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266 results about "Transfer hydrogenation" patented technology

Transfer hydrogenation is the addition of hydrogen (H₂; dihydrogen in inorganic and organometallic chemistry) to a molecule from a source other than gaseous H₂. It is applied in industry and in organic synthesis, in part because of the inconvenience and expense of using gaseous H₂. One large scale application of transfer hydrogenation is coal liquefaction using "donor solvents" such as tetralin.

Preparation method and application of glycopyrronium bromide chiral antipode

The invention belongs to the technical field of medicine, and discloses a preparation method of (3S,2'S), (3S,2'R), (3R,2'R) and (3R,2'S) four type chiral monomers of muscarine receptor antagonist racemic medicine glycopyrronium bromide. The method comprises the following steps: resolving racemic alpha-cyclopentylmandelic acid by a chemical resolution method by using L-Tyrosine methyl ester and (R)-alpha-phenylethylamine as resolution reagents to respectively prepare (S)-alpha-cyclopentylmandelic acid and (R)-alpha-cyclopentylmandelic acid; and carrying out esterification reaction to respectively obtain chiral intermediates (S)/(R)-alpha-cyclopentylmethyl mandelate. L/D-malic acid used as the raw material is subjected to four reaction steps, including condensation, carbonyl reduction, catalytic hydrogenation or transfer hydrogenation reduction debenzylation, and reduction alkylation or alkylogen alkylation, in a chiral synthesis mode to obtain another important chiral intermediate (S)/(R)-N-methyl-3-hydroxypyrrolidine. The chiral intermediate is subjected to ester exchange and quaterisation to respectively obtain the four (3S,2'S), (3S,2'R), (3R,2'R) and (3R,2'S) type glycopyrronium bromide chiral monomers. The result indicates that the (3R,2'S)-glycopyrronium bromide has the strongest cholinergic antagonistic action.
Owner:SHENYANG PHARMA UNIVERSITY +1

Catalytic hydrogenation method for olefin

The invention relates to a catalytic hydrogenation method of alkene. Under the conditions of alkene hydrogenation and the existence of hydrogenation catalysts, the alkene is reacted with hydrogen in contact way in a reactor; wherein, the reactor comprises a reacting tower and a reacting vessel, and the reacting tower and the reacting vessel are communicated with each other; the reaction tower is positioned above the reacting vessel; the hydrogen is sent into the reacting vessel from the bottom of the reacting vessel; the alkene is sent into from the middle-upper part of the reacting tower and/or the reacting vessel and contacts hydrogen in a countercurrent way; during the hydrogenation, the production separation is carried out; the light fraction exacted from the reacting tower after hydrogenation and the heavy fraction left on bottom of the reacting vessel after hydrogenation are reclaimed. The method of the invention saves the separation step and separation equipment of the ordinary alkene hydrogenation, thus greatly simplifying technology process. Besides, by directly applying reaction heat to separation of products, the energy consumption is decreased. In addition, the catalysis is carried out by taking the way of suspending and dispersing the hydrogenation catalyst into the reaction compound containing hydrogen and alkene so as to greatly improve catalysis effect and efficiency.
Owner:CHINA PETROLEUM & CHEM CORP +1

Porous carbon aerogel catalyst, and preparation method and application thereof

The invention belongs to the technical field of preparation of catalysts, and concretely relates to a porous carbon aerogel catalyst, and a preparation method and an application thereof. The method comprises the following steps: dissolving cellulose under a high-speed stirring condition, mixing the dissolved cellulose with a transition metal salt solution, and sequentially solidifying, drying, carbonizing and washing the obtained mixed solution to simultaneously achieve the preparation of aerogel and the loading of a transition metal in order to obtain the porous carbon aerogel with highly dispersed catalyst active sites. The catalyst has a good stability and a high catalytic activity, and can efficiently catalyze the transfer hydrogenation reaction of aldehydes, ketones or levulinates andalcoholic organic substances, wherein the conversion rate of aldehydes to alcohols reaches up to 98-100%, and the selectivity of alcohols reaches up to 81-99%. The catalyst is a solid aerogel monolith catalyst, so the catalyst can be well dispersed in a solution without stirring, and is easy to separate and recover. Additionally, the catalyst adopts cellulose as a raw material, so the catalyst has the advantages of low cost, greenness, environmental protection, renewability, simple preparation process, and easiness in industrialization.
Owner:SOUTH CHINA UNIV OF TECH

An enzymatic citral asymmetric reduction method capable of increasing optical purity of (R)-citronellal

An enzymatic citral asymmetric reduction method capable of increasing optical purity of (R)-citronellal is disclosed, namely a method coupling an amino-acid-catalyzed citral cis-trans isomerization reaction and a citral asymmetric hydrogenation reaction catalyzed by a saccharomyces cerevisiae enol reductase OYE1 to increase the optical purity of the (R)-citronellal that is a product of citral hydrogenation. When citral cis-trans isomers are subjected to the asymmetric hydrogenation reaction catalyzed by the saccharomyces cerevisiae enol reductase OYE1 to synthesize the (R)-citronellal, the (R)-citronellal is derived from trans-citral, (S)-citronellal is derived from cis-citral, and the catalysis speed for the trans-citral is higher than that for the cis-citral. Through coupling with the amino-acid-catalyzed citral cis-trans isomerization reaction, a part of the cis-citral is converted into the trans-citral, thus greatly increasing the ee value of the product that is the (R)-citronellal. In a catalytic system having a volume of 10 mL, 100 mg/mL of glycine is added, after 50 mM citral is subjected to a catalytic reaction for 4 h, the ee value of the (R)-citronellal is 65.4%, and is increased by 48.7% when being compared with the ee value of (R)-citronellal when the cis-trans isomerization reaction is not coupled.
Owner:ZHEJIANG UNIV OF TECH
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