Patent classifications
C07C49/10
NONAQUEOUS ELECTROLYTE SECONDARY BATTERY
A non-aqueous electrolyte secondary cell provided with: a positive electrode that has a positive electrode active material; a negative electrode; and a non-aqueous electrolyte. The positive electrode active material contains a lithium composite oxide containing Ni, and the non-aqueous electrolyte contains a non-aqueous solvent containing a fluorinated chain carboxylic acid ester and an organochlorine compound. The organochlorine compound is represented by general formula CF.sub.3CH.sub.2CO-CClR.sub.1R.sub.2 (where in the formula. R.sub.1 and R.sub.2 are respectively independent, and are selected from a hydrogen, a halogen, a C1-2 alkyl group, or a C1-2 halogenated alkyl group).
Process for producing cumene and/or sec-butylbenzene using a mixed olefins stream as alkylation agent
The present invention relates to a process for producing cumene and/or sec-butylbenzene comprising contacting benzene with a mixed olefins stream comprising ethylene and an alkylation agent in the presence of a selective alkylation catalyst under selective alkylation conditions.
Process for producing cumene and/or sec-butylbenzene using a mixed olefins stream as alkylation agent
The present invention relates to a process for producing cumene and/or sec-butylbenzene comprising contacting benzene with a mixed olefins stream comprising ethylene and an alkylation agent in the presence of a selective alkylation catalyst under selective alkylation conditions.
PROCESSES FOR PREPARATION OF EMPAGLIFLOZIN
The present invention relates to processes for the preparation of empagliflozin. In particular, the present invention relates to the preparation of empagliflozin and intermediates thereof. The present invention also relates to co-crystal of empagliflozin and amino acid and amorphous form of empagliflozin.
PROCESSES FOR PREPARATION OF EMPAGLIFLOZIN
The present invention relates to processes for the preparation of empagliflozin. In particular, the present invention relates to the preparation of empagliflozin and intermediates thereof. The present invention also relates to co-crystal of empagliflozin and amino acid and amorphous form of empagliflozin.
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.
Catalysts for conversion of 2,3-butanediol-containing fermentation mixture to hydrocarbons
A method for producing one or more hydrocarbon compounds from at least one of 2,3-butanediol, acetoin, and ethanol, the method comprising contacting said at least one of 2,3-butanediol, acetoin, and ethanol with a catalyst at a temperature of at least 100 C. and up to 500 C. to result in said 2,3-butanediol, acetoin, and/or ethanol being converted to said one or more hydrocarbon compounds, wherein said catalyst is either: (i) a catalyst comprising nanoparticles composed of (a) a first metal oxide selected from the group consisting of zirconium oxide, cerium oxide, titanium oxide, and lanthanum oxide, and (b) a main group metal oxide; or (ii) a catalyst comprising a zeolite loaded with at least one metal selected from the group consisting of copper, silver, nickel, palladium, platinum, rhodium, and ruthenium in an amount of 1-30 wt % by weight of the zeolite.
Catalysts for conversion of 2,3-butanediol-containing fermentation mixture to hydrocarbons
A method for producing one or more hydrocarbon compounds from at least one of 2,3-butanediol, acetoin, and ethanol, the method comprising contacting said at least one of 2,3-butanediol, acetoin, and ethanol with a catalyst at a temperature of at least 100 C. and up to 500 C. to result in said 2,3-butanediol, acetoin, and/or ethanol being converted to said one or more hydrocarbon compounds, wherein said catalyst is either: (i) a catalyst comprising nanoparticles composed of (a) a first metal oxide selected from the group consisting of zirconium oxide, cerium oxide, titanium oxide, and lanthanum oxide, and (b) a main group metal oxide; or (ii) a catalyst comprising a zeolite loaded with at least one metal selected from the group consisting of copper, silver, nickel, palladium, platinum, rhodium, and ruthenium in an amount of 1-30 wt % by weight of the zeolite.
Catalysts for conversion of 2,3-butanediol-containing fermentation mixture to hydrocarbons
A method for producing one or more hydrocarbon compounds from at least one of 2,3-butanediol, acetoin, and ethanol, the method comprising contacting said at least one of 2,3-butanediol, acetoin, and ethanol with a catalyst at a temperature of at least 100 C. and up to 500 C. to result in said 2,3-butanediol, acetoin, and/or ethanol being converted to said one or more hydrocarbon compounds, wherein said catalyst is either: (i) a catalyst comprising nanoparticles composed of (a) a first metal oxide selected from the group consisting of zirconium oxide, cerium oxide, titanium oxide, and lanthanum oxide, and (b) a main group metal oxide; or (ii) a catalyst comprising a zeolite loaded with at least one metal selected from the group consisting of copper, silver, nickel, palladium, platinum, rhodium, and ruthenium in an amount of 1-30 wt % by weight of the zeolite.