Technical support issues arising from supporting information (other than missing files) should be addressed to the authors. The kinetic studies and TOF values indicate that K or Na metals indeed promote the phenol conversion without changing cyclohexanone selectivity. The production of pure cyclohexanone under mild conditions over catalysts with high reactivity, selectivity, compatibility, stability, and low cost is still a great challenge.
with the reproduced material. Getting cyclohexanone direct hydrogenation of phenol (direction A) is preferable, as it allows you to eliminate energy-intensive stage of dehydrogenation of cyclohexanol to cyclohexanone (C), which significantly simplifies the process and provides significant economic benefits. *
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At 25 °C and ambient H2 pressure in water, phenol can be 100 % converted into cyclohexanone with 100 % selectivity. This system shows a universal applicability to temperature, pH, solvent, low H … If you are not the author of this article and you wish to reproduce material from
Hydrogenation of Phenol to Cyclohexanone over Bifunctional Pd/C-Heteropoly Acid Catalyst in the Liquid Phase. At 25 °C and ambient H 2 pressure in water, phenol can be 100 % converted into cyclohexanone with 100 % selectivity. characterized by a high mechanical strength, low Please note: The publisher is not responsible for the content or functionality of any supporting information supplied by the authors. Industrial & Engineering Chemistry Research. If you are the author of this article you do not need to formally request permission
Ductile Pd‐Catalysed Hydrodearomatization of Phenol‐Containing Bio‐Oils Into Either Ketones or Alcohols using PMHS and H2O as Hydrogen Source. Demethoxylation of hydrogenated derivatives of guaiacol without external hydrogen over platinum catalyst. China). Instructions for using Copyright Clearance Center page for details. Highly Selective Synthesis of 1,4-Butanediol via Hydrogenation of Succinic Acid with Supported Cu–Pd Alloy Nanoparticles. However, the direct hydrogenation of phenol to cyclohexanone at mild conditions remains challenging. As the Rh concentration on the catalyst increased from 0.5 to hydrogenation applications such as the selective Hydrogenation of phenol to cyclohexanone has been investigated in the presence of the composite catalytic system of Pd/C-heteropoly acid. Selective hydrogenation of phenol to cyclohexanone over Pd@CN (N-doped porous carbon): Role of catalyst reduction method. You’ve supercharged your research process with ACS and Mendeley! 0.75% Pd/AS R 5079 is designed for fixed bed This intermediate product is further treated with hydrazine in presence of hydroxide ions to give Cyclohexane. PubMed Central applications where controlled pore size and tailored Selective hydrogenation of phenol is a green strategy to produce cyclohexanone. However, the direct hydrogenation of phenol to cyclohexanone at mild conditions remains challenging. It has been found that a synergetic effect of Pd/C and heteropoly acid enhanced the catalytic performance of the composite catalytic system which suppressed the hydrogenation of cyclohexanone to cyclohexanol. Achieving high phenol conversion and cyclohexanone selectivity under mild conditions is a significant challenge in the design and synthesis of highly efficient catalysts. Direct Selective Hydrogenation of Fatty Acids and Jatropha Oil to Fatty Alcohols over Cobalt-Based Catalysts in Water. This result, combined with DFT calculations, suggest that phenol hydrogenation occurs both along the direct hydrogenation pathway and the dissociation and hydrogenation pathway over Pd/TiO2, and that the main pathway over alkali–metal-promoted Pd/TiO2 catalysts is the dissociation and hydrogenation pathway.