2568-90-3Relevant articles and documents
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Bal,B.S.,Pinnick,H.W.
, p. 3727 - 3728 (1979)
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Utilization of Formic Acid as C1 Building Block for the Ruthenium-Catalyzed Synthesis of Formaldehyde Surrogates
Beydoun, Kassem,Thenert, Katharina,Wiesenthal, Jan,Hoppe, Corinna,Klankermayer, Jürgen
, p. 1944 - 1947 (2020/04/08)
Dialkoxymethanes are becoming increasingly important as fuel additives, formaldehyde surrogates, and chemical intermediates, but the effective synthesis remains challenging. Herein, the catalytic synthesis of dialkoxymethane products using a molecular catalyst is reported. The catalytic system, comprising the [Ru(triphos)(tmm)] in combination with the Lewis acid Al(OTf)3, enables the direct synthesis of dialkoxymethane products with formic acid as C1 building block in high to excellent turnover numbers.
Tailor-made Molecular Cobalt Catalyst System for the Selective Transformation of Carbon Dioxide to Dialkoxymethane Ethers
Schieweck, Benjamin G.,Klankermayer, Jürgen
supporting information, p. 10854 - 10857 (2017/08/30)
Herein a non-precious transition-metal catalyst system for the selective synthesis of dialkoxymethane ethers from carbon dioxide and molecular hydrogen is presented. The development of a tailored catalyst system based on cobalt salts in combination with selected Triphos ligands and acidic co-catalysts enabled a synthetic pathway, avoiding the oxidation of methanol to attain the formaldehyde level of the central CH2 unit. This unprecedented productivity based on the molecular cobalt catalyst is the first example of a non-precious transition-metal system for this transformation utilizing renewable carbon dioxide sources.
Preparation method of dibutoxymethane
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Paragraph 0035; 0036, (2016/10/10)
The invention discloses a preparation method of dibutoxymethane and relates to a preparation method of methane. The method comprises the process as follows: dimethoxymethane and n-butanol in a certain proportion are taken as raw materials, various liquid acids and supported liquid acids are taken as catalysts, the mixture is subjected to a reaction at the temperature of 0-160 DEG C and under the pressure of 0.1-10.0 MPa, and dibutoxymethane is generated in a high-selectivity manner; a heteropolyacid catalyst is prepared with an equivalent-volume impregnation method, and at least one of activated carbon, TiO2, Al2O3, SiO2, SBA-15 and MCM-41 is taken as a supporter; the supported heteropolyacid catalyst comprises heteropolyacid and a supporter for supporting the heteropolyacid, and heteropolyacid is one or more of phosphotungstic acid, silicotungstic acid, phosphomolybdic acid and silicomolybdic acid. A product prepared with the method is relatively single, the selectivity is high, required raw materials are cheap and easy to obtain, the whole process is simple to operate, no chemical substances polluting the environment are produced, and the preparation method belongs to an environment-friendly technological route.