2020
DOI: 10.1021/acssuschemeng.9b05634
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Synthesis of Al-Modified SBA-15-Supported Ru Catalysts by Chemical Fluid Deposition for Hydrogenation of Dimethyl Terephthalate in Water

Abstract: Uniformly dispersed 5 wt % ruthenium catalysts supported on Al x SBA-15 (x = Si/Al ratio) were prepared by chemical fluid deposition employing supercritical CO2 as the solvent for hydrogenating dimethyl terephthalate to dimethyl 1,4-cyclohexanedicarboxylate in water. Complete conversion of dimethyl terephthalate was achieved over a Ru5/Al20SBA-15 catalyst having the highest number of Lewis acid sites at 100 °C and 4.14 MPa H2 pressure in 1 h. Here, 100% selectivity with a dimethyl 1,4-cyclohexanedicarboxylate … Show more

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Cited by 18 publications
(23 citation statements)
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“…Following the first impregnation step, the complete removal of THF was ensured using a rotary evaporator. The dried catalyst powders were then transferred to an autoclave and scCO 2 treatment was carried out at a pressure of 2500 psi and a temperature of 40 °C for 2 h. A CO 2 pressure higher than its critical pressure was used to enhance its solubilizing capability toward organometallic precursors Rh­(acac) 3 and Pt­(acac) 3 based on previous knowledge for the synthesis of SBA-15-supported Rh–Pt bimetallic catalysts using CFD . For post-scCO 2 treatment, the autoclave was depressurized slowly, and the collected powders were subjected to chemical reduction using H 2 (20 mL/min) at 400 °C for 4 h. The reduced catalyst powders were marked Rh x Pt y /SBA-15, where x and y represent the theoretical metal loadings of Rh and Pt, respectively.…”
Section: Methodsmentioning
confidence: 99%
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“…Following the first impregnation step, the complete removal of THF was ensured using a rotary evaporator. The dried catalyst powders were then transferred to an autoclave and scCO 2 treatment was carried out at a pressure of 2500 psi and a temperature of 40 °C for 2 h. A CO 2 pressure higher than its critical pressure was used to enhance its solubilizing capability toward organometallic precursors Rh­(acac) 3 and Pt­(acac) 3 based on previous knowledge for the synthesis of SBA-15-supported Rh–Pt bimetallic catalysts using CFD . For post-scCO 2 treatment, the autoclave was depressurized slowly, and the collected powders were subjected to chemical reduction using H 2 (20 mL/min) at 400 °C for 4 h. The reduced catalyst powders were marked Rh x Pt y /SBA-15, where x and y represent the theoretical metal loadings of Rh and Pt, respectively.…”
Section: Methodsmentioning
confidence: 99%
“…It has been previously reported that when using water as a solvent for the hydrogenation of aromatic ring compounds the reaction rates were amplified considerably even though the reactants were insoluble in water. The formation of a H 2 bond at the aqueous catalyst–reactant interface, known as the on-water mechanism, was identified as the major reason for this amplification. Through the on-water mechanism, polarization of the aromatic rings of the reactant takes place thereby increasing the susceptibility of the aromatic rings to be attacked by spillover H atoms and undergo hydrogenation by the active metals of catalysts employed.…”
Section: Introductionmentioning
confidence: 99%
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“…Various synthesis procedures have been employed, which include direct synthesis, postsynthetic wet impregnation, Sonication, post-grafting, Insitu-method, the chemical fluid method, evaporation induced wet impregnation, as well as immobilization [38][39][40][41][42][43][44][45] . Table-1 illustrates the different types of synthesis of functionalized metal-doped SBA-15 and their textural properties.…”
Section: Figure-1 a Typical Synthesis Steps Of Sba-15mentioning
confidence: 99%
“…Biomass-derived furfural such as furfuryl alcohol, methyl levulinate, Maleic anhydride, succinic acid, and many more chemicals intermediate is prepared by renewable resources. These chemicals find extensively used for the synthesis of the valuable compound for flavoring agents, fuel additives, and fine chemicals [36][37][38][39][40][41][42][43][44][45][46][47][48][49][50][51][52][53] . In recent times, However, the author invented continuous production of GVL, and reported the 77% yield of GVL in the 24h stream by using Co-SBA-15 catalyst under atmospheric H 2 pressure [36][37][38] .…”
Section: Biomass Valorizationmentioning
confidence: 99%