2012
DOI: 10.1007/s11244-012-9864-5
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Sorbitol Hydrogenolysis Over Ni, Pt and Ru Supported on NaY

Abstract: The hydrogenolysis of sorbitol into 1,2-propanediol (PD), ethylene glycol (EG) and glycerol (G) was investigated over Ni, Pt and Ru supported on NaY at 220°C and 60 bar in a batch reactor. Ni(6 %)-NaY was investigated in detail at different process conditions, including its recyclability. Attempts have been made to rationalize the experimentally observed conversion and product selectivity obtained over the different catalysts with results of Density Functional Theory calculations of adsorption energy and bond … Show more

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Cited by 43 publications
(29 citation statements)
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References 28 publications
(34 reference statements)
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“…Sorbitol is widely used as a sweetener, a moisture controller in cosmetics, and in medical applications. [36,37] A historical retrospect of the progress of hydrolytic hydrogenation of cellulose into sorbitol reveals that most of the catalytic systems used share two main components (Scheme 1): 1) a transition-metal catalyst (often Pt or Ru) and 2) a dilute acid or a solid support with sufficient acidity (e.g., oxidized carbon, silica-alumina, or acidic zeolites). [36,37] A historical retrospect of the progress of hydrolytic hydrogenation of cellulose into sorbitol reveals that most of the catalytic systems used share two main components (Scheme 1): 1) a transition-metal catalyst (often Pt or Ru) and 2) a dilute acid or a solid support with sufficient acidity (e.g., oxidized carbon, silica-alumina, or acidic zeolites).…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…Sorbitol is widely used as a sweetener, a moisture controller in cosmetics, and in medical applications. [36,37] A historical retrospect of the progress of hydrolytic hydrogenation of cellulose into sorbitol reveals that most of the catalytic systems used share two main components (Scheme 1): 1) a transition-metal catalyst (often Pt or Ru) and 2) a dilute acid or a solid support with sufficient acidity (e.g., oxidized carbon, silica-alumina, or acidic zeolites). [36,37] A historical retrospect of the progress of hydrolytic hydrogenation of cellulose into sorbitol reveals that most of the catalytic systems used share two main components (Scheme 1): 1) a transition-metal catalyst (often Pt or Ru) and 2) a dilute acid or a solid support with sufficient acidity (e.g., oxidized carbon, silica-alumina, or acidic zeolites).…”
Section: Introductionmentioning
confidence: 99%
“…It also has been studied as a resource for the production of hydrogen, [33] alkanes, [34,35] and value-added chemicals. [36,37] A historical retrospect of the progress of hydrolytic hydrogenation of cellulose into sorbitol reveals that most of the catalytic systems used share two main components (Scheme 1): 1) a transition-metal catalyst (often Pt or Ru) and 2) a dilute acid or a solid support with sufficient acidity (e.g., oxidized carbon, silica-alumina, or acidic zeolites). [21][22][23][24][25][26][27][28] A good balance between the two catalytic functions is a necessity.…”
Section: Introductionmentioning
confidence: 99%
“…Banu et al. investigated the conversion of sorbitol over Ru‐, Pt‐ and Ni‐NaY catalysts in the presence of base . Ni‐NaY showed the best results with over 60 % conversion and 70 % selectivity to glycols.…”
Section: Introductionmentioning
confidence: 99%
“…In previous work, oxidation of glucose to gluconic acid has been investigated using supported Pt, Pd, and Au catalysts [8,[11][12][13] or their combinations, such as PtPd, PdAu, PtPdBi, PtAu, PtBi, and PdTe [14][15][16][17][18][19][20][21][22][23][24][25]. Although reasonable oxidation activity (TOF = 48-1423 h À1 based on surface metal composition, 45-70°C) was achieved, reported glucose to glucaric acid yields are very low (Y $ 3%).…”
Section: Introductionmentioning
confidence: 99%