b-axis direction under the assistance
of ethylamine. Meanwhile, the adjacent ZSM-5 nanosheet crystals would
spontaneously stack together. The catalyst Zn/S-2-1 exhibited relatively
higher n-hexane conversion and selectivity of benzene,
toluene, ethylbenzene, and xylene (BTEX) as well as catalytic stability
in contrast to the catalyst synthesized using S-1 as seed when being
used in the n-hexane aromatization reaction. This
work opened up a new prospective for ZSM-5 aggregates assembled from
the nanosheet catalyst design in the application of hydrocarbon aromatization.
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