1825-14-5Relevant articles and documents
Itoh,O. et al.
, p. 1353 - 1358 (1976)
Heterogenized Ru(II) phenanthroline complex for chemoselective hydrogenation of diketones under biphasic aqueous medium
Deshmukh, Amit,Kinage, Anil,Kumar, Rajiv,Meijboom, Reinout
, p. 114 - 120 (2010)
The chemoselective hydrogenation of acetylacetone to 4-hydroxypentan-2-one over immobilized ruthenium phenanthroline metal complexes in amino functionalized MCM-41 in biphasic aqueous reaction medium was investigated. The catalyst was characterized by XRD, TEM, surface analysis, FT-IR and UV-vis to understand the morphology, complex geometry, and XPS such that the oxidation state of the metal complex inside the MCM-41 framework could be understood. The use of water as a solvent, not only gives high activity and selectivity for hydrogenation of acetylacetone, but also gives a path for an environmentally safer process. The optimizations of ligand, metal to ligand ratio, the choice of solvent and other reaction parameters were studied in detail. The heterogeneous catalytic system gave a higher degree of chemoselectivity (99%) towards 4-hydroxypentan-2-one as compared to homogeneous catalyst when hydrogenation was carried out using water as a solvent. The immobilized ruthenium-phenanthroline complex was easily separated and reused.
Tanabe
, p. 2233 (1973)
Stereochemical Studies of the Hydrogenation with an Asymmetrically Modified Raney Nickel Catalyst. The Hydrogenation of Acetylacetone
Tai, Akira,Ito, Kazuhisa,Harada, Tadao
, p. 223 - 227 (1981)
The hydrogenation of acetylacetone (I) over asymmetrically modified Raney nickel (MRNi) proceeded, step by step, as follows: Step 1 Step 2 acetylacetone (I) ------> 4-hydroxy-2-pentanone (III) ------> 2,4-pentanediol (II).It was demonstrated that the optical yield of Step 1 and the diastereomer excess of Step 2 are governed by the ratio of the stereo-differentiating reaction site to the non-stereo-differentiating reaction site on the catalyst.The stereochemistry of each step was also discussed based on the mode of the intermolecular hydrogen bondings between the substrate and tartaric acid adsorbed on the catalyst.RNi modified with a mixture of tartaric acid and NaBr (TA-NaBr-MRNi) gave the best result with respect to both Step 1 and Step 2.
Chemoselective formation of cyclo-aliphatic and cyclo-olefinic 1,3-diolsviapressure hydrogenation of potentially biobased platform molecules using Kn?lker-type catalysts
Alsters, Paul L.,Chou, Khi Chhay,De Wildeman, Stefaan M. A.,Faber, Teresa,Hadavi, Darya,Han, Peiliang,Quaedflieg, Peter J. L. M.,Schwalb Freire, Alfonso J.,Verzijl, Gerard K. M.,van Slagmaat, Christian A. M. R.
supporting information, p. 10102 - 10112 (2021/08/03)
The hydrogenative conversions of the biobased platform molecules 4-hydroxycyclopent-2-enone and cyclopentane-1,3-dione to their corresponding 1,3-diols are established using a pre-activated Kn?lker-type iron catalyst. The catalyst exhibits a high selectivity for ketone reduction, and does not induce dehydration. Moreover, by using different substituents of the ligand, thecis-transratio of the products can be affected substantially. A decent compatibility of this catalytic system with various structurally related substrates is demonstrated.
Method for preparing beta-diol from beta-diketone by hydrogenation
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Paragraph 0041-0044, (2017/02/23)
The invention relates to a method for preparing beta-diol from beta-diketone by hydrogenation. The method comprises the following steps: in the presence of a catalyst and under the fixed-bed hydrotreating reaction condition, enabling beta-diketone to be in contact with hydrogen, so as to obtain beta-diol, wherein the catalyst contains CuO and ZnO, preferably also contains Al2O3, and more preferably also contains alkali metal oxides. According to the method for preparing beta-diol from beta-diketone by hydrogenation, provided by the invention, the technology of continuously producing beta-diol by adopting a fixed bed device is realized, the technology is simple and convenient to operate, the utilization ratio of raw materials and the production efficiency of products are improved, the reaction does not need to be carried out under high pressure, and potential safety hazards are reduced.
