摘要:
The present invention relates to a process for producing unsaturated cyclic and/or aromatic compounds from 1,8-cineole, the process comprising pyrolysing 1,8-cineole in the presence of gamma-alumina supported transition metal catalyst.
摘要:
Provided are a selective hydrogenation catalyst exhibiting a superior reactivity and selectivity against an oxygen-containing polar functional group(s) in a compound having a hydrogenation reaction site(s) such as a carbon-carbon double bond and an oxygen-containing polar functional group(s) such as an epoxy bond; a method for producing such selective hydrogenation catalyst; and a method for selectively hydrogenating such compound using this type of selective hydrogenation catalyst. In a method for hydrogenating a compound having a hydrogenation reaction site(s) and an oxygen-containing polar functional groups(s), this compound is brought into contact with a hydrogen gas in a liquid phase under the presence of a selective hydrogenation catalyst with a silver component-cerium oxide complex being supported on a metal oxide support, the silver component-cerium oxide complex including silver component particles and a cerium oxide supported on the surfaces of such silver component particles. Thus, the oxygen atoms in the oxygen-containing polar functional group(s) can be selectively hydrogenated.
摘要:
The present invention relates to a process for producing unsaturated cyclic and/or aromatic compounds from 1,8-cineole, the process comprising pyrolysing 1,8-cineole in the presence of gamma-alumina supported transition metal catalyst.
摘要:
The invention is directed to the increasing of selectiveness of the process (UYUP), increasing of conversion of raw materials and heavy residue, and also the depth of processing. The indicated technical result is achieved by that way, that the method of processing of co-products of liquid-phase synthesis of isoprene from formaldehyde or formaldehyde-containing products is carried out at the temperature of 400-480°C in the presence of the water vapor with the aluminum silicate-containing catalyst with the further heating up to the temperature of 400-550°C, in this case, the process is carried out at the initial temperature, that is 5-40°C lower and the final temperature, that is 5-40°C higher, than the average temperature of contacting during the progressive increasing of the temperature from the initial au to the final one and during the constant reducing of the feed space velocity at the beginning of contacting 3-15 % higher, and at the end of contacting 3-15 % lower, than the middling cycling feed space velocity (table 4).