Effect of MgO addition to Cu-Ni/Al2O3 catalysts on glycerol hydrogenolysis in continuous reactor without external hydrogen was written by Mendonca, Victor G. S.;Freitas, Isabelle C.;Manfro, Robinson L.;Souza, Mariana M. V. M.. And the article was included in Applied Catalysis, A: General in 2022.Quality Control of 1,2-Propanediol This article mentions the following:
Cu-Ni/xMgO-Al2O3 catalysts with x = 0, 10, 20 and 30 wt% were prepared and evaluated in glycerol hydrogenolysis to 1,2-propanediol (1,2-PDO) at 250°C, pressure of 40 bar for 30 h, without addition of external hydrogen. The addition of MgO to alumina decreased the surface area, increased the Cu/Ni dispersion and the number of basic sites. The highest 1,2-PDO yield was achieved by Cu-Ni/30%MgO-Al2O3 catalyst: 50% after 6 h of reaction; it decreases to 25% after 30 h. The decrease in 1,2-PDO yield is accompanied by an increase in acetol yield, showing that the rate limiting step for MgO-Al2O3 catalysts is the hydrogenation of acetol to 1,2-PDO because there is not enough hydrogen in reaction medium. For Cu-Ni/MgO catalyst, the reaction pathway changed to the basic route, with preferential formation of lactic acid (50% of lactic acid yield in the first hours of reaction). In the experiment, the researchers used many compounds, for example, 1,2-Propanediol (cas: 57-55-6Quality Control of 1,2-Propanediol).
1,2-Propanediol (cas: 57-55-6) belongs to alcohols. Alcohols are weak acids. The most acidic simple alcohols (methanol and ethanol) are about as acidic as water, and most other alcohols are somewhat less acidic. Converting an alcohol to an alkene requires removal of the hydroxyl group and a hydrogen atom on the neighbouring carbon atom. Dehydrations are most commonly carried out by warming the alcohol in the presence of a strong dehydrating acid, such as concentrated sulfuric acid.Quality Control of 1,2-Propanediol
Referemce:
Alcohol – Wikipedia,
Alcohols – Chemistry LibreTexts