2014
DOI: 10.1016/j.catcom.2014.08.001
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Selective liquid-phase hydrogenation of maleic anhydride to succinic anhydride on biosynthesized Ru-based catalysts

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Cited by 29 publications
(10 citation statements)
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“…To explore the catalytic performance of 2D MoS 2 , the selective hydrogenation of MAH is used, which is an industrially important catalytic reaction in the field of fine chemical synthesis (Figure a). , The 2D MoS 2 yields a selectivity of 100% for MAH selective hydrogenation to SA with the conversion rates from 38.7 to 100% (Reaction conditions: 90–120 °C, 20 mL of 0.06 M MAH solution, 0.908 g 2D MoS 2 catalysts, 0.1–0.6 MPa H 2 , 4 h). Typically, the 2D MoS 2 yields 100% conversion of MAH and 100% selectivity to SA at 120 °C, while c-MoS 2 as the catalyst does not show any detectable activity (Figure b).…”
Section: Resultsmentioning
confidence: 99%
“…To explore the catalytic performance of 2D MoS 2 , the selective hydrogenation of MAH is used, which is an industrially important catalytic reaction in the field of fine chemical synthesis (Figure a). , The 2D MoS 2 yields a selectivity of 100% for MAH selective hydrogenation to SA with the conversion rates from 38.7 to 100% (Reaction conditions: 90–120 °C, 20 mL of 0.06 M MAH solution, 0.908 g 2D MoS 2 catalysts, 0.1–0.6 MPa H 2 , 4 h). Typically, the 2D MoS 2 yields 100% conversion of MAH and 100% selectivity to SA at 120 °C, while c-MoS 2 as the catalyst does not show any detectable activity (Figure b).…”
Section: Resultsmentioning
confidence: 99%
“…Currently, much research effort has been devoted to develop effective catalysts to achieve the high conversion of MA into SA, including noble and non‐noble metal catalysts. In the case of noble metal catalysts, Pt, 4 Pd, 1 Rh, 5 and Ru 6 have been prepared for highly effective catalyzing the reaction that was generally carried out at 100–240°C and 0.2–5 MPa, producing SA and GBL. However, the limitation of precious metals as catalysts is their expensive cost.…”
Section: Introductionmentioning
confidence: 99%
“…For these reasons, the tailoring of high activity and selectivity catalysts to obtain SA or GBL, as well as an exploration of the relationship between the structure of the catalysts and their hydrogenation performances, are scientifically significant and of practical value [3,4]. The metal catalysts Pd, Ru, Cu, and Ni are widely accepted as being active in the hydrogenation of MA [3,[5][6][7][8]. They are usually supported on metal oxides (for example, Al2O3, SiO2, diatomite, SiO2-Al2O3, and zeolite) [9][10][11][12].…”
Section: Introductionmentioning
confidence: 99%
“…The metal catalysts Pd, Ru, Cu, and Ni are widely accepted as being active in the hydrogenation of MA [3,[5][6][7][8]. They are usually supported on metal oxides (for example, Al 2 O 3 , SiO 2 , diatomite, SiO 2 -Al 2 O 3 , and zeolite) [9][10][11][12].…”
Section: Introductionmentioning
confidence: 99%