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Treating hydrated Na75-Y with Na2S(aq) results in the formation of a cationic sodium sulfide cluster within the zeolite

Treating hydrated Na75-Y with Na2S(aq) results in the formation of a cationic sodium sulfide cluster within the zeolite

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The extraframework sodium sulfide cationic cluster, Na4S2+, has been introduced into zeolite Y (FAU, Si/Al = 1.56). A single crystal of |Na73(Na4S2+)1.0|[Si117Al75O384]-FAU was prepared by allowing aqueous 0.1 M Na2S solution to flow past a |Na75|[Si117Al75O384]-FAU crystal, and followed by vacuum dehydration at 723 K. Its structure was determined...

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... The average number of diamines per supercage was calculated by dividing the moles of amine in the zeolite by the moles of supercages in FAU zeolite (details in Supporting Information Section S4). [38][39][40] Before pre-treatment, approximately 0.5, 1.2, 2.1, and 1.8 molecules of 44TMDP were loaded per supercage for the nominal loadings of 5, 10, 25, 40 wt% from wet impregnation (Figure 3c). The difference in number of 44TMDP per supercage for nominal loadings of 25 and 40 wt% is within experimental error. ...
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Dehydration of methyl lactate to acrylic acid and methyl acrylate was experimentally evaluated over Na-FAU zeolite catalyst impregnated with multifunctional diamines. 1,2-bis(4-pyridyl)ethane (12BPE) and 4,4-trimethylenedipyridine (44TMDP), at a nominal loading of 40 wt% or two molecules per Na-FAU supercage, afforded a dehydration selectivity of 96+3% over 2000 min time on stream, exceeding the selectivity target of 90% for commercial viability. During continuous reaction at 300 °C, the amine loadings in Na-FAU remained constant for 12BPE but decreased as much as 83% for 44TMDP. Although 12BPE and 44TMDP have van der Waals diameters approximately 90% of the Na-FAU window opening diameter, both flexible diamines interact with internal active sites of Na-FAU as characterized by infrared spectroscopy. Tuning the weighted hourly space velocity (WHSV) from 0.9 to 0.2 h-1 afforded a yield as high as 92% at a selectivity of 96% with 44TMDP impregnated Na-FAU, resulting in the highest yield reported to date.
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Co-feeding an inert and site-selective chemical titrant provides desirable selectivity tuning when titrant adsorption is favored over side reaction pathways on a solid acid catalyst. Here, a selectivity enhancement from 61 to 84 C % was demonstrated for methyl lactate dehydration to methyl acrylate and acrylic acid over a NaY zeolite catalyst using amines as the co-fed titrants to suppress side reactions on in situ-generated Brønsted acid sites (BASs). The effectiveness of BAS titration was evaluated by considering both the basicity and steric properties of the titrant molecule with the goal to maximize the selectivity enhancement. The presence of electron-donating alkyl functional groups not only enhances amine basicity but also introduces additional steric constraints to the molecule with respect to the pore dimensions of the NaY zeolite. While higher basicity of titrant amines favors stronger adsorption on BASs, steric limitations hinder site binding through contributions from internal diffusion limitations and local steric repulsion between the titrant and the zeolite wall around the BAS. Titrant bases with proton affinities above ∼1040 kJ/mol and sizes below 85% of the NaY supercage window or pore diameter are predicted to afford dehydration selectivities above 90 C % to acrylate products.