Handbook of Heterogeneous Catalysis 2008
DOI: 10.1002/9783527610044.hetcat0165
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Dehydrogenation of Alcohols: Formaldehyde

Abstract: The sections in this article are Introduction Direct Dehydrogenation of Methanol to Formaldehyde Silver‐Containing Catalysts Copper‐Containing Catalysts Zinc‐Containing Catalysts Other Catalysts Industrial Applications

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Cited by 8 publications
(8 citation statements)
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“…The ratio of rates of production of acetaldehyde to formaldehyde is about 300 at 500 K, decreasing to about 200 and 100 at 600 and 700 K, respectively. Overall, the simulated results here are reasonably consistent with the experimental observations of the lower production efficiency of formaldehyde ,,, compared to acetaldehyde on Cu. A high temperature is needed to produce anhydrous formaldehyde on Cu; however, an upper bound of temperature should exist to avoid its further decomposition into CO and H 2 .…”
Section: Resultssupporting
confidence: 87%
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“…The ratio of rates of production of acetaldehyde to formaldehyde is about 300 at 500 K, decreasing to about 200 and 100 at 600 and 700 K, respectively. Overall, the simulated results here are reasonably consistent with the experimental observations of the lower production efficiency of formaldehyde ,,, compared to acetaldehyde on Cu. A high temperature is needed to produce anhydrous formaldehyde on Cu; however, an upper bound of temperature should exist to avoid its further decomposition into CO and H 2 .…”
Section: Resultssupporting
confidence: 87%
“…Overall, the decreased production efficiency of formaldehyde ,,, compared to acetaldehyde on Cu can be qualitatively understood by their reaction kinetics. The critical differences in C–H bond-breaking barriers between methoxy and the other alkoxides are much larger than errors in the calculations, which are typically <0.05 eV.…”
Section: Resultsmentioning
confidence: 99%
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“…Aldehydes are important precursors or reactants in the production of a large number of industrial chemicals, such as plastics, resins, explosives, and drugs. , The oxidative dehydrogenation of alcohols over noble-metal-based catalysts in the presence of O 2 is generally used for commercial catalytic processes, which creates a significant energy cost because of the need to separate the water byproduct . Therefore, there is considerable interest in the development of catalytic non-oxidative alcohol dehydrogenation pathways in which, instead of water, valuable H 2 is produced.…”
Section: Introductionmentioning
confidence: 99%
“…All the parameters of the microkinetic model were performed as described in Section 3 of the Supplementary information. The steadystate numerical solutions to the microkinetic model were obtained assuming a 0.1% approach to equilibrium (95% CH 3 OH, 1% CH 2 O, 1% CO, and 3% H 2 ) at 823 K and 1 bar to achieve reasonable rates and simulate reactor operation under differential conditions [28].…”
Section: Microkinetic Modelingmentioning
confidence: 99%