Patent classifications
C07C45/73
Method for catalytic production of refined enal products from an aldehyde feed stream using a single enclosed unit
Disclosed is a method for forming enals from corresponding alehydes in a single enclosed unit such as a divided wall reaction distillation unit. The method of the present invention includes (a) feeding an aldehyde feed stream comprising at least one aldehyde reactant into a reaction zone contained within said single enclosed unit; (b) reacting said at least one aldehyde reactant in said reaction zone in the presence of a catalyst to form an enal-containing reaction zone effluent comprising an enal; (c) purifying said enal-containing reaction zone effluent in a first separation zone within said single enclosed unit to form an enal-rich product mixture and a residual unreacted aldehyde mixture; and (d) collecting from said single enclosed unit at least a portion of said enal-rich product mixture. The method of the present invention results in high enal yields at a markedly reduced capital cost and energy consumption as compared to prior art processes.
Method for producing high-octane components from olefins from catalytic cracking
- Aleksandr Sergeevich Haritonov ,
- Konstantin Aleksandrovich Dubkov ,
- Mihail Vladimirovich PARFENOV ,
- Aleskandr Stepanovich Noskov ,
- Valery Aleksandrovich Golovachev ,
- Andrei Vladimirovich KLEIMENOV ,
- Dmitry Olegovich KONDRASHEV ,
- Valentina Dmitrievna Miroshkina ,
- Dmitrii Petrovich Ivanov ,
- Sergey Vladimirovich Semikolenov ,
- Valery Sergeevich Chernyavsky ,
- Larisa Vladimirovna Piryutko ,
- Kristina Andreevna Rusetskaya ,
- Sergey Evgenyevich Kuznetsov
The invention relates to the field of petrochemistry, and specifically to a method for synthesizing high-octane oxygen containing components of motor fuel. The objects of the invention consist in variants of a method for synthesizing high-octane oxygen-containing components of motor fuel from olefin-containing gas mixtures via oxidative non-catalytic conversions using nitrous oxide, and the subsequent condensation and hydrogenation of the produced oxygenates using heterogeneous catalysts. The high-octane components according to the proposed method consist in a mixture of carbonyl compounds (ketones, aldehydes, hydroxy ketones, hydroxy aldehydes) C.sub.2-C.sub.9 and/or branched hydrocarbons C.sub.5-C.sub.9 and/or alcohols in different ratios. Depending on the production method variant, the octane number of a mixture of the proposed high-octane components consists in a value between 100 and 130 RON. The technical result consists in broadening the resource base for the production of high-octane gasolines and of a variety of environmentally-friendly high-octane additives.
Method for producing high-octane components from olefins from catalytic cracking
- Aleksandr Sergeevich Haritonov ,
- Konstantin Aleksandrovich Dubkov ,
- Mihail Vladimirovich PARFENOV ,
- Aleskandr Stepanovich Noskov ,
- Valery Aleksandrovich Golovachev ,
- Andrei Vladimirovich KLEIMENOV ,
- Dmitry Olegovich KONDRASHEV ,
- Valentina Dmitrievna Miroshkina ,
- Dmitrii Petrovich Ivanov ,
- Sergey Vladimirovich Semikolenov ,
- Valery Sergeevich Chernyavsky ,
- Larisa Vladimirovna Piryutko ,
- Kristina Andreevna Rusetskaya ,
- Sergey Evgenyevich Kuznetsov
The invention relates to the field of petrochemistry, and specifically to a method for synthesizing high-octane oxygen containing components of motor fuel. The objects of the invention consist in variants of a method for synthesizing high-octane oxygen-containing components of motor fuel from olefin-containing gas mixtures via oxidative non-catalytic conversions using nitrous oxide, and the subsequent condensation and hydrogenation of the produced oxygenates using heterogeneous catalysts. The high-octane components according to the proposed method consist in a mixture of carbonyl compounds (ketones, aldehydes, hydroxy ketones, hydroxy aldehydes) C.sub.2-C.sub.9 and/or branched hydrocarbons C.sub.5-C.sub.9 and/or alcohols in different ratios. Depending on the production method variant, the octane number of a mixture of the proposed high-octane components consists in a value between 100 and 130 RON. The technical result consists in broadening the resource base for the production of high-octane gasolines and of a variety of environmentally-friendly high-octane additives.
METHOD FOR PRODUCING HIGH-OCTANE COMPONENTS FROM OLEFINS FROM CATALYTIC CRACKING
- Aleksandr Sergeevich Haritonov ,
- Konstantin Aleksandrovich Dubkov ,
- Mihail Vladimirovich PARFENOV ,
- Aleskandr Stepanovich Noskov ,
- Valery Aleksandrovich Golovachev ,
- Andrei Vladimirovich KLEIMENOV ,
- Dmitry Olegovich KONDRASHEV ,
- Valentina Dmitrievna Miroshkina ,
- Dmitrii Petrovich Ivanov ,
- Sergey Vladimirovich Semikolenov ,
- Valery Sergeevich Chernyavsky ,
- Larisa Vladimirovna Piryutko ,
- Kristina Andreevna Rusetskaya ,
- Sergey Evgenyevich Kuznetsov
The invention relates to the field of petrochemistry, and specifically to a method for synthesizing high-octane oxygen containing components of motor fuel. The objects of the invention consist in variants of a method for synthesizing high-octane oxygen-containing components of motor fuel from olefin-containing gas mixtures via oxidative non-catalytic conversions using nitrous oxide, and the subsequent condensation and hydrogenation of the produced oxygenates using heterogeneous catalysts. The high-octane components according to the proposed method consist in a mixture of carbonyl compounds (ketones, aldehydes, hydroxy ketones, hydroxy aldehydes) C.sub.2-C.sub.9 and/or branched hydrocarbons C.sub.5-C.sub.9 and/or alcohols in different ratios. Depending on the production method variant, the octane number of a mixture of the proposed high-octane components consists in a value between 100 and 130 RON. The technical result consists in broadening the resource base for the production of high-octane gasolines and of a variety of environmentally-friendly high-octane additives.
CATALYTICAL PROCESS OF MAKING 4-HEXEN-3-ONE
This disclosure relates to a process which involves reacting 2-butanone with acetaldehyde in the presence of a zinc complex catalyst in a reaction zone to produce a product mixture comprising 4-hexen-3-one and 3-methyl-3-penten-2-one. This disclosure also relates to a process which involves (a) reacting 2-butanone with acetaldehyde in the presence of a zinc complex catalyst to produce a product mixture comprising 4-hexen-3-one, 3-methyl-3-penten-2-one and the zinc complex catalyst; (b) recovering the zinc complex catalyst from the product mixture; and (c) reusing the recovered zinc complex catalyst in the reacting step (a).
CATALYTICAL PROCESS OF MAKING 4-HEXEN-3-ONE
This disclosure relates to a process which involves reacting 2-butanone with acetaldehyde in the presence of a zinc complex catalyst in a reaction zone to produce a product mixture comprising 4-hexen-3-one and 3-methyl-3-penten-2-one. This disclosure also relates to a process which involves (a) reacting 2-butanone with acetaldehyde in the presence of a zinc complex catalyst to produce a product mixture comprising 4-hexen-3-one, 3-methyl-3-penten-2-one and the zinc complex catalyst; (b) recovering the zinc complex catalyst from the product mixture; and (c) reusing the recovered zinc complex catalyst in the reacting step (a).
SINGLE-STEP CONVERSION OF N-BUTYRALDEHYDE TO 2-ETHYLHEXANAL
Disclosed is a method of making and using a titania supported palladium catalyst for the single step synthesis of 2-ethylhexanal from a feed of n-butyraldehyde. This titania supported palladium catalyst demonstrates high n-butyraldehyde conversion but also produces 2-ethylhexanal in an appreciable yield with maintained activity between runs. This method provides a single step synthesis of 2-ethylhexanal from n-butyraldehyde with a catalyst that can be regenerated that provides cleaner downstream separations relative to the traditional caustic route.
SINGLE-STEP CONVERSION OF N-BUTYRALDEHYDE TO 2-ETHYLHEXANAL
Disclosed is a method of making and using a titania supported palladium catalyst for the single step synthesis of 2-ethylhexanal from a feed of n-butyraldehyde. This titania supported palladium catalyst demonstrates high n-butyraldehyde conversion but also produces 2-ethylhexanal in an appreciable yield with maintained activity between runs. This method provides a single step synthesis of 2-ethylhexanal from n-butyraldehyde with a catalyst that can be regenerated that provides cleaner downstream separations relative to the traditional caustic route.
Single step conversion of N-butyraldehyde to 2-ethylhexanal
Disclosed is a method of making and using a titania supported palladium catalyst for the single step synthesis of 2-ethylhexanal from a feed of n-butyraldehyde. This titania supported palladium catalyst demonstrates high n-butyraldehyde conversion but also produces 2-ethylhexanal in an appreciable yield with maintained activity between runs. This method provides a single step synthesis of 2-ethylhexanal from n-butyraldehyde with a catalyst that can be regenerated that provides cleaner downstream separations relative to the traditional caustic route.
Single step conversion of N-butyraldehyde to 2-ethylhexanal
Disclosed is a method of making and using a titania supported palladium catalyst for the single step synthesis of 2-ethylhexanal from a feed of n-butyraldehyde. This titania supported palladium catalyst demonstrates high n-butyraldehyde conversion but also produces 2-ethylhexanal in an appreciable yield with maintained activity between runs. This method provides a single step synthesis of 2-ethylhexanal from n-butyraldehyde with a catalyst that can be regenerated that provides cleaner downstream separations relative to the traditional caustic route.