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Небесная энциклопедия

Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

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Мониторинг СМИ

Мониторинг СМИ и социальных сетей. Сканирование интернета, новостных сайтов, специализированных контентных площадок на базе мессенджеров. Гибкие настройки фильтров и первоначальных источников.

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Форма поиска

Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
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Применить Всего найдено 21130. Отображено 100.
19-01-2012 дата публикации

Microencapsulated catalyst

Номер: US20120016139A1
Принадлежит: REAXA Ltd

The present invention relates to a catalyst system. In particular the invention relates to a catalyst in the form of metal or an alloy that is encapsulated within a polymer shell or matrix. More specifically the invention is directed towards reactive catalytic metals that may be pyrophoric or otherwise reactive in air and/or susceptible to oxidation. In particular, the invention is concerned with catalysts based on nickel. Raney or sponge nickel is highly hazardous: a self-igniting solid; produces hazardous fumes when burning; causes irritation of the respiratory tract, nasal cavities; causes pulmonary fibrosis if inhaled; ingestion may lead to convulsions and intestinal disorders; causes eye and skin irritation; and chronic exposure may lead to pneumonitis and sensitization (“nickel itch”). The invention provides metal catalysts that avoid such problems and have a good shelf life and working life.

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23-02-2012 дата публикации

Method for producing color-stable mda and mdi

Номер: US20120046497A1
Принадлежит: BASF SE

The invention relates to a process for preparing methylenediphenyldiamine (MDA) by reacting formaldehyde and aniline in the presence of an acidic catalyst, wherein the oxygen content in the process for preparing MDA is <10 000 ppm, based on all compounds present in the process. The invention further relates to the phosgenation of MDA to methylenediphenyl diisocyanate (MDI).

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08-03-2012 дата публикации

Zeolite-palladium complex, method for producing the same, catalyst containing the complex, and method for producing a coupling compound by using the catalyst

Номер: US20120059191A1
Принадлежит: Individual

There is provided a substance having much higher catalytic activity for a Suzuki-Miyaura coupling reaction than conventional heterogenous catalysts. The present invention provides a zeolite-palladium complex including USY-zeolite and Pd supported on the USY-zeolite, the Pd having a Pd—Pd coordination number of 4 or less and an oxidation number of 0.5 or less.

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03-05-2012 дата публикации

Method for the direct amination of hydrocarbons into amino hydrocarbons, including electrochemical separation of hydrogen and electrochemical reaction of the hydrogen into water

Номер: US20120107707A1
Принадлежит: BASF SE

Process for the direct amination of hydrocarbons to aminohydrocarbons by reaction of a feed stream E comprising at least one hydrocarbon and at least one aminating reagent to form a reaction mixture R comprising aminohydrocarbon and hydrogen in a reaction zone RZ and electrochemical separation of at least part of the hydrogen formed in the reaction from the reaction mixture R by means of a gastight membrane-electrode assembly having at least one selectively proton-conducting membrane and at least one electrode catalyst on each side of the membrane, where at least part of the hydrogen is oxidized to protons at the anode catalyst on the retentate side of the membrane and the protons pass through the membrane and on the permeate side are reacted with oxygen to form water, where the oxygen originates from an oxygen-comprising stream O which is brought into contact with the permeate side of the membrane, over the cathode catalyst.

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10-05-2012 дата публикации

Method for direct amination of hydrocarbons to form amino hydrocarbons with the electrochemical separation of hydrocarbon

Номер: US20120111732A1
Принадлежит: BASF SE

Process for the direct amination of hydrocarbons to aminohydrocarbons, which comprises the steps: a) reaction of a feed stream E comprising at least one hydrocarbon and at least one aminating reagent to form a reaction mixture R comprising aminohydrocarbons and hydrogen and b) electrochemical separation of at least part of the hydrogen formed in the reaction from the reaction mixture R by means of a gastight membrane-electrode assembly having at least one selectively proton-conducting membrane and at least one electrode catalyst on each side of the membrane, where at least part of the hydrogen is oxidized to protons over the anode catalyst on the retentate side of the membrane and the protons are, after passing through the membrane, b1) reduced to hydrogen and/or b2) reacted with oxygen from an oxygen-comprising stream O which is brought into contact with the permeate side of the membrane to form water over the cathode catalyst on the permeate side.

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10-05-2012 дата публикации

Process for separating one or more aliphatic diamines from reductive amination reaction solvents and impurities

Номер: US20120116123A1
Принадлежит: Dow Global Technologies LLC

The instant invention provides a process for separating one or more aliphatic diamines from reductive amination reaction solvents and impurities, and aliphatic diamines obtained via such a process. The process for separating one or more aliphatic diamines from reductive amination reaction solvents and impurities according to the instant invention comprises the steps of: (1) feeding one or more cycloaliphatic cyanoaldehydes, hydrogen, ammonia, and optionally one or more solvents into a continuous reductive amination reactor system; (2) contacting said one or more cycloaliphatic cyanoaldehydes, hydrogen, and ammonia with each other in the presence of one or more heterogeneous metal based catalyst systems at a temperature in the range of from 80° C. to about 160° C. and a pressure in the range of from 700 to 3500 psig; (3) thereby forming a product mixture comprising one or more cycloaliphatic diamines, optionally one or more bicyclic by-products, optionally one or more cycloaliphatic aminonitriles, optionally one or more cycloaliphatic aminoalcohols, optionally one or more oligomeric by-products, ammonia, water, hydrogen, and optionally one or more solvents; (4) removing said product mixture from the reactor system; (5) removing at least a portion of said ammonia, said hydrogen, or mixture thereof from said product mixture via distillation; (6) removing at least a portion of said water and said one or more optional solvents via distillation; (7) removing at least a portion of one or more optional bicyclic by-products via distillation; (8) removing one or more optional cycloaliphatic aminonitriles, one or more optional cycloaliphatic aminoalcohols, one or more optional oligomeric by-products via distillation; and (9) thereby separating said one or more cycloaliphatic diamines from said product mixture.

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24-05-2012 дата публикации

Method of preparing 1-chloroacetamido-1,3,3,5,5-pentamethylcyclohexane

Номер: US20120130127A1
Принадлежит: Mer Pharma GmbH and Co KGaA

Method of preparing 1-chloroacetamido-1,3,3,5,5-pentamethylcyclohexane, an intermediate in the synthesis of 1-amino-1,3,3,5,5-pentamethylcyclohexane (Neramexane) or a pharmaceutically acceptable salt thereof, comprising step (iii): (iii) reacting 1-hydroxy-1,3,3,5,5-pentamethylcyclohexane with chloroacetonitrile in the presence of an acid, wherein 1-hydroxy-1,3,3,5,5-pentamethylcyclohexane is employed in step (iii) as obtained in the reaction of a methylmagnesium halide with 3,3,5,5-tetramethylcyclohexanone without having been subjected to a purification step.

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31-05-2012 дата публикации

Process for improving the catalytic activity of catalyst systems for reductive amination of aliphatic cyanoaldehydes to aliphatic diamines

Номер: US20120136173A1
Принадлежит: Dow Global Technologies LLC

The instant invention provides a process for improving catalytic activity of catalyst systems for reductive amination of aliphatic cyanoaldehydes to aliphatic diamines. The process for improving catalytic activity of catalyst systems for reductive amination of aliphatic cyanoaldehydes to aliphatic diamines comprises the steps of: (1) feeding ammonia, optionally hydrogen, and optionally one or more solvents over one or more heterogeneous metal based catalyst systems having a reduced catalytic activity for a period of greater than 1 hour at a temperature in the range of from 50° C. to 500° C.; wherein said one or more heterogeneous metal based catalyst systems have a yield of less than 90 percent based on the molar conversion of cyanoaldehydes to diamines; and (2) thereby improving the catalytic activity of said one or more heterogeneous metal based catalyst systems.

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05-07-2012 дата публикации

Compositions, Synthesis, and Methods of Using Cycloalkylmethylamine Derivatives

Номер: US20120172426A1
Принадлежит: Reviva Pharmaceuticals Inc

The present invention provides novel cycloalkylmethylamine derivatives, and methods of preparing cycloalkylmethylamine derivatives. The present invention also provides methods of using cycloalkylmethylamine derivatives and compositions of cycloalkylmethylamine derivatives. The pharmaceutical compositions of the compounds of the present invention can be advantageously used for treating and/or preventing obesity and obesity related co-morbid indications and depression and depression related co-morbid indications.

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05-07-2012 дата публикации

Continuous method for the hydrogenation of aromatic compounds

Номер: US20120172632A1
Принадлежит: AET Group

The invention relates to a continuous method for the catalytic hydrogenation of an aromatic compound into a cycloaliphatic compound, wherein said method is carried out in a piston reactor provided with a mechanical axially agitating means and comprises continuously feeding a liquid phase comprising said aromatic compound and a catalyst dispersed to the liquid phase, subjecting said liquid phase, at a temperature of between 100° C. and 300° C. and while being mechanical axially agitated, to the effects of a hydrogen pressure of between 10 and 250 bars in the presence of said catalyst dispersed in the liquid phase for a residence time of between 1 second and 10 minutes, and removing the liquid phase from the reactor.

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27-09-2012 дата публикации

Process for hydrogenating nitriles

Номер: US20120245390A1
Принадлежит: BASF SE

The present invention relates to a process for hydrogenating nitriles by means of hydrogen in the presence of a catalyst in a reactor, where the catalyst is arranged in a fixed bed, wherein the cross-sectional loading in the reactor is in the range from 5 kg/(m 2 s) to 50 kg/(m 2 s). The present invention further relates to a process for preparing downstream products of isophoronediamine (IPDA) or N,N-dimethylaminopropylamine (DMAPA) from amines prepared according to the invention.

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18-10-2012 дата публикации

Efficient process to induce enantioselectivity in procarbonyl compounds

Номер: US20120264933A1
Принадлежит: Laurus Labs Pvt Ltd

The present invention provides an efficient method to induce the enantioselectivity in procarbonyl compounds using chiral organometallic complexes. The present invention also provides a method for producing chiral organometallic complexes using a chiral additive, achiral additive, a base and a metal salt.

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22-11-2012 дата публикации

Catalyst and process for hydrogenating aromatics

Номер: US20120296111A1
Принадлежит: BASF SE

The present invention relates to an eggshell catalyst comprising an active metal selected from the group consisting of ruthenium, rhodium, palladium, platinum and mixtures thereof, applied to a support material comprising silicon dioxide, wherein the pore volume of the support material is 0.6 to 1.0 ml/g, determined by Hg porosimetry, the BET surface area is 280 to 500 m 2 /g, and at least 90% of the pores present have a diameter of 6 to 12 nm, to a process for preparing this eggshell catalyst, to a process for hydrogenating an organic compound which comprises at least one hydrogenatable group using the eggshell catalyst, and to the use of the eggshell catalyst for hydrogenating an organic compound.

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03-01-2013 дата публикации

Process for the conversion of aromatic nitro compound into amines

Номер: US20130006018A1
Принадлежит: Huntsman International LLC

A process for hydrogenating an aromatic nitro compound according to the invention comprises providing a hydrogen gas stream and a liquid aromatic nitro compound stream; providing a fixed bed catalytic reactor having an inflow side and an outflow side; feeding to the inflow side, the hydrogen gas stream and the liquid aromatic nitro compound stream; converting the hydrogen gas and the aromatic nitro compound into an aromatic amine, thereby providing a reactor effluent comprising the aromatic amine and water; evacuating the reactor effluent from the reactor at the outflow side of the reactor; wherein an inert solvent or water is fed to the inflow side of the reactor at a molar ratio of moles inert solvent or water to moles hydrogen is more than 1.

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21-02-2013 дата публикации

Method for the Hydrolysis of Substituted Formylamines into Substituted Amines

Номер: US20130046111A1
Автор: Mikhail Bobylev
Принадлежит: Individual

An improved method for the synthesis of substituted formylamines and substituted amines via an accelerated Leuckart reaction. The Leuckart reaction is accelerated by reacting formamide or N-alkylformamide and formic acid with an aldehyde or a ketone at a preferred molar ratio that accelerates the reaction. The improved method is applicable to various substituted aldehydes and ketones, including substituted benzaldehydes. An accelerated method for the hydrolysis of substituted formylamines into substituted amines using acid or base and a solvent at an elevated temperature. The improved method is useful for the accelerated synthesis of agrochemicals and pharmaceuticals such as vanillylamine, amphetamine and its analogs, and formamide fungicides.

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28-02-2013 дата публикации

Process for preparing eddn and/or edmn and a process for preparing deta and/or teta

Номер: US20130053536A1
Принадлежит: BASF SE

A process for preparing EDDN and/or EDMN by a) conversion of FA, HCN and EDA, the conversion being effected in the presence of water, b) depleting water from the reaction mixture obtained in stage a), and c) treating the mixture from stage b) with an absorbent in the presence of an organic solvent, wherein the adsorbent is a solid acidic adsorbent.

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14-03-2013 дата публикации

PROCESS FOR PREPARING ALKYLATED P-PHENYLENEDIAMINES

Номер: US20130066113A1
Принадлежит: Jiangsu Sinorgchem Technology Co., Ltd.

A process for preparing alkylated p-phenylenediamine having the steps of reacting aniline and nitrobenzene in presence of a complex base catalyst to obtain 4-aminodiphenylamine intermediates, hydrogenating the 4-aminodiphenylamine intermediates to 4-aminodiphenylamine in presence of a hydrogenation catalyst, and reductively alkylating the 4-aminodiphenylamine to alkylated p-phenylenediamine. 1. A process for preparing alkylated p-phenylenediamine , comprisingreacting aniline and nitrobenzene in presence of a complex base catalyst to obtain 4-aminodiphenylamine intermediates,hydrogenating the 4-aminodiphenylamine intermediates to 4-aminodiphenylamine in presence of a hydrogenation catalyst, andreductively alkylating the 4-aminodiphenylamine to alkylated p-phenylenediamine.2. The process of claim 1 , further comprisingseparating, recovering, and reusing excess aniline.3. The process of claim 1 , further comprisingseparating, recovering, and reusing the complex base catalyst.4. The process of claim 1 , further comprisingrecovering and reusing the hydrogenation catalyst.5. The process of claim 1 , wherein the complex base catalyst comprises a tetraalkyl ammonium hydroxide and a tetraalkyl ammonium salt.6. The process of claim 1 , wherein the hydrogenation catalyst is a powdery catalyst comprising nickel claim 1 , aluminum claim 1 , and a component A that is selected from the group consisting of Fe claim 1 , Cu claim 1 , Co claim 1 , Mn claim 1 , Cr claim 1 , Mo claim 1 , B claim 1 , P claim 1 , and a mixture thereof.7. The process of claim 1 , further comprisingrefining the 4-aminodiphenylamine before the reductive alkylation step.8. A process for preparing alkylated p-phenylenediamine claim 1 , comprisingcontinuously feeding and reacting nitrobenzene, aniline and a complex base catalyst to form a condensation liquid containing 4-nitrodiphenylamine, 4-nitrosodiphenylamine, salts of 4-nitrodiphenylamine, salts of 4-nitrosodiphenylamine, or a mixture thereof,continuously ...

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21-03-2013 дата публикации

Supported metal catalysts

Номер: US20130072722A1
Принадлежит: JOHNSON MATTHEY PLC

The present invention relates to supported metal catalysts, wherein the catalysts are modified by at least one amine, a method for the preparation thereof and hydrogenation processes utilising the supported metal catalysts.

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28-03-2013 дата публикации

Process for preparing eddn and edmn

Номер: US20130079492A1
Принадлежит: BASF SE

A process for preparing EDDN and/or EDMN by conversion of FA, HCN and EDA, the reaction being effected in the presence of water, and, after the conversion, water being depleted from the reaction mixture in a distillation column, which comprises performing the distillation in the presence of an organic solvent which has a boiling point between water and EDDN and/or EDMN at the distillation pressure existing in the column or which forms a low-boiling azeotrope with water.

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28-03-2013 дата публикации

METHOD FOR PRODUCING beta-AMINOCARBONYL COMPOUND

Номер: US20130079543A1

An optically active β-aminocarbonyl compound is obtained by a Mannich reaction between an aldimine in which: nitrogen is protected and a malonic acid diester, in the presence of optically active BINOL and dialkyl magnesium (in which two alkyl groups are the same or different) in an amount 1 to 2 molar times the amount of the BINOL. 1. A method for producing a β-aminocarbonyl compound comprising carrying out a Mannich reaction between an aldimine in which nitrogen is protected and a malonic acid diester , in the presence of optically active BINOL and dialkyl magnesium (in which two alkyl groups are the same or different) in an amount 1 to 2 molar times the amount of the BINOL , to obtain an optically active β-aminocarbonyl compound.2. The method for producing a β-aminocarbonyl compound according to claim 1 , wherein the aldimine is a compound represented by R—CH═NR(wherein Ris an aryl group or an ester group claim 1 , and Ris tert-butoxycarbonyl (Boc) claim 1 , benzyloxycarbonyl (Cbz) claim 1 , 2 claim 1 ,2 claim 1 ,2-trichloroethoxycarbonyl (Troc) claim 1 , a phenyl group claim 1 , a 2-methoxyphenyl group claim 1 , a 4-methoxyphenyl group claim 1 , or a naphthyl group).3. The method for producing a β-aminocarbonyl compound according to claim 1 , wherein the malonic acid diester is a compound represented by CHX(COR)(wherein X is a hydrogen atom or a halogen atom claim 1 , and Ris alkyl claim 1 , allyl claim 1 , benzyl claim 1 , or aryl).4. The method for producing a β-aminocarbonyl compound according to claim 1 , wherein the BINOL is used in an amount of 2.5 mole percent to 10 mole percent relative to the aldimine.5. The method for producing a β-aminocarbonyl compound according to claim 1 , wherein an aromatic solvent or a halogenated hydrocarbon solvent is used as a reaction solvent. The present invention relates to a method for producing a β-aminocarbonyl compound.Mannich reactions in which a carbonyl compound is added directly to an aldimine are one. Of the most ...

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28-03-2013 дата публикации

SOLID BASE CATALYST AND METHOD FOR MAKING AND USING THE SAME

Номер: US20130079560A1
Автор: CHEN Xinmin, Zhu Jianliang
Принадлежит: Jiangsu Sinorgchem Technology Co., Ltd.

A solid base catalyst having a carrier, an organic base, and an inorganic base. Both of the organic base and inorganic base are loaded on the carrier. The solid base catalyst is especially suitable for the synthesis of 4-Aminodiphenylamine (4-ADPA). 1. A solid base catalyst comprisingan organic base,an inorganic base; anda carrier,wherein the organic base is chemically bound to the carrier, and the inorganic base is adsorbed in the carrier.2. The solid base catalyst of claim 1 , wherein the organic base is methylamine claim 1 , ethylamine claim 1 , cyclohexylamine claim 1 , aniline claim 1 , phenyl diamine claim 1 , dodecyl trimethyl ammonium chloride claim 1 , trimethyl benzyl ammonium chloride claim 1 , tetramethyl ammonium chloride claim 1 , tetramethyl ammonium bromide claim 1 , tetramethyl ammonium hydroxide claim 1 , tetraethyl ammonium hydroxide claim 1 , tetrapropyl ammonium hydroxide claim 1 , tetrabutyl ammonium hydroxide claim 1 , tetramethyl ammonium hydroxide claim 1 , benzyl trimethyl ammonium hydroxide claim 1 , benzyl triethyl ammonium hydroxide claim 1 , 4-dimethylamino pyridine claim 1 , crown ether claim 1 , or a mixture thereof.3. The solid base catalyst of claim 1 , wherein the organic base is tetramethyl ammonium hydroxide or tetraethyl ammonium hydroxide.4. The solid base catalyst of wherein the inorganic base is potassium hydroxide claim 1 , sodium hydroxide claim 1 , calcium hydroxide claim 1 , cesium hydroxide claim 1 , aluminum hydroxide claim 1 , sodium methoxide claim 1 , sodium ethoxide claim 1 , potassium methoxide claim 1 , potassium ethoxide claim 1 , or a mixture thereof.5. The solid base catalyst of claim 1 , wherein the inorganic base is potassium hydroxide or sodium hydroxide.6. The solid base catalyst of claim 1 , wherein the carrier is alumina claim 1 , silica gel claim 1 , diatomite claim 1 , molecular sieve claim 1 , macroporous adsorption resin claim 1 , or a mixture thereof.7. The solid base catalyst of claim 6 , wherein ...

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04-04-2013 дата публикации

Unknown

Номер: US20130085286A1
Принадлежит: BASF SE

A process for preparing amines of the formula (II) 111-. (canceled)13. The process of claim 12 , wherein the nitriles are ethylenediaminediacetonitrile claim 12 , ethylenediaminemonoacetonitrile claim 12 , or iminodiacetonitrile.14. The process of claim 12 , wherein the hydrogenation is effected at a temperature in the range from 60 to 150° C.15. The process of claim 13 , wherein the hydrogenation is effected at a temperature in the range from 60 to 150° C.16. The process of claim 12 , wherein the pressure existing in the hydrogenation is in the range from 170 to 240 bar.17. The process of claim 15 , wherein the pressure existing in the hydrogenation is in the range from 170 to 240 bar.18. The process of claim 12 , wherein the hydrogenation is effected in the presence of an organic solvent.19. The process of claim 17 , wherein the hydrogenation is effected in the presence of an organic solvent.20. The process of claim 12 , wherein the hydrogenation is effected in the presence of tetrhydrofuran.21. The process of claim 12 , wherein the hydrogenation is effected in the presence of tetrahydrofuran and toluene.22. The process of claim 19 , wherein the hydrogenation is effected in the presence of tetrhydrofuran.23. The process of claim 19 , wherein the hydrogenation is effected in the presence of tetrahydrofuran and toluene.24. The process of claim 12 , wherein the nitrile of formula (I) is treated before the hydrogenation with an adsorbent in the presence of an organic solvent.25. The process of claim 24 , wherein the adsorbent is a solid acidic adsorbent.26. The process of claim 12 , wherein the space velocity is 0.25·10to 5·10kg of nitrile of formula (I) per mof catalyst surface area and hour.27. A process for preparing an epoxy resin claim 12 , amide claim 12 , or polyamide claim 12 , which comprises in a first stage preparing triethylenetetramine or diethylenetriamine by the process of claim 12 , and in a second stage converting the triethylenetetramine or ...

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11-04-2013 дата публикации

SYNTHESIS SYSTEM, RUBBER CHEMICAL SUBSTANCE FOR TIRES, SYNTHETIC RUBBER FOR TIRES, AND PNEUMATIC TIRE

Номер: US20130090445A1
Принадлежит: SUMITOMO RUBBER INDUSTRIES, LTD.

The present invention provides a synthesis system that can synthesize aniline and/or styrene efficiently, a synthesis system that can synthesize butadiene (1,3-butadiene) efficiently, a rubber chemical for a tire which is synthesized from the aniline obtained by the synthesis system, a synthetic rubber for a tire which is synthesized from the styrene and/or butadiene obtained by the synthesis systems, and a pneumatic tire produced using the rubber chemical for a tire and/or the synthetic rubber for a tire. The present invention relates to a synthesis system for synthesizing aniline and/or styrene from an alcohol having two or more carbon atoms via an aromatic compound. 1. A synthesis system for synthesizing at least one of aniline and styrene from an alcohol having two or more carbon atoms via an aromatic compound.2. The synthesis system according to claim 1 ,wherein the alcohol is ethanol.3. The synthesis system according to claim 2 ,wherein the ethanol is bioethanol.4. The synthesis system according to claim 1 ,wherein the aromatic compound is benzene.5. The synthesis system according to claim 4 ,wherein the benzene is synthesized via at least one of toluene and xylene.6. The synthesis system according to claim 1 ,wherein the aromatic compound is synthesized via an alkene.7. The synthesis system according to claim 1 ,wherein the synthesis system is adapted to subject the alcohol to catalysis by a solid acid catalyst.8. The synthesis system according to claim 7 ,wherein the solid acid catalyst is at least one selected from the group consisting of zeolites, alumina, and titanium compounds.9. The synthesis system according to claim 7 ,wherein the solid acid catalyst is an MFI-type zeolite.10. The synthesis system according to claim 1 ,wherein the synthesis system is adapted to subject the alcohol to catalysis by a solid acid catalyst to give a reaction product, andcirculate the reaction product so that it is further subjected to catalysis by the solid acid catalyst. ...

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11-04-2013 дата публикации

PROCESS FOR PREPARING EDDN AND/OR EDMN BY CONVERSION OF FACH AND EDA

Номер: US20130090452A1
Принадлежит: BASF SE

A process for reacting formaldehyde cyanohydrin (FACH) with ethylenediamine (EDA) in a reactor with limited backmixing at a temperature in the range from 20 to 120° C., wherein the residence time in the reactor is 300 seconds or less. 116-. (canceled)17. A process for reacting formaldehyde cyanohydrin (FACH) with ethylenediamine (EDA) in a reactor with limited backmixing at a temperature in the range from 20 to 120° C. , wherein the residence time in the reactor is 300 seconds or less.18. The process according to claim 17 , wherein the residence time in the reactor is less than 60 seconds.19. The process according to claim 17 , wherein the reactor is a tubular reactor.20. The process according to claim 17 , wherein the inlet temperature of the reactants into the reactor is in the range from 10 to 50° C.21. The process according to claim 17 , wherein the reaction is effected in the presence of one or more organic solvents.22. The process according to claim 17 , wherein the conversion is performed in the presence of water.23. The process according to claim 22 , wherein at least a portion of the water is mixed with EDA before entry into the reactor and the resulting mixture is then cooled.24. The process according to claim 17 , wherein the reaction mixture is cooled after it leaves the reactor.25. The process according to claim 17 , wherein the reaction mixture is cooled by flash evaporation.26. The process according to claim 25 , wherein the pressure in the flash evaporation step is less than 300 mbar.27. The process according to at least one of claim 21 , wherein the organic solvent has a miscibility gap with water.28. The process according to claim 27 , wherein the organic solvent which has a miscibility gap with water is toluene.29. The process according to at least one of claim 17 , wherein the tubular reactor is additionally cooled by means of a cooling jacket.Ethylenediamine (EDA)Ethylenediamine-formaldehyde bisadduct (EDFA)Ethylenediamine-formaldehyde ...

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11-04-2013 дата публикации

Process for preparing TETA and DETA

Номер: US20130090453A1
Принадлежит: BASF SE

A process for preparing TETA and/or DETA by hydrogenating EDDN and/or EDMN with hydrogen in the presence of a catalyst, which comprises preparing EDDN and/or EDMN from FA, HCN and EDA in the presence of toluene as a solvent and performing the hydrogenation in suspension mode in the presence of THF. 16-. (canceled)7. A process for preparing triethylenetetramine (TETA) and/or diethylenetriamine (DETA) by hydrogenating ethylenediaminediacetonitrile (EDDN) and/or Ethylenediaminemonoacetonitrile (EDMN) with hydrogen in the presence of a catalyst , which comprises preparing EDDN and/or EDMN from formaldehyde (FA) , hydrogen cyanide (HCN) and ethylenediamine (EDA) in the presence of toluene as a solvent and performing the hydrogenation in suspension mode in the presence of tetrahydrofuran.8. The process of claim 7 , wherein HCN and EDA are first converted to formaldehyde cyanohydrin claim 7 , which is subsequently reacted with EDA.9. The process of claim 7 , wherein EDDN is obtained by reacting an ethylenediamine-formaldehyde adduct (EDFA) claim 7 , or EDMN by reacting an ethylenediamine-monoformaldehyde adduct (EDMFA) claim 7 , with HCN claim 7 , EDFA or EDMFA being obtained by reacting EDA with FA.10. The process of claim 7 , wherein the output from the EDDN or EDMN preparation is treated with a solid acidic adsorbent in the presence of tetrahydrofuran.11. The process of claim 7 , wherein the reaction output from the hydrogenation which is obtained in the reaction of EDDN or EDMN with hydrogen in the presence of tetrahydrofuran and a catalyst and which comprises TETA or DETA and water claim 7 , with or without organic compounds having higher and lower boiling points than TETA or DETA claim 7 , is separated claim 7 , wherein{'b': '1', 'i) the reaction output after removal of hydrogen is supplied to a distillation column DK in which a tetrahydrofuran/water azeotrope is removed via the top and which may also comprise further organic compounds having a lower boiling point ...

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11-04-2013 дата публикации

GOLD COMPLEXES FOR USE IN THE TREATMENT OF CANCER

Номер: US20130090472A1
Принадлежит: UNIVERSITY OF KWAZULU-NATAL

The invention provides compounds of the Formula (I), in which W is independently selected from W, W, W, W, W, or W represents a pair of substituents independently selected from H, alkyl, aryl or amide in which the amide is optionally part of a linking chain, and the Z—Zbonds (n=4-17; n′=n+1) are optionally of any whole or partial bond order, Y is Yor Y represents a pair of substituents independently selected from H, C--Calkyl, Zor Zaryl, or Y is optionally a bridging structure that may comprise one or more C--Camide, C--Cether, or C--Cester groups, R-Rare independently selected from no substituent, a lone pair of electrons, H, halogen, C-Caryl, C- C-alkyl, amine, C--Calkylamine, C--Camide, nitro, cyano, carboxyl, C--Cester, phosphane, thiol, C--Cthioether, OR′, and suitable pairs of adjacent R groups (R-R) may optionally together form part of a Cor Caryl ring, a Zor Zring, R′ is independently selected from H, C--Calkyl, Zor Zaryl, C--Cester, poly(—CO—), amine, and C--Calkylamine, Z-Zare independently selected from C, N, P, O, and S, and X is a pharmaceutically acceptable anion, for the treatment of cancer. 2. The compound of claim 1 , in which the anion is selected from halide claim 1 , hexafluorophosphate claim 1 , nitrate claim 1 , and triflate.3. The compound of claim 1 , in which Y represents two hydrogen atoms or Y.4. The compound of claim 3 , in which Y is Yand Zand Zare N.5. The compound of claim 4 , in which Z-Zare C.6. The compound of claim 1 , in which R-Rare selected from H claim 1 , C-Calkyl claim 1 , O—C-Calkyl claim 1 , hydroxyl and halogen.7. The compound of claim 6 , in which C-Calkyl is methyl claim 6 , O—C-Calkyl is O-ethyl claim 6 , and halogen is chlorine.8. The compound of claim 1 , in which W is selected from W claim 1 , W claim 1 , WWor W.9. The compound of claim 8 , in which R-Rare selected from H claim 8 , C-Calkyl claim 8 , O—C-Calkyl and halogen.10. The compound of claim 9 , in which C-Calkyl is methyl claim 9 , O—C-Calkyl is O-ethyl and ...

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18-04-2013 дата публикации

Process for conversion of isobutylene to tertiary butylamine

Номер: US20130096349A1
Принадлежит: Individual

The invention discloses an improved process for the conversion of isobutylene to tertiary butylamine with conversion up to 50% at pressure lower than 40 bar.

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18-04-2013 дата публикации

Method to Recover Organic Tertiary Amines from Waste Sulfuric Acid

Номер: US20130096350A1

The present invention describes a method to recover organic tertiary amines from waste sulfuric acid comprising the following steps: 1. Method to recover organic tertiary amines from waste sulfuric acid comprising the following steps: 'ii) ammonia in an amount sufficient to obtain a pH of 9.5 or higher and', 'a) reacting i) waste sulfuric acid comprising organic tertiary amines with'}b) separating the organic tertiary amines from the reaction mixture obtained in step a) wherein during the separation the pH of the reaction mixture is adjusted to a pH of 9.5 or higher.2. Method according to wherein the organic tertiary amine is separated from the reaction mixture obtained in step a) in a distillation column.3. Method according to wherein during the distillation ammonia is added to the distillation column.4. Method according to wherein during the distillation ammonia is added to the distillation column in a counter flow to the reaction mixture obtained in step a).5. Method according to wherein during the distillation the reaction mixture obtained in step a) is continuously fed to the upper part of a distillation column and the ammonia is continuously fed to the lower part or the middle part of the distillation column.6. Method according to wherein the ammonia feed to the distillation column is positioned such that the aqueous solution which is essentially free of organic tertiary amine and which comprises the ammonium sulfate in the lower part of the column has a pH ranging from 5 to 7.7. Method according to wherein the organic tertiary amine is separated fro the reaction mixture by extraction with an organic liquid claim 1 , preferably a liquid hydrocarbon claim 1 , more preferably an aliphatic liquid hydrocarbon comprising at least 6 carbon atoms claim 1 , especially octane.8. Method according to wherein the pH in step a) and/or step b) ranges from 9.8 to 12.9. Method according to wherein the organic tertiary amine is triethylamine.10. Method according to wherein the ...

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25-04-2013 дата публикации

TRANSITION METAL-CATALYZED PROCESSES FOR THE PREPARATION OF N-ALLYL COMPOUNDS AND USE THEREOF

Номер: US20130102780A1
Принадлежит: Rhodes Technologies

The present disclosure provides processes for the N-dealkylation of tertiary amines and the use of transition metal catalysts to prepare tertiary N-allyl amine derivatives and secondary amine derivatives thereof. The tertiary amines can be alkaloids and, more particularly, the tertiary amines can be opioids. In specific embodiments, the present disclosure provides methods for use in processes for the synthesis of naloxone and naltrexone from oripavine. 3. The method of claim 1 , wherein the transition metal catalyst comprises a transition metal selected from the group consisting of Pd[0] claim 1 , Pd[II] claim 1 , Ni[0] claim 1 , Ni[II] claim 1 , Mo[0] claim 1 , Ru[II] claim 1 , Rh[I] claim 1 , and combinations of two or more thereof.4. The method of claim 3 , wherein the transition metal catalyst is selected from the group consisting of Pd(PPh) claim 3 , Pd(PhP(CH)PPh) claim 3 , Ni(PPh) claim 3 , Ni(PhP(CH)PPh) claim 3 , ((pentamethylcyclopentadienyl)RuCl) claim 3 , [Pd(DBA)]/PPh claim 3 , [Pd(OAc)]/PPh claim 3 , [Ni(COD)]/PPh claim 3 , NiCl/PPh claim 3 , Ni[P(OEt)] claim 3 , [Mo(CO)-DPPE] claim 3 , RhH(PPh)-P(n-Bu) claim 3 , and combinations of two or more thereof.6. The method of claim 5 , wherein the solvent is selected from the group consisting of ether solvents claim 5 , acetonitrile claim 5 , benzene claim 5 , N claim 5 ,N-dimethylformamide claim 5 , dimethyl sulfoxide claim 5 , N claim 5 ,N-dimethylpropionamide claim 5 , 1 claim 5 ,3-dimethyl-3 claim 5 ,4 claim 5 ,5 claim 5 ,6-tetrahydro-2(1H)-pyrimidinone claim 5 , 1 claim 5 ,3-dimethyl-2-imidazolidinone claim 5 , 1 claim 5 ,2-dimethoxyethane claim 5 , N claim 5 ,N-dimethylacetamide claim 5 , N-methylpyrrolidinone claim 5 , ethyl acetate claim 5 , ethyl formate claim 5 , ethyl-methyl ketone claim 5 , iso-butylmethylketone claim 5 , formamide claim 5 , hexamethylphosphoramide claim 5 , methyl acetate claim 5 , N-methylacetamide claim 5 , N-methylformamide claim 5 , nitrobenzene claim 5 , nitromethane claim 5 ...

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16-05-2013 дата публикации

Adhesive Compositions for Bonding Composites

Номер: US20130123513A1
Принадлежит: GEORGIA-PACIFIC CHEMICALS LLC

The present invention relates to a non-thermosetting composition made by reacting epichlorohydrin and a primary amine, to the use of that composition for making thermosetting (curable) adhesives suitable for bonding composites, to a method of preparing composites using the thermosetting (curable) adhesives, and to the related composites bonded with the thermosetting (curable) adhesives. 1. A non-thermosetting, reaction product of (a) epichlorohydrin and (b) an amine selected from the group consisting of ammonia, a primary amine and mixtures thereof, wherein the reaction product is produced by reacting the epichlorohydrin and the amine in a ratio of 0.40 to 0.92 moles of epichlorohydrin per atom equivalent of amine hydrogen and wherein the epi-amine reaction product is produced by reacting in a serial fashion separate portions of the epichlorohydrin and separate portions of the amine at a temperature of not greater than 60° C. This application is a divisional of co-pending U.S. patent application Ser. No. 12/718,391, filed on Mar. 5, 2010, which claims the benefit of U.S. Provisional Application No. 61/158,013 filed Mar. 6, 2009, each of which is hereby incorporated by reference in its entirety.The present invention is directed to a non-thermosetting composition made by reacting epichlorohydrin and an amine, to the use of that composition for making thermosetting (curable) adhesives, particularly adhesives suitable for bonding composites, to a method of preparing composites, particularly wood composites using the thermosetting (curable) adhesives, and to the related composites bonded with the cured thermosetting (curable) adhesives.A variety of composite materials are made by bonding into a unitary product a primary constituent, often a structural or reinforcement component, using a bonding agent or matrix material, such as an adhesive resin. Composites include engineered wood products (wood-adhesive composite products), insulation products and the like.Wood-adhesive ...

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16-05-2013 дата публикации

METHOD FOR PRODUCING 2,5-DIAMINOTOLUENE

Номер: US20130123540A1
Автор: Aeby Johann, Goettel Otto
Принадлежит: ALFA PARF GROUP S.P.A.

The invention relates to a method for producing 2,5-diaminotoluene by catalytic hydrogenation in an aprotic-non-polar solvent or in a mixture made of two or more aprotic-nonpolar solvents with hydrogen in the presence of a catalyst or a mixture of two or more catalysts. The invention further relates to crystalline 2,5-diaminotoluene having characteristic crystal modification. As compared to conventional forms of administration common in industry, this is characterised in that it is largely insensitive to air oxidation. 1. A method for producing 2 ,5-diaminotoluene , comprising hydrogenating 2-methyl-4-nitroaniline in an aprotic nonpolar solvent or in a mixture made of two or more aprotic nonpolar solvents with hydrogen in the presence of a catalyst or a mixture made of two or more catalysts , thereby forming a solution containing 2 ,5-diaminotoluene and an aprotic nonpolar solvent or a mixture made of two or more aprotic nonpolar solvents.2. The method according to claim 1 , wherein the aprotic nonpolar solvent or the mixture made of two or more aprotic nonpolar solvents has a dielectric constant ∈in the range of 2.3 to 6.1.3. The method according to claim 1 , wherein the catalyst is a solid catalyst or the mixture made of two or more catalysts is a mixture containing at least one solid catalyst.4. The method according to claim 1 , wherein the catalyst is a palladium/activated carbon catalyst or the mixture made of two or more catalysts is a mixture containing at least one palladium/activated carbon catalyst.5. The method according to claim 1 , wherein the 2-methyl-4-nitroaniline is hydrogenated in a temperature range of 0° C. to 150° C.6. The method according to claim 1 , wherein the 2-methyl-4-nitroaniline is hydrogenated at a hydrogen overpressure in the range of 0 to 5 MPa.7. The method according to claim 1 , wherein at least one of the following steps is carried out after the hydrogenation:separating the catalyst or the mixture made of two or more catalysts ...

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16-05-2013 дата публикации

METHOD OF PREPARING 3,3,5,5-TETRAMETHYLCYCLOHEXANONE

Номер: US20130123541A1
Принадлежит: Merz Pharma GmbH & Co. KGaA

Method of preparing 3,3,5,5-tetramethylcyclohexanone comprising step (i): (i) converting isophorone to 3,3,5,5-tetramethylcyclohexanone in the presence of methylmagnesium chloride. The thus prepared 3,3,5,5-tetramethylcyclohexanone may be employed in a method of preparing 1-amino-1,3,3,5,5-pentamethylcyclohexane (Neramexane) or a pharmaceutically acceptable salt thereof. 116.-. (canceled)17. A method of preparing 3 ,3 ,5 ,5-tetramethylcyclohexanone comprising step (i):(i) converting isophorone to 3,3,5,5-tetramethylcyclohexanone in the presence of methylmagnesium chloride.18. The method according to claim 17 , wherein step (i) is performed in the presence of a copper compound.19. The method according to claim 18 , wherein the copper compound is a copper(I) halide.20. The method according to claim 19 , wherein the copper(I) halide is copper(I) iodide.21. The method according to claim 17 , wherein step (i) performed in the presence of a lithium compound.22. The method according to claim 21 , wherein the lithium compound is a lithium halide claim 21 ,23. The method according to claim 22 , wherein the lithium halide is lithium chloride.24. The method according to claim 22 , wherein the molar ratio of copper(I) halide to lithium halide is in the range of from 1:1.5 to 1:2.5.25. The method according to claim 17 , wherein step (i) is performed in a solvent comprising an ether.26. The method according to claim 25 , wherein the ether is tetrahydrofuran.27. The method according to claim 17 , wherein in step (i) isophorone is converted to 3 claim 17 ,3 claim 17 ,5 claim 17 ,5-tetramethylcyclohexanone in the presence of methylmagnesium chloride claim 17 , copper(I) iodide and lithium chloride in tetrahydrofuran.28. The method according to claim 27 , wherein a solution comprising methylmagnesium chloride in tetrahydrofuran is added to a solution comprising isophorone claim 27 , copper(I) iodide and lithium chloride.29. A method of preparing 1-amino-1 claim 27 ,3 claim 27 ,3 ...

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23-05-2013 дата публикации

Production of renewable aromatic compounds

Номер: US20130130345A1
Принадлежит: JNF BIOCHEMICALS LLC

The invention provides a process for producing a variety renewable aromatic compounds such as benzene, toluene, xylenes, and cumene, as well as compounds derived from these including, for example, aniline, benzoic acid, cresol, cyclohexane, cyclohexanone, phenol and bisphenol A, toluene di-isocyanate, isophthalic acid, phthalic anhydride, terephthalic acid and dimethyl terephthalate. The invention also provides for renewable forms of these aromatic compounds.

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23-05-2013 дата публикации

Process for Preparing Ethylamines and Monoisopropylamine (MIPA)

Номер: US20130131385A1
Принадлежит: BASF SE

A process for preparing ethylamines and monoisopropylamine (MIPA), in which bioethanol is reacted with ammonia in the presence of hydrogen and of a heterogeneous catalyst to give ethylamines, said bioethanol having a content of sulfur and/or sulfur compounds of ≧0.1 ppm by weight (calculated S), and then isopropanol is reacted with ammonia in the presence of the same catalyst and in the presence of hydrogen to give MIPA. 124.-. (canceled)25. A process for preparing ethylamines and monoisopropylamine (MIPA) , which comprises reacting bioethanol with ammonia in the presence of hydrogen and of a heterogeneous catalyst to give ethylamines , said bioethanol having a content of sulfur and/or sulfur compounds of ≧0.1 ppm by weight (calculated S) , and then reacting isopropanol with ammonia in the presence of the same catalyst and in the presence of hydrogen to give MIPA.26. The process according to claim 25 , wherein the sulfur content of the catalyst at the end of the period over which the reaction of bioethanol with ammonia is performed is <700 ppm by weight.27. The process according to claim 25 , wherein the reactions are performed in the presence of a heterogeneous copper and/or nickel and/or cobalt catalyst.28. The process according to claim 25 , wherein the reactions are performed in the presence of a heterogeneous catalyst having a nickel content of more than 90% by weight claim 25 , based on any and all metals of group VIII of the Periodic Table present.29. The process according to claim 25 , wherein the reactions are performed in the presence of a heterogeneous catalyst having a cobalt content of more than 90% by weight claim 25 , based on any and all metals of group VIII of the Periodic Table present.30. The process according to claim 25 , wherein the reactions are performed in the presence of a heterogeneous copper and nickel catalyst.31. The process according to claim 25 , wherein the reactions are performed in the presence of a heterogeneous copper and nickel ...

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30-05-2013 дата публикации

Novel method of preparing secondary amine compound using microflow reactor

Номер: US20130137900A1

Disclosed is a novel method of preparing a secondary amine compound using a microflow reactor. According to the method, a primary amine compound and a halide compound are allowed to react with each other in the microflow reactor, such that the production of a tertiary amine compound or an ammonium salt is minimized, whereby the secondary amine compound is efficiently prepared.

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30-05-2013 дата публикации

SYNTHESIS OF POLYALKYLENEPOLYAMINES HAVING A LOW COLOR INDEX BY HOMOGENEOUSLY CATALYZED ALCOHOL AMINATION IN THE PRESENCE OF HYDROGEN

Номер: US20130137901A1
Принадлежит:

Process for the preparation of polyalkylenepolyamines by homogeneously catalyzed alcohol amination, in which aliphatic amino alcohols are reacted with one another or aliphatic diamines or polyamines are reacted with aliphatic diols or polyols with the elimination of water in the presence of a homogeneous catalyst and in the presence of hydrogen gas. Polyalkylenepolyamines obtainable by such processes and polyalkylenepolyamines comprising hydroxy groups, secondary amines or tertiary amines. Uses of such polyalkylenepolyamines as adhesion promoters for printing inks, adhesion promoters in composite films, cohesion promoters for adhesives, crosslinkers/curing agents for resins, primers for paints, wet-adhesion promoters for emulsion paints, complexing agents and flocculating agents, penetration assistants in wood preservation, corrosion inhibitors, immobilizing agents for proteins and enzymes. 1. A process for the preparation of polyalkylenepolyamines by homogeneously catalyzed alcohol amination , in which(i) aliphatic amino alcohols are reacted with one another or(ii) aliphatic diamines or polyamines are reacted with aliphatic diols or polyols with the elimination of water in the presence of a homogeneous catalyst and in the presence of hydrogen gas.2. The process according to claim 1 , wherein the reaction is carried out at a partial pressure of the hydrogen gas of from 0.1 to 25 MPa.3. The process according to or claim 1 , wherein the hydrogen gas engages chemically in the catalyzed alcohol amination claim 1 , thereby reducing the formation of coloring components.4. The process according to to claim 1 , wherein the catalyst is a transition metal complex catalyst.5. The process according to to claim 1 , wherein the catalyst comprises ruthenium or iridium.6. The process according to to claim 1 , wherein the catalyst comprises a nitrogen-heterocyclic carbene ligand.7. The process according to claim 6 , wherein the catalyst comprises a carbene ligand from the group ...

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06-06-2013 дата публикации

PROCESSES FOR PRODUCING DIAMINOBUTANE (DAB), SUCCINIC DINITRILE (SDN) AND SUCCINAMIDE (DAM)

Номер: US20130144028A1
Принадлежит:

Processes include providing a clarified diammonium succinate (DAS)- or monoammonium succinate (MAS)- containing fermentation broth; distilling the broth of an overhead that includes water and ammonia, and a liquid bottoms that includes SA, and at least about 20 wt % water; cooling the bottoms to a temperature sufficient to cause the bottoms to separate into a liquid portion in contact with a solid portion that is substantially pure SA; separating the solid portion from the liquid portion; and converting the solid portion to produce nitrogen containing compounds such as diamino butane (DAB), succinic dinitrile (SDN), succinic amino nitrile (SAN) or succinamide (DAM) and downstream products. 1. A process for making nitrogen containing compounds of SA comprising:(a) providing a clarified DAS-containing fermentation broth;(b) distilling the broth under super atmospheric pressure at a temperature of >100° C. to about 250° C. to form an overhead that comprises water and ammonia, and a liquid bottoms that comprises SA, and at least about 20 wt % water;(c) cooling and/or evaporating the bottoms to attain a temperature and composition sufficient to cause the bottoms to separate into a liquid portion and a solid portion that is substantially pure SA;(d) separating the solid portion from the liquid portion;(e) (1) contacting at least as part of the solid portion with hydrogen and an ammonia source in the presence of at least one hydrogenation catalyst to produce DAB, (2) dehydrating at least part of the solid portion to produce SDN or (3) dehydrating at least part of the solid portion to produce DAM; and(f) recovering the DAB, SDN or DAM.2. A process for making nitrogen containing compounds of SA comprising:(a) providing a clarified DAS-containing fermentation broth;(b) adding an ammonia separating and/or water azeotroping solvent to the broth;(c) distilling the broth at a temperature and pressure sufficient to form an overhead that comprises water and ammonia, and a liquid ...

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13-06-2013 дата публикации

NOVEL PROCESS FOR PREPARING PHENYLCYCLOPROPYLAMINE DERIVATIVES USING NOVEL INTERMEDIATES

Номер: US20130150577A1
Принадлежит: ACTAVIS GROUP PTC EHF

Provided herein is a novel process for the preparation of phenylcyclopropylamine derivatives, which are useful intermediates in the preparation of triazolo[4,5-d]pyrimidine compounds. Provided particularly herein is a novel, commercially viable and industrially advantageous process for the preparation of a substantially pure ticagrelor intermediate, trans-(1R,2S)-2-(3,4-difluorophenyl)-cyclopropylamine. The intermediate is useful for preparing ticagrelor, or a pharmaceutically acceptable salt thereof, in high yield and purity. 2. The process of claim 1 , wherein the halogen atom in the compounds of formulae II claim 1 , III claim 1 , IV claim 1 , V claim 1 , VI and VII is F; and wherein the leaving group ‘X’ in the compound of formula VIII is Cl.3. The process of claim 1 , wherein the R claim 1 , Rand Rin the compounds of formulae II claim 1 , III claim 1 , IV claim 1 , V claim 1 , VI and VII are H claim 1 , and wherein the Rand Rare F.4. The process of claim 1 , wherein the first solvent used in step-(a) is selected from the group consisting of an aliphatic or alicyclic hydrocarbon claim 1 , a chlorinated aliphatic or aromatic hydrocarbon claim 1 , an aromatic mono or dinitro hydrocarbon claim 1 , and mixtures thereof; wherein the second solvent used in step-(b) is selected from the group consisting of a ketone claim 1 , an aliphatic amide claim 1 , a nitrile claim 1 , a hydrocarbon claim 1 , a cyclic ether claim 1 , an aliphatic ether claim 1 , a polar aprotic solvent claim 1 , and mixtures thereof; wherein the third solvent used in step-(c) is selected from the group consisting of a hydrocarbon claim 1 , a cyclic ether claim 1 , an aliphatic ether claim 1 , a chlorinated hydrocarbon claim 1 , and mixtures thereof; wherein the fourth solvent used in step-(d) is selected from the group consisting of a hydrocarbon claim 1 , cyclic ethers claim 1 , an ether claim 1 , an ester claim 1 , a nitrile claim 1 , an aliphatic amide claim 1 , a chlorinated hydrocarbon claim 1 ...

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13-06-2013 дата публикации

Method for Producing Primary Aliphatic Amines from Aldehydes

Номер: US20130150624A1
Принадлежит: OXEA GMBH

A continuous process for producing primary aliphatic amines having 9 to 18 carbon atoms by reaction of corresponding aliphatic aldehydes with ammonia and hydrogen in the presence of a hydrogenation catalyst in the liquid phase, characterized in that the reaction is carried out solventlessly at a molar ratio of aliphatic aldehyde:ammonia of at least 1:30, at a temperature of 100 to 200° C. and at a pressure of 6 to 11 MPa. 1. Continuous process for producing primary aliphatic amines having 9 to 18 carbon atoms by reaction of corresponding aliphatic aldehydes with ammonia and hydrogen in the presence of a hydrogenation catalyst in the liquid phase , characterized in that the reaction is carried out solventlessly at a molar ratio of aliphatic aldehyde:ammonia of at least 1:30 , at a temperature of 100 to 200° C. and at a pressure of 6 to 11 MPa.2. Process according to claim 1 , characterized in that the molar ratio of aliphatic aldehyde:ammonia is at least 1:35.3. Process according to claim 1 , characterized in that the reaction is carried out at a temperature of 100 to 170° C.4. Process according to claim 3 , characterized in that the reaction is carried out at a temperature of 120 to 150° C.5. Process according to claim 1 , characterized in that the reaction is carried out at a pressure of 7 to 9 MPa.6. Process according to claim 1 , characterized in that the aliphatic aldehydes to be reacted contain 9 to 15 carbon atoms in the molecule.7. Process according to claim 1 , characterized in that the hydrogenation catalyst contains at least nickel claim 1 , cobalt claim 1 , platinum claim 1 , palladium claim 1 , iron claim 1 , rhodium or copper.8. Process according to claim 1 , characterized in that the hydrogenation catalyst contains a support material.9. Process according to claim 1 , characterized in that the hydrogenation catalyst contains oxides of calcium claim 1 , of barium claim 1 , of zinc claim 1 , of aluminium claim 1 , of zirconium claim 1 , of chromium claim ...

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20-06-2013 дата публикации

RUTHENIUM-DIAMINE COMPLEXES AND METHOD FOR PRODUCING OPTICALLY ACTIVE COMPOUNDS

Номер: US20130158276A1
Принадлежит: TAKASAGO INTERNATIONAL CORPORATION

Provided is a catalyst for asymmetric reduction, which can be produced by a convenient and safe production method, has a strong catalytic activity, and has excellent stereoselectivity. The present invention relates to a ruthenium complex represented by the following formula (1): wherein Rrepresents an alkyl group or the like; Y represents a hydrogen atom; X represents a halogen atom or the like; j and k each represent 0 or 1; Rand Reach represent an alkyl group or the like; Rto Reach represent a hydrogen atom, an alkyl group or the like; Z represents oxygen or sulfur; nrepresents 1 or 2; and nrepresents an integer from 1 to 3, a method for producing the ruthenium complex, a catalyst for asymmetric reduction formed from the ruthenium complex, and methods for selectively producing an optically active alcohol and an optically active amine using the catalyst for asymmetric reduction. 4. A method for producing a reduction product by reducing an organic compound in the presence of the ruthenium complex as set forth in and a hydrogen donor.5. A method for producing an optically active alcohol claim 1 , the method comprising reducing a carbonyl group of a carbonyl compound in the presence of the ruthenium complex according to and a hydrogen donor.6. A method for producing an optically active amine claim 1 , the method comprising reducing an imino group of an imine compound in the presence of the ruthenium complex according to and a hydrogen donor.7. The method according to claim 4 , wherein the hydrogen donor is selected from formic acid claim 4 , a formic acid alkali metal salt claim 4 , and an alcohol having a hydrogen atom on the α-position carbon atom substituted with a hydroxyl group.8. The method according to claim 4 , wherein the hydrogen donor is hydrogen.9. A catalyst for reduction claim 4 , comprising the ruthenium complex according to .10. The catalyst according to claim 9 , wherein the catalyst is a catalyst for asymmetric reduction. The present invention ...

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20-06-2013 дата публикации

PROCESS FOR THE SYNTHESIS OF 1-AMINO-3-HALO-4,6-DINITROBENZENE

Номер: US20130158296A1
Принадлежит: E I DU PONT DE NEMOURS AND COMPANY

A process is provided for the preparation of 1-amino-3-halo-4,6-dinitrobenzene and related compounds by monoamination of dihalodinitrobenzenes by ammonia in the presence of solvent and water. Using glycol as a solvent for the dihalodinitrobenzene and feeding ammonia at a rate at which it is consumed allows for the synthesis of high purity product, such as 1-amino-3-chloro-4,6-dinitrobenzene, at high yields. 2. A process according to wherein each Z is Cl.3. A process according to wherein Z═Cl and R claim 2 , R claim 2 , R claim 2 , and Rare each H.4. A process according to wherein the solvent comprises an aliphatic dihydric alcohol.5. A process according to wherein the aliphatic dihydric alcohol is ethylene glycol.6. A process according to wherein the reaction mixture is prepared by contacting a suspension of a compound represented by Formula (III) in solvent and water with gaseous ammonia.7. A process according to wherein the reaction mixture is prepared by contacting a suspension of a compound represented by Formula (III) in solvent with an aqueous solution of ammonia.8. A process according to wherein the reaction mixture is prepared by contacting a compound represented by Formula (III) with a feed stream containing solvent claim 1 , water and NH.9. A process according to wherein the amount of water is between about 1 and about 5 times the amount of NH.10. A process according to wherein the compound represented by Formula (II) thereby produced is filtered and washed with solvent and then water.11. A process according to wherein the filtrate containing solvent is collected and distilled claim 10 , and the solvent is recovered and recycled to the reaction mixture.12. A process according to wherein the compound represented by Formula (II) thereby produced is slurried with water as a suspension and transferred to another reactor for further processing. This application claims priority under 35 U.S.C. §119(e) from, and claims the benefit of, U.S. Provisional Application ...

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27-06-2013 дата публикации

PROCESS FOR THE DIRECT AMINATION OF SECONDARY ALCOHOLS WITH AMMONIA TO GIVE PRIMARY AMINES

Номер: US20130165672A1
Принадлежит: EVONIK DEGUSSA GmbH

The invention relates to a process for preparing primary amines which comprises the process steps 1. A process for preparing a primary amine , the process comprising:i) providing a solution of a secondary alcohol in a fluid, nongaseous phase, free ammonia, at least one ammonia-releasing compound, or both,', 'and a homogeneous catalyst, and, 'ii) contacting the solution with'} 'wherein:', 'iii) optionally isolating the primary amine obtained in said contacting ii),'}a) a volume ratio of a liquid phase to a gas phase in said contacting ii) is greater than or equal to 0.25, orb) a molar ratio of the ammonia to hydroxyl groups in the secondary alcohol is at least 5:1, orboth a) and b).2. The process according to claim 1 , wherein the homogeneous catalyst isan alkali metal alkoxide, an aluminium alkoxide, a lanthanide alkoxide, an inorganic compound of noble metals,a monometallic or multimetallic, mononuclear or multinuclear coordination compound of at least one noble metal selected from the group consisting of ruthenium, iridium, rhodium, osmium, palladium, platinum and iron,or any mixture thereof.3. The process according to claim 1 ,whereinthe secondary alcohol comprises at least two secondary hydroxy groups.4. The process according to claim 1 ,whereinthe secondary alcohol comprises a cyclic or polycyclic carbon skeleton.5. The process according to claim 1 ,whereinthe secondary alcohol is selected from the group consisting of:2-dodecanol, cyclododecanol, 4-phenyl-2-butanol, isosorbide, isomannide, isoidite, polypropylene glycol, mannitol, sorbitol, galactitol and an alkyl glycoside.6. The process according to claim 1 ,whereinthe secondary alcohol is selected from the group consisting of an alpha-hydroxycarboxylic acid and an OH-modified, natural fatty acid.7. The process according to claim 1 ,wherein a liquid or supercritical ammonia, a solution of ammonium salts in a solvent, or both is used in said contacting ii).8. The process according to claim 1 ,whereinsaid ...

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27-06-2013 дата публикации

NOVEL PROCESSES FOR THE PREPARATION OF PHENYLCYCLOPROPYLAMINE DERIVATIVES AND USE THEREOF FOR PREPARING TICAGRELOR

Номер: US20130165696A1
Принадлежит: ACTAVIS GROUP PTC EHF

Provided herein are novel processes for the preparation of phenylcyclopropylamine derivatives, which are useful intermediates in the preparation of triazolo[4,5-d]pyrimidine compounds. Provided particularly herein are novel, commercially viable and industrially advantageous processes for the preparation of a substantially pure ticagrelor intermediate, trans-(1R,2S)-2-(3,4-difluorophenyl)-cyclopropylamine. Provided further herein are novel acid addition salts of trans-(1R,2S)-2-(3,4-difluorophenyl)-cyclopropylamine, and process for their preparation. The intermediate and its acid addition salts are useful for preparing ticagrelor, or a pharmaceutically acceptable salt thereof, in high yield and purity. 2. The process of claim 1 , wherein the halogen atom ‘X’ in the compound of formula VII is Cl or Br; and wherein the halogen atom in the compounds of formulae II claim 1 , III claim 1 , IV claim 1 , VI and VIII is F.3. The process of claim 1 , wherein the halogen atom ‘X’ in the compound of formula VII is Br; and wherein the R claim 1 , Rand Rin the compounds of formulae II claim 1 , III claim 1 , IV claim 1 , VI and VIII are H claim 1 , and wherein the Rand Rare F.4. The process of claim 1 , wherein the first solvent used in step-(a) is selected from the group consisting of an ester claim 1 , a nitrile claim 1 , a hydrocarbon claim 1 , a cyclic ether claim 1 , an aliphatic ether claim 1 , a polar aprotic solvent claim 1 , and mixtures thereof; wherein the second solvent used in step-(b) is selected from the group consisting of a ketone claim 1 , an ester claim 1 , a hydrocarbon claim 1 , a chlorinated hydrocarbon claim 1 , a cyclic ether claim 1 , an aliphatic ether claim 1 , and mixtures thereof; wherein the third solvent used in step-(c) is selected from the group consisting of water claim 1 , an alcohol claim 1 , a ketone claim 1 , a cyclic ether claim 1 , an aliphatic ether claim 1 , a hydrocarbon claim 1 , a chlorinated hydrocarbon claim 1 , a nitrile claim 1 , ...

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04-07-2013 дата публикации

PROCESSES FOR PRODUCING DIAMINOBUTANE (DAB), SUCCINIC DINITRILE (SDN) AND SUCCINAMIDE (DAM)

Номер: US20130172519A1
Принадлежит: BIOAMBER S.A.S.

Processes that make nitrogen-containing compounds include converting succinic acid (SA) or monoammonium succinate (MAS) derived from a diammonium succinate (DAS)- or MAS-containing fermentation broth to produce such compounds including diaminobutane (DAB), succinic dinitrile (SDN), succinic amino nitrile (SAN), succinamide (DAM), and related polymers. 1. A process for making nitrogen containing compounds , comprising:(a) providing a clarified DAS-containing fermentation broth;(b) distilling the broth to form an overhead that comprises water and ammonia, and a liquid bottoms that comprises MAS, at least some DAS, and at least about 20 wt % water;(c) cooling and/or evaporating the bottoms, and optionally adding an antisolvent to the bottoms, to attain a temperature and composition sufficient to cause the bottoms to separate into a DAS-containing liquid portion and a MAS-containing solid portion that is substantially free of DAS;(d) separating at least part of the solid portion from the liquid portion; (2) dehydrating at least a part of the solid portion to produce SDN; or', '(3) dehydrating at least a part of the solid portion to produce DAM; and, '(e) (1) contacting the solid portion with hydrogen and optionally an ammonia source in the presence of at least one hydrogenation catalyst to produce DAB; or'}(f) recovering the DAB, SDN or DAM.2. A process for making nitrogen containing compounds , comprising:(a) providing a clarified DAS-containing fermentation broth;(b) distilling the broth to form a first overhead that includes water and ammonia, and a first liquid bottoms that includes MAS, at least some DAS, and at least about 20 wt % water;(c) cooling and/or evaporating the bottoms, and optionally adding an antisolvent to the bottoms, to attain a temperature and composition sufficient to cause the bottoms to separate into a DAS-containing liquid portion and a MAS-containing solid portion that is substantially free of DAS;(d) separating the solid portion from the ...

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04-07-2013 дата публикации

Method for producing alcohol and/or amine from amide compound

Номер: US20130172619A1
Принадлежит: Takasago International Corp

Disclosed herein is a method for producing an alcohol and an amine from an amide under an atmosphere of hydrogen with the use of, as a catalyst, a ruthenium complex that is easily prepared, easy to handle, and relatively cheaply obtained. Specifically, the method is a method for producing an alcohol and/or an amine from an amide compound under an atmosphere of hydrogen with the use of as a catalyst, a ruthenium carbonyl complex represented by the following general formula (1): RuXY(CO)(L) (1) wherein X and Y may be the same or different from each other and each represents an anionic ligand and L represents a tridentate aminodiphosphine ligand containing two phosphino groups and a —NH— group.

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11-07-2013 дата публикации

High-speed mixing reactor and application thereof

Номер: US20130178596A1
Принадлежит: Yantai Wanhua Polyurethanes Co Ltd

Disclosed is a rapid mixing reactor, comprising a first feed-in passage housing, a reactor housing, a second feed-in passage, a hollow blade-wheel feed distributor, a rotation shaft, and a first feed distributor, wherein the first feed-in passage housing and the reactor housing are constructed coaxially and communicated with each other; the second feed-in passage, the hollow blade-wheel feed distributor and the rotation shaft each are fixed in connection with each other in the sequence along the central axis of the reactor; the hollow blade-wheel feed distributor is located within the reactor housing and rotates axially under the driving force of the rotation shaft; the second feed-in passage is connected with the hollow blade-wheel feed distributor; the first feed-in passage housing is set up with at least one first feed-in inlet therein; the reactor housing is set up with at least one reaction liquid outlet at its distal end; and the first feed distributor and the hollow blade-wheel feed distributor are provided with first feed-in jetting hole(s) and second feed-in jetting hole(s), respectively. The reactor is capable of effecting instantaneously rapid mixing of two streams of fluid under a massive capacity, and improving the yield and quality of the target product.

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11-07-2013 дата публикации

Processes for preparing 3-benzazepines

Номер: US20130178620A1
Принадлежит: Arena Pharmaceuticals Inc

The present invention provides processes and intermediates for the preparation of 3-benzazepines and salts thereof which can be useful as serotonin (5-HT) receptor agonists for the treatment of, for example, central nervous system disorders such as obesity.

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11-07-2013 дата публикации

PROCESS FOR CINACALCET HYDROCHLORIDE

Номер: US20130178654A1
Принадлежит: HETERO RESEARCH FOUNDATION

3-[3-(Trifluoromethyl)phenyl]propionaldehyde is a key intermediate for the preparation of cinacalcet hydrochloride. The present invention provides a novel process for the preparation of 3-[3-(trifluoromethyl)phenyl]propionaldehyde. The present invention also provides an improved process for preparation of cinacalcet hydrochloride in high yields. The present invention further provides a process for purification of cinacalcet hydrochloride. 2. The process according to claim 1 , wherein the R′ is methyl or ethyl.3. (canceled)4. The process according to claim 1 , wherein the solvent used in the process is selected from the group consisting of cyclohexane claim 1 , cyclohexene claim 1 , cycloheptane claim 1 , cyclopentane claim 1 , n-hexane claim 1 , n-heptane claim 1 , benzene claim 1 , toluene claim 1 , xylene claim 1 , dichloromethane claim 1 , chloromethane claim 1 , dichloroethane claim 1 , chloroform claim 1 , carbon tetrachloride claim 1 , chlorobenzene claim 1 , tetrahydrofuran claim 1 , diisopropyl ether claim 1 , tertrahydropyran claim 1 , 1 claim 1 ,4-dioxane claim 1 , methyl tert-butyl ether claim 1 , ethyl tert-butyl ether claim 1 , diethyl ether claim 1 , di-tert-butyl ether claim 1 , diglyme claim 1 , dimethoxyethane claim 1 , dimethoxymethane methoxyethane claim 1 , and mixtures thereof.5. The process according to claim 4 , wherein the solvent is selected from the group consisting of n-hexane claim 4 , cyclohexane claim 4 , toluene claim 4 , dichloromethane claim 4 , diisopropyl ether claim 4 , and tetrahydrofuran claim 4 , and mixtures thereof.6. The process according to claim 5 , wherein the the solvent is selected from the group consisting of n-hexane claim 5 , toluene claim 5 , dichloromethane claim 5 , tetrahydrofuran claim 5 , and mixtures thereof.7. The process according to claim 1 , wherein the reaction mass is maintained in the process below −50° C.8. The process according to claim 7 , wherein the reaction mass is maintained at about −70 to −85° ...

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11-07-2013 дата публикации

METHOD FOR SYNTHESIZING 3,5-DICHLOROANISOLE FROM 1,3,5-TRICHLOROBENZENE

Номер: US20130178655A1

The invention relates to a method for synthesizing 3,5-dichloroanisole from 1,3,5-trichlorobenzene, which comprises: 1. A method for synthesizing 3 ,5-dichloro-anisole from 1 ,3 ,5-trichlorobenzene , which comprises:a) reacting 1,3,5-trichloro-benzene and with a methanolate of an alkaline or alkaline-earth metal in a first solvent selected from the group consisting of dimethylsulfoxide, 1,1,3,3-tetramethylurea and mixtures thereof;b) precipitating the product resulting from step a) in a second solvent which is not included among the substances considered to be carcinogenic, mutagenic and/or toxic for reproduction by Regulation (EC) n° 1272/2008 of the European Parliament and of the Council of 16 Dec. 2008; thenc) recovering the precipitate thus-obtained in b).2. The method according to claim 1 , wherein the first solvent is dimethylsulfoxide.3. The method according to claim 1 , wherein the methanolate is selected from the group consisting of the methanolates of sodium claim 1 , potassium claim 1 , lithium claim 1 , magnesium claim 1 , calcium and barium.4. The method according to claim 3 , wherein the methanolate is sodium methanolate.5. The method according to claim 1 , wherein the methanolate is used to the proportion of 1 to 3 molar equivalents relative to the 1 claim 1 ,3 claim 1 ,5-trichlorobenzene.6. The method according to claim 1 , wherein a) is conducted at a temperature of 40 to 120° C.7. The method according to claim 1 , wherein a) is conducted for a time ranging from 15 minutes to 24 hours.8. The method according to claim 1 , wherein the second solvent is water.9. The method according to claim 1 , which additionally further comprises the washing of the precipitate recovered at c) with a third solvent which is not included among the substances considered to be carcinogenic claim 1 , mutagenic and/or toxic for reproduction by Regulation (EC) n° 1272/2008 of the European Parliament and of the Council of 16 Dec. 2008.10. The method according to claim 9 , ...

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11-07-2013 дата публикации

PROCESS FOR PREPARING SECONDARY AMINES IN THE LIQUID PHASE

Номер: US20130178656A1
Принадлежит:

The present application relates to a process for preparing secondary amines by aminating excess primary or secondary alcohols with primary amines in the liquid phase in the presence of copper-comprising catalysts. 2. The process according to claim 1 , excluding secondary amines of the formula I which are prepared from 1-dodecanol as the compound of the formula II with monomethylamine as the compound of the formula III.3. The process according to either of and claim 1 , wherein R claim 1 , Rand Rare each selected from the group of linear or branched aliphatic radicals having 1 to 4 carbon atoms.4. The process according to any of to claim 1 , wherein the catalyst precursor comprising copper oxides comprises 1 to 80% by weight of copper oxide.5. The process according to any of to claim 1 , wherein the catalyst support used comprises aluminum oxides claim 1 , silicon dioxide claim 1 , titanium dioxides claim 1 , zirconium dioxide claim 1 , lanthanum oxide claim 1 , molybdenum oxide claim 1 , tungsten oxide or mixtures of these oxides.6. The process according to any of to claim 1 , excluding hydrogenation catalysts which claim 1 , as well as copper claim 1 , also comprise tungsten and/or molybdenum as a metal and/or in the form of the oxides thereof.7. The process according to any of to claim 1 , wherein the catalyst support used is aluminum oxide and/or lanthanum oxide.8. The process according to to claim 1 , wherein the molar ratio of alcohol II to primary amine III is 1.5 to 15:1.9. The process according to claim 1 , wherein the hydrogenation output after step (ii) is subjected to the following workup steps:(a) distillatively removing alcohol II, optionally amine of the formula III and a portion of the water from the hydrogenation output,(b) extracting the hydrogenation output which has been obtained from (a) and freed of alcohol II, optionally amine of the formula III and a portion of the water with an aqueous alkali metal and/or alkaline earth metal hydroxide ...

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18-07-2013 дата публикации

Method for Allylating and Vinylating Aryl, Heteroaryl, Alkyl, and Alkene Halogenides Using Transition Metal Catalysis

Номер: US20130184485A1
Принадлежит: Saltigo GmbH

What is described is a process for preparing organic compounds of the general formula (I) 2. The process as claimed in preceding claim 1 , characterized in that R is an optionally substituted alkenyl claim 1 , alkyl claim 1 , aryl or heteroaryl radical claim 1 , where the heteroaryl radical is a five- claim 1 , six- or seven-membered ring having one or more nitrogen claim 1 , oxygen and/or sulfur atoms in the ring claim 1 , where any further optionally substituted aromatic claim 1 , heteroaromatic and/or cycloaliphatic radicals may be fused onto a cyclic R radical and the R radical may optionally bear one or more substituents which may each independently be (C-C)-alkyl claim 1 , (C-C)-cycloalkyl claim 1 , (C-C)-alkenyl claim 1 , (C-C)-cycloalkenyl claim 1 , (C-C)-alkynyl claim 1 , (C-C)-aryl claim 1 , O—[(C-C)-alkyl] claim 1 , O—[(C-C)-aryl] claim 1 , O—Si[(C-C)-alkyl][(C-C)-aryl] claim 1 , OC(O)—[(C-C)-alkyl] claim 1 , OC(O)—[(C-C)-aryl] claim 1 , NH claim 1 , NH[(C-C)-alkyl] claim 1 , N[(C-C)-alkyl] claim 1 , NH[(C-C)-aryl] claim 1 , N[(C-C)-aryl] claim 1 , NHC(O)—[(C-C)-alkyl] claim 1 , N[(C-C)-alkyl]C(O)—[(C-C)-alkyl] claim 1 , NHC(O)—[(C-C)-aryl] claim 1 , N[(C-C)-alkyl]C(O)—[(C-C)-aryl] claim 1 , NO claim 1 , NO claim 1 , S—[(C-C)-aryl] claim 1 , S—[(C-C)-alkyl] claim 1 , fluorine claim 1 , chlorine claim 1 , bromine claim 1 , pentafluorosulfuranyl claim 1 , CF claim 1 , CN claim 1 , COOM claim 1 , COO—[(C-C)-alkyl] claim 1 , COO—[(C-C)-aryl] claim 1 , C(O)NH—[(C-C)-alkyl] claim 1 , C(O)NH—[(C-C)-aryl] claim 1 , C(O)N—[(C-C)-alkyl] claim 1 , C(O)N—[(C-C)-aryl] claim 1 , CHO claim 1 , SO—[(C-C)-alkyl] claim 1 , SO—[(C-C)-alkyl] claim 1 , SO—[(C-C)-aryl] claim 1 , OSO—[(C-C)-alkyl] claim 1 , OSO—[(C-C)-aryl] claim 1 , PO—[(C-C)-alkyl] claim 1 , PO—[(C-C)-aryl] claim 1 , SOM claim 1 , SO—[(C-C)-alkyl] claim 1 , SO—[(C-C)-aryl] or Si[(C-C)-alkyl][(C-C)-aryl] claim 1 , where M is an alkali metal or alkaline earth metal atom and n is a natural number in the range ...

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18-07-2013 дата публикации

PROCESS FOR PRODUCTION OF HEXAMETHYLENEDIAMINE FROM CARBOHYDRATE-CONTAINING MATERIALS AND INTERMEDIATES THEREFOR

Номер: US20130184495A1
Принадлежит: Rennovia, Inc.

Processes are disclosed for the conversion of a carbohydrate source to hexamethylenediamine (HMDA) and to intermediates useful for the production of hexamethylenediamine and other industrial chemicals. HMDA is produced by direct reduction of a furfural substrate to 1,6-hexanediol in the presence of hydrogen and a heterogeneous reduction catalyst comprising Pt or by indirect reduction of a furfural substrate to 1,6-hexanediol wherein 1,2,6-hexanetriol is produced by reduction of the furfural substrate in the presence of hydrogen and a catalyst comprising Pt and 1,2,6-hexanediol is then converted by hydrogenation in the presence of a catalyst comprising Pt to 1,6 hexanediol, each process then proceeding to the production of HMDA by known routes, such as amination of the 1,6 hexanediol. Catalysts useful for the direct and indirect production of 1,6-hexanediol are also disclosed. 1. A process for preparing hexamethylenediamine from a carbohydrate source , the process comprising: converting a carbohydrate source to a furfural substrate; reacting at least a portion of the furfural substrate with hydrogen in the presence of a heterogeneous reduction catalyst to produce 1 ,6-hexanediol; and , converting at least a portion of the 1 ,6-hexanediol to hexamethylenediamine.2. The process of claim 1 , wherein the heterogeneous reduction catalyst comprises Pt.3. The process of claim 2 , wherein the heterogeneous reduction catalyst further comprises a support selected from the group consisting of zirconias claim 2 , silicas claim 2 , and zeolites.4. The process of claim 2 , wherein the heterogeneous reduction catalyst further comprises at least one metal selected from the group consisting of Mo claim 2 , La claim 2 , Sm claim 2 , Y claim 2 , W claim 2 , and Re.5. The process of claim 1 , wherein the reaction of the furfural substrate with hydrogen is carried out at a temperature in the range of about 60° C. and about 200° C. and a pressure of hydrogen in the range of about 200 psig ...

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25-07-2013 дата публикации

Fluorine Radiolabelling Process

Номер: US20130190529A1
Принадлежит:

The invention relates to a process for producing a process for producing an F-labelled compound, the process comprising treating a compound of formula (I) 4. A process according to wherein said rearomatisation is performed in situ.5. A process according to wherein said rearomatisation comprises the addition of a reagent which effects cleavage of Xfrom the carbon atom of the ring which is para to EDG′ in the compound of formula (IIa) claim 3 , to produce a compound of formula (II) claim 3 , wherein said reagent is an acid claim 3 , base or oxidising agent.613.-. (canceled)1517.-. (canceled)2021.-. (canceled)28. A process according to which further comprises a deprotection step comprising substituting H for said amino protecting group R claim 27 , thereby converting the group —NHRin the compound of formula (IIc″″) or (IId″″) into a —NHgroup.3233.-. (canceled)34. A process according to wherein said rearomatisation is performed in situ.35. A process according to wherein said rearomatisation comprises the addition of a reagent which effects cleavage of Xfrom the carbon atom of the ring which is para to EDG′ in the compound of formula (IIc) or formula (IId) claim 23 , wherein said reagent is an acid claim 23 , base or oxidising agent.3645.-. (canceled)47. A process according to wherein said deprotection step is performed in situ.4851.-. (canceled)52. A process according to wherein the step of treating the compound of formula (I) with [F]fluoride comprises treating the compound of formula (I) with a compound comprising F and a counter cation claim 1 , wherein the counter cation is a quaternary ammonium cation claim 1 , an alkali metal or H.5362.-. (canceled)63. A process according to wherein the oxidant is a hypervalent iodonium (III) reagent or a metal oxide.6466.-. (canceled)67. A process according to wherein the step of treating the compound of formula (I) with [F]fluoride is performed in the presence of an additive claim 1 , wherein the additive is an acid or a crown ...

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01-08-2013 дата публикации

Method for producing optically active amine compound

Номер: US20130197234A1

The present invention relates to methods for producing an optically active amine compound via a highly enantioselective hydrogenation reaction of an imine compound, wherein the imine compound is hydrogenated using a ruthenium metal complex having high catalytic activity and represented by Formula (1) RuXYAB  (1) such as RuBr 2 [(S,S)-xylskewphos][(S,S)-dpen].

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01-08-2013 дата публикации

METHOD FOR PRODUCING NITROBENZENE BY ADIABATIC NITRIDING

Номер: US20130197268A1
Принадлежит: Bayer Intellectual Property GmbH

The invention relates to a process for the continuous production of nitrobenzene by nitration of benzene with a mixture of nitric acid and sulfuric acid under adiabatic conditions, in which unreacted benzene is separated from the crude product obtained after phase separation before washing thereof, using the adiabatic heat of reaction. 19-. (canceled)10. A process for continuously producing nitrobenzene comprisinga) nitrating benzene with a mixture of nitric acid and sulfuric acid under adiabatic conditions to obtain a product;b) separating the product obtained in step a) by phase separation into an aqueous phase comprising sulfuric acid, nitrobenzene, and benzene, and an organic phase comprising nitrobenzene and benzene;c) transferring the aqueous phase obtained in step b) into an evaporator wherein the sulfuric acid is concentrated by pressure reduction, wherein a gaseous stream comprising water, nitrobenzene, and benzene is removed from the evaporator and then condensed, and wherein the resulting concentrated sulfuric acid is fed back into step a);d) separating via distillation from 20% by mass to 100% by mass of the benzene contained in the organic phase obtained in step b) by evaporating the benzene using the adiabatic heat of reaction obtained in step a), wherein a pre-purified nitrobenzene depleted of benzene is obtained;e) washing the pre-purified nitrobenzene obtained in step d) with at least one aqueous phase and subsequently separating the at least one aqueous phase from the nitrobenzene by phase separation to obtain purified nitrobenzene.11. The process of claim 10 , wherein in step d) from 20% by mass to 99.8% by mass of the benzene contained in the organic phase obtained in step b) is separated off and step e) is followed by:f) separating via distillation benzene and water from the purified nitrobenzene obtained in step e) to obtain dried pure nitrobenzene.12. The process of claim 10 , further comprising removing the water from the condensed gaseous ...

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01-08-2013 дата публикации

Method for producing bis(aminomethyl)cyclohexanes

Номер: US20130197269A1
Принадлежит: Mitsui Chemicals Inc

A method for producing bis(aminomethyl)cyclohexanes includes a nuclear hydrogenation step of producing hydrogenated phthalic acids or phthalic acid derivatives by nuclear hydrogenation of phthalic acids or phthalic acid derivatives of at least one selected from the group consisting of phthalic acids, phthalic acid esters, and phthalic acid amides; a cyanation step of treating the hydrogenated phthalic acids or phthalic acid derivatives obtained in the nuclear hydrogenation step with ammonia, thereby producing dicyanocyclohexanes; and an aminomethylation step of treating the dicyanocyclohexanes obtained in the cyanation step with hydrogen, thereby producing bis(aminomethyl)cyclohexanes. In the cyanation step, metal oxide is used as a catalyst, and the obtained dicyanocyclohexanes have a metal content of 3000 ppm or less.

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01-08-2013 дата публикации

METHOD FOR PRODUCING TRANS-1,4-BIS(AMINOMETHYL) CYCLOHEXANE

Номер: US20130197270A1
Принадлежит:

A method for producing trans-1,4-bis(aminomethyl)cyclohexane includes a nuclear hydrogenation step of producing a hydrogenated terephthalic acid or terephthalic acid derivative by nuclear hydrogenation of a terephthalic acid or terephthalic acid derivative, the terephthalic acid or terephthalic acid derivative being at least one selected from the group consisting of terephthalic acid, terephthalic acid ester, and terephthalic acid amide; a cyanation step of treating the hydrogenated terephthalic acid or terephthalic acid derivative with ammonia, thereby producing 1,4-dicyanocyclohexane, and producing trans-1,4-dicyanocyclohexane from the obtained 1,4-dicyanocyclohexane; and an aminomethylation step of treating the trans-1,4-dicyanocyclohexane with hydrogen, thereby producing trans-1,4-bis(aminomethyl)cyclohexane. 1. A method for producing trans-1 ,4-bis(aminomethyl)cyclohexane , the method comprising: 'the terephthalic acid or terephthalic acid derivative being at least one selected from the group consisting of terephthalic acid, terephthalic acid ester, and terephthalic acid amide;', 'a nuclear hydrogenation step of producing a hydrogenated terephthalic acid or terephthalic acid derivative by nuclear hydrogenation of a terephthalic acid or terephthalic acid derivative,'}a cyanation step of treating the hydrogenated terephthalic acid or terephthalic acid derivative obtained in the nuclear hydrogenation step with ammonia, thereby producing 1,4-dicyanocyclohexane, and producing trans-1,4-dicyanocyclohexane from the obtained 1,4-dicyanocyclohexane; andan aminomethylation step of treating the trans-1,4-dicyanocyclohexane obtained in the cyanation step with hydrogen, thereby producing trans-1,4-bis(aminomethyl)cyclohexane,wherein metal oxide is used as a catalyst in the cyanation step, and the obtained trans-1,4-dicyanocyclohexane has a metal content of 3000 ppm or less.2. A method for producing trans-1 ,4-bis(aminomethyl)cyclohexane , the method comprising:a cyanation ...

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08-08-2013 дата публикации

PROCESS FOR PRODUCING COMPOUNDS COMPRISING NITRILE FUNCTIONS

Номер: US20130204001A1
Принадлежит: Rhodia Operations

The production of compounds comprising nitrile functions and of cyclic imide compounds is described. Further described, is the production of compounds comprising nitrile functions from compounds comprising carboxylic functions, optionally of natural and renewable origin, and from a mixture N of dinitriles comprising 2-methylglutaronitrile (MGN), 2-ethylsuccinonitrile (ESN) and adiponitrile (AdN). 1. A process for preparing at least one nitrile of general formula I{'br': None, 'sub': v', '1', 'w, '(NC)—R—(CN)\u2003\u2003(I)'} {'br': None, 'sub': x', '1', 'y, '(HOOC)—R—(COOH)\u2003\u2003(II)'}, 'and at least cyclic imides 3-methylglutarimide and 3-ethylsuccinimide, by reacting at least one carboxylic acid of general formula II'}and a mixture N of dinitriles comprising 2-methylglutaronitrile (MGN), 2-ethylsuccinonitrile (ESN) and adiponitrile (AdN),whereinx, y are equal to 0 or 1 with (x+y) equal to 1 or 2,v, w are equal to 0 or 1 with (v+w) equal to 1 or 2, and from 4 carbon atoms to 34 carbon atoms when (x+y) is equal to 2, and', 'from 2 carbon atoms to 22 carbon atoms when (x+y) is equal to 1., 'R1 represents a linear or branched, saturated or unsaturated hydrocarbon-based group which can comprise heteroatoms, comprising2. The process as defined in claim 1 , wherein the mixture N of dinitriles is a mixture resulting from the process for producing adiponitrile by double hydrocyanation of butadiene.3. The process as defined in claim 1 , wherein the mixture N of dinitriles has the following composition by weight:2-Methylglutaronitrile from 70% to 95%,2-Ethylsuccinonitrile from 5% to 30%, andAdiponitrile from 0% to 10%, andwherein the remaining portion of the composition is composed of various impurities.4. The process as defined in claim 1 , wherein the compound of formula II is derived from a renewable matter of vegetable or animal origin.5. The process as defined in claim 4 , wherein the compound of formula II is selected from the group consisting of a caproic acid ...

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08-08-2013 дата публикации

NEW PROCESS FOR THE RESOLUTION OF ENANTIOMERS OF (3,4 DIMETHOXY-BICYCLO[4.2.0]OCTA-1,3,5-TRIEN-7-YL)NITRILE AND APPLICATION IN THE SYNTHESIS OF IVABRADINE

Номер: US20130204032A1
Принадлежит: LES LABORATOIRES SERVIER

Process for the optical resolution of the compound of formula (I): 4. The process of claim 3 , wherein the reduction of the compound of formula (Ia) is carried out in the presence of palladium-on-carbon and HCl under a hydrogen atmosphere or in the presence of sodium tetraborohydride and trifluoroacetic acid. The present invention relates to a process for the optical resolution of (3,4-dimethoxy-bicyclo[4.2.0]octa-1,3,5-trien-7-yl)nitrile of formula (I) and to the application thereof in the synthesis of ivabradine, of its addition salts with a pharmaceutically acceptable acid and of their hydrates.Ivabradine of formula (II):or 3-{3-[{[(7S)-3,4-dimethoxybicyclo[4.2.0]octa-1,3,5-trien-7-yl]methyl}(methyl)amino]-propyl}-7,8-dimethoxy-1,3,4,5-tetrahydro-2H-3-benzazepin-2-one, and its addition salts with a pharmaceutically acceptable acid, and more especially its hydrochloride, have very valuable pharmacological and therapeutic properties, especially bradycardic properties, making these compounds useful in the treatment or prevention of various clinical situations of myocardial ischaemia such as angina pectoris, myocardial infarct and associated rhythm disturbances, and also in various pathologies involving rhythm disturbances, especially supraventricular rhythm disturbances, and in heart failure.The preparation and therapeutic use of ivabradine and its addition salts with a pharmaceutically acceptable acid, and more especially its hydrochloride, have been described in the European patent specification EP 0 534 859.That patent specification describes the synthesis of ivabradine starting from the compound of formula (III):The compound of formula (III) is prepared starting from the compound of formula (IV):by resolution using camphorsulphonic acid.The compound of formula (III) is an important intermediate in the synthesis of ivabradine.Resolution of the secondary amine of formula (IV) results in the compound of formula (III) in only a low yield (4 to 5%).However, in view ...

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08-08-2013 дата публикации

DECOLORIZATION OF AMINES

Номер: US20130204044A1
Принадлежит:

The present invention provides methods that are used to decolorize compositions containing one or more amines in the presence of one or more weak acids. Significantly, the weak acids, particularly organic acids such as glacial acetic acid, when used in combination with a heat treatment produce dramatically less by-products than do the stronger mineral acids, making heat treatments and subsequent separation techniques more effective while producing less waste. In some modes of practice, the weak acids do not need to be neutralized, eliminating neutralizing steps and waste streams associated with neutralization. Low color products can be obtained easily at very high yield as a consequence. 1. A method of reducing color of a composition including one or more amines and one or more color bodies , comprising the steps of:(a) providing the composition, wherein the composition has an initial color;(b) heat treating the composition in the presence of at least one weak acid under conditions effective to modify the composition so that a separation technique can more effectively separate at least a portion of the amines from at least a portion of the color bodies; and(c) after heat treating, using at least the separation technique to recover at least a portion of the amines from the heat treated composition in a manner such that the recovered portion has less color relative to the initial color.2. The method of claim 1 , further comprising the step of using a color characteristic of the heat treated composition to help determine when heat treating is complete.3. The method of claim 1 , wherein step (a) comprises providing a amine composition having a color in the range from about 400 APHA to about 5000 APHA.4. The method of claim 1 , wherein the amine composition comprises linear triethylenetetramine and/or a congener thereof.5. The method of claim claim 1 , wherein the at least one weak acid comprises an organic acid.6. The method of claim 1 , wherein the at least one weak ...

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15-08-2013 дата публикации

New process for the resolution of enantiomers of (3,4 dimethoxy-bicyclo[4.2.0]octa-1,3,5-trien-7-yl)nitrile and application in the synthesis of ivabradine

Номер: US20130211070A1
Принадлежит: Laboratoires Servier SAS

Process for the optical resolution of the compound of formula (I): by chiral chromatography. Application in the synthesis of ivabradine, of its addition salts with a pharmaceutically acceptable acid and of their hydrates.

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15-08-2013 дата публикации

MONITORING OF THE STOICHIOMETRIC RATIO IN THE REACTION OF NITROAROMATICS WITH HYDROGEN

Номер: US20130211141A1
Принадлежит:

The present invention relates to a continuous process for preparing at least one aromatic amine by hydrogenation of at least one nitroaromatic by means of hydrogen, where a liquid phase comprising at least the aromatic amine and a gas phase comprising at least hydrogen are present, in the presence of a catalyst suspended in the liquid phase at a temperature of from 50 to 250° C. and a pressure of from 5 to 50 bar, wherein the pressure in the reactor is kept essentially constant by continuous adaptation of the amount of hydrogen fed to the reactor, the total amount of hydrogen fed to the reactor is monitored and the introduction of the at least one nitroaromatic is interrupted if the hydrogen uptake in the reactor is not at least 50 mol % of the amount of hydrogen required for stoichiometric reaction of the at least one nitroaromatic to form the at least one aromatic amine. 1. A continuous process for preparing at least one aromatic amine by hydrogenation of at least one nitroaromatic by means of hydrogen , where a liquid phase comprising at least the aromatic amine and a gas phase comprising at least hydrogen are present , in the presence of a catalyst suspended in the liquid phase at a temperature of from 50 to 250° C. and a pressure of from 5 to 50 bar , whereinthe pressure in the reactor is kept essentially constant by continuous adaptation of the amount of hydrogen fed to the reactor,the total amount of hydrogen fed to the reactor is monitored andthe introduction of the at least one nitroaromatic is interrupted if the hydrogen uptake in the reactor is not at least 50 mol %, preferably at least 70 mol %, particularly preferably at least 90 mol %, very particularly preferably at least 95 mol %, in particular at least 98 mol %, of the amount of hydrogen required for stoichiometric reaction of the at least one nitroaromatic to form the at least one aromatic amine.2. The process according to claim 1 , wherein the hydrogen uptake in the reactor corresponding to the ...

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15-08-2013 дата публикации

HALOGENATED DIETHYLTOLUENEDIAMINES

Номер: US20130211142A1
Принадлежит: Lonza Ltd.

Disclosed are halogenated diethyltoluenediamines of formula

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22-08-2013 дата публикации

Process for the preparation of substituted n-(benzyl)cyclopropanamines by imine hydrogenation

Номер: US20130217910A1
Принадлежит: Bayer Intellectual Property GmbH

The present invention relates to a process for the preparation of substituted N-(benzyl)cyclopropanamines of the general formula (II) starting from N-[(aryl)methylene]cyclopropanamine derivatives. The present invention further provides the N-[(arypmethylene]cyclopropanamine derivatives used as starting compounds in this process according to the invention, and their use for the preparation of substituted N (benzyl)cyclopropanamines.

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29-08-2013 дата публикации

SALTS OF POTASSIUM ATP CHANNEL OPENERS AND USES THEREOF

Номер: US20130225806A1
Принадлежит: Essentialis, Inc.

Provided are immediate or prolonged administration of certain salts of Kchannel openers such as diazoxide to a subject to achieve novel pharmacodynamic, pharmacokinetic, therapeutic, physiological, metabolic and compositional outcomes in the treatment of diseases or conditions involving Kchannels. Also provided are pharmaceutical formulations, methods of administration and dosing of the salts that achieve these outcomes and reduce the incidence of adverse effects in treated individuals. Further provided are method of co-administering the salts with other drugs to treat diseases of humans and animals. 2. The method of wherein said cation source is an alkali metal hydroxide.3. The method of wherein said cation source is sodium hydroxide or potassium hydroxide.4. The method of wherein said solvent is selected from the group consisting of acetonitrile claim 3 , low molecular weight ketones claim 3 , and tetrahydrofuran.5. The method of wherein said cation source is an organic cation source comprising an ammonium or at least one tertiary amine group.6. The method of wherein said cation source is choline hydroxide or hexamethyl hexamethylene diammonium dihydroxide.7. The method of wherein said solvent is selected from the group consisting of acetonitrile claim 6 , low molecular weight ketones claim 6 , tetrahydrofuran claim 6 , and 2-methyl tetrahydrofuran.8. The method of wherein said cation source is choline hydroxide claim 6 , and said solvent is selected from the group consisting of acetonitrile claim 6 , low molecular weight ketones claim 6 , tetrahydrofuran claim 6 , and 2-methyl tetrahydrofuran.9. The method of wherein said compound of Formulae I-IV is dissolved in a solvent at a ratio of about 1 g compound of Formulae I-IV to about 1 to 5 mL solvent.10. The method of further comprising adding a co-solvent prior to the step of removing the solvent.11. The method of wherein said co-solvent is selected from the group consisting of methyl tert-butyl ether (MTBE) claim ...

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29-08-2013 дата публикации

Metathesis Catalysts Containing Onium Groups

Номер: US20130225807A1
Принадлежит: Apeiron Synthesis Sp zoo

Disclosed herein is a general method for the preparation of complexes containing a quaternary onium group in an inert ligand. Some of these complexes may be represented by formula 1: Methods for the preparation of complexes of formula 1, the preparation of intermediates and the use of complexes of formula 1 in metathesis reactions and a method for conducting an olefin metathesis reaction are also described.

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29-08-2013 дата публикации

Fluoroalkylation Methods And Reagents

Номер: US20130225815A1
Принадлежит: University of Illinois

A method of forming a fluorinated molecular entity includes reacting in a reaction mixture an aromatic halide, copper, a fluoroalkyl group, and a ligand. The aromatic halide includes an aromatic group and a halogen substituent bonded to the aromatic group. The ligand includes at least one group-V donor selected from phosphorus and an amine. The overall molar ratio of copper to aromatic halide in the reaction mixture is from 0.2 to 3. The method further includes forming a fluoroalkylarene including the aromatic group and the fluoroalkyl group bonded to the aromatic group. A composition, which may be used in the method, consists essentially of copper, the fluoroalkyl group, and the ligand, where the molar ratio of copper to the fluoroalkyl group is approximately 1.

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29-08-2013 дата публикации

TRANSAMINATION OF NITROGEN-CONTAINING COMPOUNDS TO HIGH MOLECULAR WEIGHT POLYALKYLENEAMINES

Номер: US20130225864A1
Автор: King Stephen W.
Принадлежит:

A process for preparing high molecular weight acyclic polyamines comprising providing a reaction mixture that includes at least a first component comprising a first organic, nitrogen-containing compound that contains at least two non-tertiary amine groups separated from one another by a ternary or higher carbon atom spacing that can be transaminated in the presence of a hydrogenation/dehydrogenation catalyst to form a mixture of higher molecular weight, acyclic polyamines while minimizing the formation of cyclic polyamines. 1. A method of making a linear high molecular weight polyamine-containing product mixture comprising the steps of:(a) providing a reaction composition comprising one or more nitrogen-containing compounds comprising a first component that has at least two non-tertiary amine groups separated from one another by at least a ternary or higher carbon atom spacing (C3 or greater spacing) and, optionally, a second component that has at least two nitrogen containing groups separated from one another by a second carbon atom spacing; and(b) subjecting the reaction composition to a transamination reaction in the presence of a hydrogenation/dehydrogenation catalyst to obtain the linear high molecular weight polyamine-containing mixture.2. The method of claim 1 , wherein the component comprises a nitrogen-containing compound having (i) at least two non-tertiary amine groups separated from one another by a ternary or greater carbon atom spacing (C3 or greater spacing) claim 1 , (ii) at least two nitrile functionalities separated by at least one carbon atom (C1 spacing) claim 1 , (iii) at least one nitrile functionality and one non-tertiary amine functionality separated from one another by a binary or greater carbon atom spacing (C2 or greater spacing).6. The method of claim 3 , wherein each R is H.7. A method of making a mixture of congeners of high molecular weight polyamines claim 3 , comprising the steps of: providing a reaction mixture comprising first ...

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05-09-2013 дата публикации

PROCESS FOR PREPARING 1,6-HEXANEDIOL

Номер: US20130231505A1
Принадлежит: E I DU PONT DE NEMOURS AND COMPANY

Disclosed are processes for preparing 1,6-hexanediol from levoglucosenone. In one embodiment, the process comprises contacting levoglucosenone with hydrogen in the presence of a hydrogenation catalyst comprising palladium, platinum/tungsten, nickel/tungsten, rhodium/rhenium, or mixtures thereof at a first temperature between about 50° C. and 100° C. and at a first reaction pressure between about 50 psi and 2000 psi for a first reaction period, and at a second temperature between about 120° C. and 250° C. and at a second pressure between about 500 psi and 2000 psi for a second reaction period to form a product mixture comprising 1,6-hexanediol, wherein the first reaction period is the amount of time in which the levoglucosenone has a conversion of at least about 95%. In one embodiment, the 1,6-hexanediol is converted to 1,6-diaminohexane. 1. A process comprising:(a) contacting levoglucosenone with hydrogen in the presence of a hydrogenation catalyst comprising palladium, platinum/tungsten, nickel/tungsten, rhodium/rhenium, or mixtures thereof at a first temperature between about 50° C. and 100° C. and at a first reaction pressure between about 50 psi and 2000 psi for a first reaction period, wherein the first reaction period is the amount of time in which the levoglucosenone has a conversion of at least about 95%; and at a second temperature between about 120° C. and 250° C. and at a second reaction pressure between about 500 psi and 2000 psi for a second reaction period to form a final product mixture comprising 1,6-hexanediol;(b) isolating the 1,6-hexanediol from the final product mixture;(c) contacting the 1,6-hexanediol with ammonia and hydrogen in the presence of a reductive amination catalyst at a temperature and for a time sufficient to form an amination product mixture comprising 1,6-diaminohexane; and(d) optionally, isolating the 1,6-diaminohexane from the amination product mixture.2. The process of claim 1 , wherein the hydrogenation catalyst further ...

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12-09-2013 дата публикации

Process for preparing amino hydrocarbons by direct amination of hydrocarbons

Номер: US20130233721A1
Принадлежит: BASF SE

The present invention relates to a process for direct amination of hydrocarbons to amino hydrocarbons, comprising (a) the reaction of a reactant stream E comprising at least one hydrocarbon and at least one aminating reagent to give a reaction mixture R comprising at least one amino hydrocarbon and hydrogen in a reaction zone RZ, and (b) electrochemical removal of at least a portion of the hydrogen formed in the reaction from the reaction mixture R by means of at least one gas-tight membrane electrode assembly which is in contact with the reaction zone RZ on the retentate side and which has at least one selectively proton-conducting membrane, at least a portion of the hydrogen being oxidized over an anode catalyst to protons on the retentate side of the membrane, and the protons, after passing through the membrane, being partly or fully reduced by applying a voltage over a cathode catalyst to give hydrogen on the permeate side.

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12-09-2013 дата публикации

PROCESS FOR PREPARING AMINO HYDROCARBONS BY DIRECT AMINATION OF HYDROCARBONS

Номер: US20130236801A1
Принадлежит: BASF SE

The present invention relates to a process for direct amination of hydrocarbons to amino hydrocarbons, comprising 1. A process for direct amination of hydrocarbons to amino hydrocarbons , comprising(a) the reaction of a reactant stream E comprising at least one hydrocarbon and at least one aminating reagent to give a reaction mixture R comprising at least one amino hydrocarbon and hydrogen in a reaction zone RZ, and(b) electrochemical removal of at least a portion of the hydrogen formed in the reaction from the reaction mixture R by means of at least one gas-tight membrane electrode assembly which is in contact with the reaction zone RZ on the retentate side and which has at least one selectively proton-conducting membrane,at least a portion of the hydrogen being oxidized over an anode catalyst to protons on the retentate side of the membrane, and the protons, after passing through the membrane, being partly or fully reacted with an oxidizing agent over a cathode catalyst to give water on the permeate side, and the oxidizing agent originating from a stream O which is contacted with the permeate side of the membrane.2. The process according to claim 1 , wherein the oxidizing agent is oxygen.3. The process according to or claim 1 , wherein the hydrogen is removed from the reaction zone RZ.4. The process according to one or more of to claim 1 , wherein the electrode catalyst present on the retentate side serves simultaneously as an amination catalyst for the conversion of the hydrocarbons to amino hydrocarbons.5. The process according to one or more of to claim 1 , wherein a gas distributor layer present on the retentate side has been functionalized with an amination catalyst.6. The process according to one or more of to claim 1 , wherein the electrodes of the membrane electrode assembly (MEA) comprising an amination catalyst serve for the conversion of the hydrocarbons to amino hydrocarbons.7. The process according to one or more of to claim 1 , wherein claim 1 , in ...

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12-09-2013 дата публикации

AMINES HAVING SECONDARY ALIPHATIC AMINO GROUPS

Номер: US20130237681A1
Автор: BURCKHARDT Urs
Принадлежит: SIKA TECHNOLOGY AG

The present invention relates to novel amides having secondary amino groups, a process for preparing them, adducts of these amines and their uses. The amides can be prepared in a simple way from readily available starting materials. They and their adducts have, in particular, a low viscosity and are suitable as constituent of polyurethane and polyurea compositions having excellent processability and high flexibility, and also as constituent of epoxy resin compositions, in particular coatings. 2. The amine of formula (I) according to claim 1 , wherein Rand Reach stand for a methyl radical and/or Rstands for a hydrogen atom.3. The amine of formula (I) according to claim 1 , wherein Rstands for a hydrogen atom or for a hydrocarbon radical with 1 to 12 carbon atoms claim 1 , optionally containing an ether oxygen.4. The amine of formula (I) according to claim 1 , wherein Rstands for a hydrogen atom or a linear or branched alkyl radical with 1 to 11 carbon atoms claim 1 , optionally with cyclic fractions and optionally with at least one heteroatom or for a mono- or polyunsaturated linear or branched hydrocarbon radical with 5 to 11 carbon atoms or for an optionally substituted aromatic or heteroaromatic six-membered ring.5. The amine of formula (I) according to claim 1 , wherein Xstands for a phenyl claim 1 , biphenyl or naphthyl radical claim 1 , where this radical is optionally substituted claim 1 , with linear or branched alkyl radicals with 1 to 6 carbon atoms claim 1 , with alkoxy groups with 1 to 6 carbon atoms claim 1 , with ester groups with 1 to 6 carbon atoms or with nitrilo groups.7. The method of synthesis of an amine of formula (I) according to claim 6 , wherein the process is carried out in such a way that at one amine PA of formula (II) is condensed with at least one aldehyde ALD of formula (III) to form an aldimine which is then hydrogenated.8. The method according to claim 6 , wherein the amine PA of formula (II) is selected from the group consisting of 1 ...

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19-09-2013 дата публикации

PROCESS FOR HOMOGENEOUSLY CATALYZED, HIGHLY SELECTIVE DIRECT AMINATION OF PRIMARY ALCOHOLS WITH AMMONIA TO PRIMARY AMINES WITH A HIGH VOLUME RATIO OF LIQUID PHASE TO GAS PHASE AND/OR HIGH PRESSURES

Номер: US20130245276A1
Принадлежит: EVONIK DEGUSSA GmbH

The present invention relates to a process for preparing primary amines comprising the process steps 1. A process for preparing a primary amine , the process comprisingA)contacting (i) a solution of a primary alcohol in a fluid, nongaseous phase with (ii) free ammonia or an ammonia-releasing compound and (iii) a homogeneous catalyst, to form a primary amine, and optionallyB) isolating the primary aminewherein a volume ratio of a volume of a liquid phase to a volume of a gas phase in the contacting is greater than 0.05 and/orthe contacting is performed at a pressure greater than 10 bar.2. The process of claim 1 , wherein in the contactingthe ammonia is present in a molar ratio based on hydroxyl groups in the primary alcohol of at least 5:1.3. The process of claim 1 , whereinthe primary alcohol comprises a carboxyl or ester group.4. The process of claim 1 , whereinthe primary alcohol comprises an aliphatic alkyl radical comprising at least three carbon atoms covalently bound to one another and no quaternary carbon atom.5. The process of claim 1 , whereinthe primary alcohol comprises no heteroatoms.6. The process of claim 4 , whereinthe aliphatic alkyl radical is a linear or branched alkyl radical comprising at least 4 carbon atoms.7. The process of claim 1 , whereinthe primary alcohol is selected from the group consisting of 1-butanol, 2-methyl-1-propanol, 1-pentanol, 3-methyl-1-butanol, 2-methyl-1-butanol, 1-hexanol, 4-methyl-1-pentanol, 3-methyl-1-pentanol, 2-methyl-1-pentanol, 2-ethyl-1-butanol, tripropylene glycol, an anhydrohexitol, and tripropylene glycol.8. The process of claim 1 , whereina concentration of the primary alcohol in (i) is from 0.1 to 10000 mmol/l.9. The process of claim 1 , whereinthe catalyst is selected from the group consisting of:an alkali metal alkoxide, an aluminum alkoxide, a lanthanide alkoxide,an inorganic compound comprising a noble metal,and a coordination compound comprising one or more noble metals selected from the group consisting ...

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26-09-2013 дата публикации

PROCESS FOR THE PRODUCTION OF AMIDES

Номер: US20130253225A1
Принадлежит:

The present invention relates to a process for the preparation of compounds of formula I 2. A compound of formula IV according to claim 1 , wherein Rand Rare methyl.4. A compound of formula IV prepared by the process of . This application is a divisional application of U.S. Ser. No. 13/198,739 filed Jan. 8, 2013, which is a divisional application of U.S. Ser. No. 12/066,683 filed Jul. 16, 2008, which is a 371 of International Application No. PCT/EP2006/008982 filed Sep. 14, 2006, which claims priority to CH 01520/05 filed Sep. 16, 2005 and CH 0296/06 filed Feb. 24, 2006, the contents of which are incorporated herein by reference.The present invention relates to a process for the preparation of pyrazolyl-4-carboxylic acid benzo-norbornen-5-yl-amides and also to novel intermediates for use in such a process. The present invention further relates to a novel crystal modification of syn-3-difluoromethyl-1-methyl-1H-pyrazole-4-carboxylic acid (9-isopropyl-1,2,3,4-tetrahydro-1,4-methano-naphthalen-5-yl)-amide, compositions comprising it and to the use thereof in the control of fungus infestation in cultivated plants.Pyrazolyl-4-carboxylic acid benzonorbornen-5-yl-amides, for example 3-difluoromethyl-1-methyl-1H-pyrazole-4-carboxylic acid (9-isopropyl-1,2,3,4-tetrahydro-1,4-methano-naphthalen-5-yl)-amide, are valuable fungicides, such as are described, for example, in WO 04/035589.WO 04/035589 describes a process for the preparation of pyrazolyl-4-carboxylic acid benzonorbornen-5-yl-amides (see Scheme 1):According to WO 04/035589, a 3-nitro-dehydrobenzene generated, for example, from 6-nitro-anthralinic acids of formula (A) wherein Rand Rmay be, inter alia, hydrogen, is first reacted in a Diels-Alder reaction with a cyclic 1,4-diene of formula (B) wherein R, R, Rand Rmay be, inter alia, hydrogen and Y may be, inter alia, —CH((i)-CH)—, to form a 5-nitro-benzonorbornadiene compound of formula (C). Subsequent catalytic reduction under standard conditions (for example, Ra/Ni or ...

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26-09-2013 дата публикации

PROCESS FOR PREPARING 3-AMINOMETHYL-3,5,5-TRIMETHYLCYCLOHEXYLAMINE

Номер: US20130253226A1
Принадлежит: EVONIK DEGUSSA GmbH

The invention relates to an improved process for preparing 3-aminomethyl-3,5,5-trimethylcyclohexylamine, referred to hereinafter as isophoronediamine or, in abbreviated form, IPDA, by: I. preparation of isophorone by catalyzed aldol condensations with acetone as reactant; II. reaction of isophorone with HCN to form isophoronenitrile (IPN, 3-cyano-3,5,5-trimethylcyclohexanone); III. catalytic hydrogenation and/or catalytic reductive amination (also referred to as aminative hydrogenation) of 3-cyano-3,5,5-trimethylcyclohexanone, hereinafter called isophoronenitrile or, in abbreviated form, IPN, to give the isophoronediamine. 1. A process for preparing isophoronediamine IPDA , the process comprising:(i) reacting acetone via a catalyzed aldol condensation in a reactor, thereby obtaining a reaction product comprising isophorone,(ii) working-up the reaction product, thereby obtaining a stream of value(iii) hydrolyzing the stream of value in a hydrolysis apparatus,(iv) separating the stream of value into an organic fraction and an aqueous fraction,(v) recovering isophorone from the organic fraction,(vi) distilling the aqueous fraction in a distillative workup apparatus comprising a top and a bottom,(vii) passing vapors from the top of the distillative workup apparatus onward into the hydrolysis apparatus,(viii) reacting isophorone with HCN via a base-catalyzed reaction, thereby obtaining isophoronenitrile IPN, and(ix) reacting IPN via a catalytic hydrogenation, a catalytic reductive amination, or both in the presence of ammonia, hydrogen, at least one catalyst, and optionally a solvent or a solvent mixture, thereby obtaining IPDA,wherein a cyanide ion concentration in a reaction mixture sent to the catalytic hydrogenation is of from 200 ppmw to 5000 ppmw, based on the IPN used.2. The process of claim 1 , wherein water from the bottom of the distillative workup apparatus is subjected to a flash evaporation claim 1 , thereby obtaining a purified water which is recycled into ...

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03-10-2013 дата публикации

PROCESS FOR PREPARING 3-AMINOMETHYL-3,5,5-TRIMETHYLCYCLOHEXYLAMINE

Номер: US20130261341A1
Принадлежит: EVONIK DEGUSSA GmbH

The invention relates to an improved process for preparing 3-aminomethyl-3,5,5-trimethylcyclohexylamine, referred to hereinafter as isophoronediamine or IPDA for short, by means of catalytic hydrogenation and/or catalytic reductive amination (also referred to as aminating hydrogenation) of -cyano--trimethylcyclohexanone, also called isophoronenitrile or IPN for short hereinafter. 1. A process for preparing isophoronediamine , the process comprising:hydrogenating, reductively aminating, or both hydrogenating and reductively aminating isophoronenitrile, in a presence of ammonia, hydrogen, a catalyst and optionally a solvent or a solvent mixture,wherein a cyanide ion concentration in a reaction mixture sent to the hydrogenating is of from 200 ppmw to 5000 ppmw, based on an amount of the isophoronenitrile added.2. The process of claim 1 ,wherein the cyanide ion concentration is of from 200 ppmw to 3000 ppmw.3. The process of claim 1 ,wherein the cyanide ion concentration is adjusted by controlled metered addition of HCN or a cyanide salt, or with an isophoronenitrile quality having the cyanide ion concentration of from 200 ppmw to 5000 ppmw.4. The process of claim 1 ,wherein an adjustment of the cyanide ion concentration is achieved by controlled redissociation of the isophoronenitrile in an imination stage.5. The process of claim 4 ,wherein the adjustment of the cyanide ion concentration by increasing a temperature in the imination stage by 5-50 K, above a temperature, depending on a presence of an imination catalyst, is needed to achieve a conversion of isophoronenitrile to isophoronenitrileimine of at least 80% in the imination stage.6. The process of claim 1 ,wherein the process is performed in one stage or a plurality of stages.7. The process of claim 1 ,wherein the isophoronediamine is prepared in a two-stage process.8. The process of claim 7 ,wherein the isophoronenitrile is partially converted to isophoronenitrileimine in a first stage by reacting with the ...

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17-10-2013 дата публикации

PROCESSES FOR SEPARATING ONE OR MORE AMINE BYPRODUCTS FROM ONE OR MORE DESIRED AMINES

Номер: US20130274522A1
Принадлежит: Dow Global Technologies LLC

The present invention relates to separating one or more amine byproducts from one or more desired amines. More particularly, the invention involves forming a byproduct component with one or more amine byproducts and a first adjuvant component. The byproduct component has an enhanced separation characteristic relative to separating the amine byproducts from the desired amines in the absence of an adjuvant. Preferably, the byproduct component is separated in the presence of a second adjuvant component that preferably has a boiling point less than the boiling point of the first adjuvant component.

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24-10-2013 дата публикации

P-terphenyl compound mixture and electrophotographic photoreceptors made by using the same

Номер: US20130280652A1
Принадлежит: Hodogaya Chemical Co Ltd

An object of the invention is to provide a method of making a p-terphenyl compound mixture which includes two symmetric p-terphenyl compounds respectively represented by formula (1) and formula (2) and an asymmetric p-terphenyl compound represented by formula (3)

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24-10-2013 дата публикации

Novel ruthenium complexes and their uses in processes for formation and/or hydrogenation of esters, amides and derivatives thereof

Номер: US20130281664A1
Принадлежит: Yeda Research and Development Co Ltd

The present invention relates to novel Ruthenium catalysts and related borohydride complexes, and the use of such catalysts, inter alia, for (1) hydrogenation of amides (including polyamides) to alcohols and amines; (2) preparing amides from alcohols with amines (including the preparation of polyamides (e.g., polypeptides) by reacting dialcohols and diamines and/or by polymerization of amino alcohols); (3) hydrogenation of esters to alcohols (including hydrogenation of cyclic esters (lactones) or cyclic di-esters (di-lactones) or polyesters); (4) hydrogenation of organic carbonates (including polycarbonates) to alcohols and hydrogenation of carbamates (including polycarbamates) or urea derivatives to alcohols and amines; (5) dehydrogenative coupling of alcohols to esters; (6) hydrogenation of secondary alcohols to ketones; (7) amidation of esters (i.e., synthesis of amides from esters and amines); (8) acylation of alcohols using esters; (9) coupling of alcohols with water to form carboxylic acids; and (10) dehydrogenation of beta-amino alcohols to form pyrazines. The present invention further relates to the novel uses of certain pyridine Ruthenium catalysts.

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24-10-2013 дата публикации

Compounds for the treatment of metabolic disorders

Номер: US20130281705A1
Автор: Shalini Sharma
Принадлежит: Wellstat Therapeutics Corp

Compounds useful for the treatment of various metabolic disorders, such as insulin resistance syndrome, diabetes, hyperlipidemia, fatty liver disease, cachexia, obesity, atherosclerosis and arteriosclerosis, are disclosed.

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31-10-2013 дата публикации

TERTIARY AMINE PREPARATION PROCESS

Номер: US20130289309A1
Принадлежит: KAO CORPORATION

The present invention relates to a process for producing a tertiary amine, including the following steps (1) and (2): 111-. (canceled)13. The process for producing a tertiary amine according to claim 12 , further comprising the following step (A) between the step (1) and the step (2):Step (A): reducing an amount of the amine contained in the hydrogen-containing gas discharged from the first reaction vessel.14. The process for producing a tertiary amine according to claim 13 , wherein in the step (A) claim 13 , the hydrogen-containing gas is contacted with water to reduce an amount of the amine contained in the hydrogen-containing gas.15. The process for producing a tertiary amine according to claim 13 , wherein in the step (A) claim 13 , the hydrogen-containing gas is contacted with an acid aqueous solution to reduce an amount of the amine contained in the hydrogen-containing gas.16. The process for producing a tertiary amine according to claim 12 , further comprising the following step (3):Step (3): treating the metal catalyst used in the second reaction vessel with hydrogen.17. The process for producing a tertiary amine according to claim 12 , wherein the metal catalyst used in the second reaction vessel contains at least one metal selected from the group consisting of nickel claim 12 , cobalt claim 12 , ruthenium claim 12 , platinum claim 12 , rhodium claim 12 , palladium claim 12 , molybdenum claim 12 , tungsten and rhenium as a main active component.18. The process for producing a tertiary amine according to claim 17 , wherein the metal catalyst used in the second reaction vessel contains at least one metal selected from the group consisting of ruthenium claim 17 , platinum claim 17 , rhodium claim 17 , palladium claim 17 , tungsten and rhenium as a main active component claim 17 , and the reaction in the second reaction vessel is carried out at a temperature of from 100 to 350° C.19. The process for producing a tertiary amine according to claim 17 , wherein ...

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31-10-2013 дата публикации

Method for producing tertiary amine

Номер: US20130289310A1
Принадлежит: Kao Corp

The present invention discloses the method for producing a tertiary amine, using the column reactor packed with catalyst layers, containing supplying a liquid and a gaseous raw materials from the bottom of the column, reacting these raw materials in the column, and discharging the product from the top of the column, wherein the column reactor includes two or more honeycomb catalyst layers as the catalyst layers, one or more spaces between each honeycomb catalyst layer, and one or more rectifying sections that prevents a partial or whole back flow of the raw materials, arranged in each space without contacting with the honeycomb catalyst layer.

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31-10-2013 дата публикации

PRODUCTION OF ALPHA, OMEGA-DIOLS

Номер: US20130289311A1
Принадлежит:

Disclosed herein are processes for preparing an α,ω-C-diol, wherein n is 5 or greater, from a feedstock comprising a Coxygenate. In one embodiment, the process comprises contacting the feedstock with hydrogen gas in the presence of a catalyst comprising Cu, a Cu oxide, or mixtures thereof; a heteropoly acid component comprising H[P(WO)], H[Si(WO)], H[P(MoO)], H[Si(MoO)], CsH[P(WO)], CsH[Si(WO)], or mixtures thereof; optionally a second metal component comprising Cr, a Cr oxide, Ni, a Ni oxide, Mn, a Mn oxide, Fe, an Fe oxide, Co, a Co oxide, Mo, a Mo oxide, W, a W oxide, Re, a Re oxide, Zn, or a Zn oxide, Ag, a Ag oxide, SiO, or AlO; optionally at least one promoter comprising Na, K, Mg, Rb, Cs, Ca, Sr, Ba, Ce, or mixtures thereof; and optionally a support. 1. A process for preparing an α ,ω-C-diol , comprising the steps:{'sub': 'n', '(a) providing a feedstock comprising a Coxygenate;'}{'sub': 'n', '(b) contacting the feedstock with hydrogen gas, in the presence of a catalyst and at a temperature and for a time sufficient to form a product mixture comprising an α,ω-C-diol;'}wherein n is 5 or greater; and wherein the catalyst comprises a first metal component, a heteropoly acid component, optionally a second metal component, optionally at least one promoter, and optionally a support;wherein:the first metal component comprises Cu, a Cu oxide, or mixtures thereof;{'sub': 3', '3', '10', '4', '4', '3', '10', '4', '4', '3', '10', '4', '4', '3', '10', '4', '2.5', '0.5', '3', '10', '4', '2.5', '0.5', '3', '10', '4, 'the heteropoly acid component comprises H[P(WO)], H[Si(WO)], H[P(MoO)], H[Si(MoO)], CsH[P(WO)], CsH[Si(WO)], or mixtures thereof;'}{'sub': 2', '2', '3, 'the second metal component comprises Cr, a Cr oxide, Ni, a Ni oxide, Mn, a Mn oxide, Fe, an Fe oxide, Co, a Co oxide, Mo, a Mo oxide, W, a W oxide, Re, a Re oxide, Zn, or a Zn oxide, Ag, a Ag oxide, SiO, or AlO; and'}the promoter comprises Na, K, Mg, Rb, Cs, Ca, Sr, Ba, Ce, or mixtures thereof.2. The process of ...

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31-10-2013 дата публикации

PRODUCTION OF ALPHA, OMEGA-DIOLS

Номер: US20130289312A1
Принадлежит: E I DU PONT DE MEMOURS AND COMPANY

Disclosed herein are processes for preparing an α,ω-C-diol, wherein n is 5 or greater, from a feedstock comprising a Coxygenate. In some embodiments, the process comprises contacting the feedstock with hydrogen gas in the presence of a catalyst comprising metals M1, M2, and M3 and optionally a support, wherein: M1 is Mn, Cr, V, or Ti; M2 is Ni, Co, or Fe; and M3 is Cu, Ag, Pt, Pd or Au; or M1 is Pt or Rh; M2 is Cu, Ni or Pd; and M3 is Mo, Re or W. The Coxygenate may be obtained from a biorenewable resource. 2. The process of claim 1 , wherein n=5 or 6.3. The process of claim 1 , wherein the optional support is present in the catalyst and comprises WO claim 1 , SiO claim 1 , AlO claim 1 , carbon claim 1 , TiO claim 1 , ZrO claim 1 , SiO—AlO claim 1 , montmorillonite claim 1 , SiO—TiO claim 1 , tungstated ZrO claim 1 , zeolites claim 1 , VO claim 1 , MoO claim 1 , or mixtures thereof.4. The process of claim 1 , wherein the Coxygenate comprises 1 claim 1 ,2 claim 1 ,6-hexanetriol; 1 claim 1 ,2 claim 1 ,5-pentanetriol; 2H-tetrahydropyran-2-methanol; tetrahydrofuran-2 claim 1 ,5-dimethanol; furan-2 claim 1 ,5-dimethanol; 2 claim 1 ,5 dihydrofuran-2 claim 1 ,5-dimethanol; levoglucosenone; levoglucosan; levoglucosenol; 1 claim 1 ,6-anhydro-3 claim 1 ,4-dideoxy-p-D-pyranose-2-one; isosorbide; hydroxymethylfurfural; sorbitol; glucose; fructose; xylitol; 3 claim 1 ,4-dihydro-2H-pyran-2-carbaldehyde; 1 claim 1 ,2 claim 1 ,5 claim 1 ,6-hexanetetraol; 1 claim 1 ,2 claim 1 ,3 claim 1 ,5 claim 1 ,6-hexanepentanol; 1 claim 1 ,5-anhydro-3 claim 1 ,4-dideoxy-hexitol; 5-hydroxy-2H-tetrahydropyran-2 methanol; furfural; furfuryl alcohol; tetrahydrofurfuryl alcohol; pentoses; dimers containing pentose; oligomers containing pentose; hexoses; dimers containing hexose; oligomers containing hexose; condensation products from the reaction of 5-(hydroxymethyl)-2-furfural with ketones and/or aldehydes; and condensation products from the reaction of furfural with ketones and/or aldehydes.5. The ...

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07-11-2013 дата публикации

Method for producing xylylenediamine

Номер: US20130296609A1
Принадлежит: Mitsubishi Gas Chemical Co Inc

Provided is a method for stably and economically producing xylylenediamine with a high yield and long catalyst service life by hydrogenating dicyanobenzene that is obtained by ammoxidating xylene. By bringing an aqueous basic solution into contact with a dicyanobenzene-absorbed liquid, which is obtained by bringing an ammoxidation reaction gas into contact with an organic solvent, under specified temperature conditions, and subjecting a base and a carboxylic acid in the dicyanobenzene-absorbed liquid to a neutralization reaction so as to form an aqueous phase that contains a water-soluble salt, and then subjecting an organic phase and the aqueous phase to liquid-liquid separation so as to remove the aqueous phase, it is possible to remove the carboxylic acid contained in the dicyanobenzene-absorbed liquid with high selectivity while inhibiting loss of the dicyanobenzene. By subjecting the raw material dicyanobenzene, which is obtained by separating low boiling point compounds from the post liquid-liquid separation organic phase by distillation under reduced pressure, to hydrogenation, xylylenediamine is produced with a high yield and the service life of the hydrogenation catalyst is extended.

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14-11-2013 дата публикации

PRODUCTION METHOD FOR AMINO COMPOUND

Номер: US20130303805A1
Принадлежит: MITSUBISHI GAS CHEMICAL COMPANY, INC.

The present invention relates to a process for producing an amino compound by subjecting a polyamine and an alkenyl compound to addition reaction in the presence of an alkali metal hydride compound which is capable of supplying the amino compound in a stable manner without occurrence of odor. 1: A process for producing an amino compound , the process comprising:conducting an addition reaction between a polyamine and an alkenyl compound in the presence of an alkali metal hydride compound.2: The process according to claim 1 ,wherein the conducting comprises mixing and contacting the alkali metal hydride compound with the polyamine, thereby obtaining a mixture and adding the alkenyl compound to the mixture.3: The process according to claim 1 ,wherein the conducting comprises adding the alkenyl compound intermittently in divided parts.4: The process according to claim 1 ,wherein the alkali metal hydride compound is present in an amount of from 0.01% to 3% by mass on a basis of a total amount of the alkali metal hydride compound and the polyamine.5: The process according to claim 1 , {'br': None, 'H2N—CH2-A-CH2—NH2\u2003\u2003(1),'}, 'wherein the polyamine is a polyamine represented by formula (1)wherein A is a phenylene group or a cyclohexylene group.6: The process according to claim 1 , {'br': None, 'H2N—(CH2CH2NH)n-H\u2003\u2003(2),'}, 'wherein the polyamine is a polyamine represented by formula (2)wherein n is an integer of from 1 to 5.7: The process according to claim 1 ,wherein the polyamine is a cyclic aliphatic polyamine having 9 or more carbon atoms and 2 or more amino groups in a molecule thereof as well as 3 or more active hydrogen atoms derived from amino groups.8: The process according to claim 7 ,{'b': 4', '3, 'wherein the cyclic aliphatic polyamine is menthenediamine, isophoronediamine, diaminodicyclohexyl methane, bis(-amino--methylcyclohexyl)methane, N-aminomethyl piperazine, or norbornanediamine.'}9: The process according to claim 1 ,wherein the ...

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21-11-2013 дата публикации

Synthesis of therapeutic and diagnostic drugs centered on regioselective and stereoselective ring opening of aziridinium ions

Номер: US20130310555A1
Автор: Hyun-Soon Chong
Принадлежит: Illinois Institute of Technology

Stereoselective and regioselective synthesis of compounds via nucleophilic ring opening reactions of aziridinium ions for use in stereoselective and regioselective synthesis of therapeutic and diagnostic compounds.

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21-11-2013 дата публикации

Processes for preparing amines and catalysts for use therein

Номер: US20130310560A1
Принадлежит: BASF SE

Processes for preparing an amine are described which comprise reacting a primary or secondary alcohol, aldehyde and/or ketone with hydrogen and a nitrogen compound selected from the group of ammonia, primary and secondary amines, in the presence of a zirconium dioxide-, copper- and nickel-containing catalyst. The catalytically active composition of the catalyst, before its reduction with hydrogen, comprises oxygen compounds of zirconium, of copper, of nickel, in the range from 1.0 to 5.0% by weight of oxygen compounds of cobalt, calculated as CoO, and in the range from 0.2 to 5.0% by weight of oxygen compounds of sulfur, of phosphorus, of gallium, of lead and/or of antimony, calculated in each case as H2SO4, H3PO4, Ga203, PbO and Sb203 respectively.

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05-12-2013 дата публикации

PROCESS FOR PRODUCTION OF FLUOROSULFONYLIMIDE AMMONIUM SALT

Номер: US20130323154A1
Принадлежит: NIPPON SODA CO., LTD.

A compound [I] such as ammonium N-(chlorosulfonyl)-N-(fluorosulfonyl)imide is reacted with hydrogen fluoride to obtain a compound [II] such as ammonium N,N-di(fluorosulfonyl)imide. The obtained compound [II] is reacted with an alkali metal compound or the like to obtain a compound [IV] such as an N,N-di(fluorosulfonyl)imide alkali metal salt. 4. The process disclosed according to claim 3 , wherein the fluorosulfonylimide ammonium salt represented by formula II is reacted with an alkali metal hydroxide or a tertiary amine compound claim 3 , and M in formula IV represents an alkali metal cation or a tertiary ammonium cation. The present invention relates to a process for producing a fluorosulfonylimide ammonium salt. More specifically, the present invention relates to a process for producing a fluorosulfonylimide ammonium salt with good efficiency and maximum suppression of the contamination of metal impurities that degrade electrolyte properties and the like.Priority is claimed on Japanese Patent Application No. 2011-027563, filed Feb. 10, 2011, the content of which is incorporated herein by reference.Fluorosulfonylimide salts are useful compounds in a wide variety of fields, and are used as electrolytes, as additives added to the electrolytes of fuel cells, and as selective electron withdrawing compounds and the like (see Patent Document 1). Fluorosulfonylimide alkali metal salts and various fluorosulfonylimide onium salts can be obtained by reactions using an alkali metal compound or an onium compound. Fluorosulfonylimide ammonium salts are useful as production intermediates for fluorosulfonylimide alkali metal salts and fluorosulfonylimide onium salts other than the ammonium salts.Various processes have been proposed for synthesizing fluorosulfonylimide ammonium salts. For example, Non-Patent Document 1 discloses a process of synthesizing a di(fluorosulfonyl)imide ammonium salt from di(fluorosulfonyl)imide and ammonia.Patent Document 2 discloses a process for ...

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05-12-2013 дата публикации

Processes for producing hexamethylenediamine (hmd), adiponitrile (adn), adipamide (adm) and derivatives thereof

Номер: US20130324694A1
Принадлежит: Bioamber SAS

Processes for producing nitrogen containing compounds include producing hexamethylenediamine (HMD), adiponitrile (ADN), adipamide (ADM) and derivatives thereof from adipic acid (AA) obtained from fermentation broths containing diammonium adipate (DAA) or monoammonium adipate (MAA).

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05-12-2013 дата публикации

Process for preparing styrene derivatives

Номер: US20130324745A1
Принадлежит: Saltigo GmbH

A process is provided which allows the synthesis of a large number of styrene derivatives with formation of C—C bonds, with use being possible of economically advantageous substrates, readily available carbon nucleophiles, and both inexpensive and environmentally unproblematic catalyst systems, permitting reaction under mild conditions and a high compatibility with functional groups on the reactants involved.

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12-12-2013 дата публикации

Process for Preparing Piperazine

Номер: US20130331573A1
Принадлежит:

Process for preparing piperazine of the formula I 134-. (canceled)36. The process according to claim 35 , wherein the catalytically active mass of the catalyst claim 35 , prior to its reduction with hydrogen claim 35 , comprises in the range from 0.4 to 4.0% by weight of oxygen-containing compounds of tin claim 35 , calculated as SnO.37. The process according to claim 35 , wherein the catalytically active mass of the catalyst claim 35 , prior to its reduction with hydrogen claim 35 , comprises in the range from 0.6 to 3.0% by weight of oxygen-containing compounds of tin claim 35 , calculated as SnO.38. The process according to claim 35 , wherein the catalytically active mass of the catalyst claim 35 , prior to its reduction with hydrogen claim 35 , comprises in the range from 5.0 to 35% by weight of oxygen-containing compounds of cobalt claim 35 , calculated as CoO.39. The process according to claim 35 , wherein the catalytically active mass of the catalyst claim 35 , prior to its reduction with hydrogen claim 35 , comprises in the range from 10 to 30% by weight of oxygen-containing compounds of cobalt claim 35 , calculated as CoO.40. The process according to claim 35 , wherein the catalytically active mass of the catalyst claim 35 , prior to its reduction with hydrogen claim 35 , comprises in the range from{'sub': 2', '3, '15 to 80% by weight of oxygen-containing compounds of aluminum, calculated as AlO,'}1.0 to 20% by weight of oxygen-containing compounds of copper, calculated as CuO, and5.0 to 35% by weight of oxygen-containing compounds of nickel, calculated as NiO.41. The process according to claim 35 , wherein the catalytically active mass of the catalyst claim 35 , prior to its reduction with hydrogen claim 35 , comprises in the range from{'sub': 2', '3, '30 to 70% by weight of oxygen-containing compounds of aluminum, calculated as AlO, 2.0 to'}18% by weight of oxygen-containing compounds of copper, calculated as CuO, and10 to 30% by weight of oxygen- ...

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12-12-2013 дата публикации

PROCESS FOR THE DIRECT AMINATION OF ALCOHOLS USING AMMONIA TO FORM PRIMARY AMINES BY MEANS OF A XANTPHOS CATALYST SYSTEM

Номер: US20130331580A1
Принадлежит: EVONIK DEGUSSA GmbH

The present invention relates to a chemocatalytic liquid-phase process for the direct one-stage amination of alcohols to primary amines by means of ammonia in high yields using a catalyst system containing at least one transition metal compound and a xantphos ligand. 2. The process according to claim 1 ,wherein{'sup': 1', '2', '3', '4, 'sub': 3', '2, 'R=R=R=R=phenyl, and A=—C(CH)—.'}3. The process according to claim 1 ,whereinthe xantphos ligand is carbonylchlorohydrido[9,9-dimethyl-4,5-bis(diphenylphosphino)xantheno]ruthenium(II)].4. The process according to claim 1 ,whereinthe alcohol is an aliphatic, linear ω-hydroxycarboxylic acid having a carbon chain comprising at least 8 carbon atoms.5. The process according to claim 1 ,whereinthe alcohol has a concentration of from 0.1 to 1000 mmol/l, based on the fluid phase.6. The process according to claim 1 ,wherein the contacting comprises contacting with liquid or supercritical ammonia, with a solution of ammonium salts in a solvent, or both.7. The process according to claim 1 ,wherein in the contacting,the ammonia has a molar ratio to hydroxyl groups in the alcohol of at least 5:1.8. The process according to claim 1 ,wherein the contacting is carried out at a pressure of from 1 to 1000 bar.9. The process according to claim 1 ,wherein the contacting is carried out in a temperature range of from 80 to 220° C.10. The process according to claim 1 ,whereina volume ratio of a liquid phase to a gas phase in the contacting is greater than or equal to 0.05.11. The process according to claim 1 ,wherein the process is carried out in an absence of hydrogen.12. The process according to claim 1 , wherein the alcohol has a concentration of from 0.1 to 100 mmol/l based on the fluid phase.13. The process according to claim 1 , wherein the alcohol has a concentration of from 0.1 to 10 mmol/l based on the fluid phase.14. The process according to claim 1 , wherein in the contacting claim 1 , the ammonia has a molar ratio to hydroxyl ...

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19-12-2013 дата публикации

NOVEL ORGANIC METAL COMPLEX AND PROCESS FOR PREPARING AMINE COMPOUND

Номер: US20130338359A1
Принадлежит:

[Problem] 2. The organometallic compound according to claim 1 , wherein the nitrogen-containing six-membered monocyclic aromatic ring is selected from a pyridine ring claim 1 , a pyridazine ring claim 1 , a pyrazine ring claim 1 , a Pyrimidine ring or a triazine ring.3. The organometallic compound according to claim 1 , wherein the polycyclic aromatic ring is selected from a quinoline ring claim 1 , an isoquinoline ring claim 1 , a quinazoline ring claim 1 , a quinoxaline ring claim 1 , acridine ring claim 1 , a cinnoline ring or a phthalazine ring.5. The catalyst according to claim 4 , wherein the nitrogen-containing six-membered monocyclic aromatic ring is selected from a pyridine ring claim 4 , a pyridazine ring claim 4 , a pyrazine ring claim 4 , a Pyrimidine ring or a triazine ring.6. The catalyst according to claim 4 , wherein the polycyclic aromatic ring is selected from a quinoline ring claim 4 , an isoquinoline ring claim 4 , a quinazoline ring claim 4 , a quinoxaline ring claim 4 , acridine ring claim 4 , a cinnoline ring or a phthalazine ring.7. A process for preparing an amine compound claim 4 , wherein the amine compound is prepared by reacting a hydrogen-donating organic or inorganic compound with an imine compound or an enamine compound under the presence of the catalyst according to .8. The process for preparing the amine compound according to claim 7 , wherein the amine compound is prepared by the reaction of an imine compound or an enamine compound generated by mixing a carbonyl compound with an amine compound in a reaction system.10. The process for preparing an amine compound according to claim 7 , wherein the hydrogen-donating organic or inorganic compound is formic acid or formate.11. The catalyst according to claim 4 , wherein M in general formula (5) is rhodium or iridium.12. A process for preparing an amine compound claim 5 , wherein the amine compound is prepared by reacting a hydrogen-donating organic or inorganic compound with an imine ...

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19-12-2013 дата публикации

Process for the Synthesis of Aminobiphenylene

Номер: US20130338369A1
Принадлежит: BASF SE

The present invention relates to a process for the synthesis of 2-aminobiphenylene and derivatives thereof by reacting a benzene diazonium salt with an aniline compound under basic reaction conditions. 127-. (canceled)31. The process of claim 28 , wherein the reaction is performed at a pH of 9.1 or greater32. The process of claim 28 , wherein the reaction is performed in the presence of at least one solvent.33. The process of claim 32 , wherein the solvent is an aqueous solvent.34. The process of claim 28 , wherein the reaction is performed in the presence of water and of at least one base.35. The process of claim 34 , wherein the base is selected from the group consisting of alkali metal hydroxides claim 34 , alkaline earth metal hydroxides claim 34 , alkali metal carbonates and alkali metal phosphates claim 34 , and is preferably sodium hydroxide or potassium hydroxide.36. The process of claim 28 , wherein the reaction is performed within the temperature range from 50 to 130° C.37. The process of claim 28 , wherein the compound of the formula 1 or the compound of the formula 2 or both compounds 1 and 2 are used in the reaction dispersed in an alkaline medium.38. The process of claim 37 , wherein the pH of the alkaline medium is at least 9.1.39. The process of claim 28 , wherein claim 28 , in a first step claim 28 , a compound of the formula 1 is reacted with a base in aqueous medium and claim 28 , in a second step claim 28 , the dispersion obtained is added to the compound of the formula 2.40. The process of claim 39 , wherein the pH of the dispersion obtained is at least 9.1.41. The process of claim 39 , wherein the compound 2 claim 39 , prior to addition of the dispersion claim 39 , is brought to a temperature of 50 to 130° C.42. The process of claim 28 , wherein the compound of the formula 2 is initially charged in an alkaline medium and the compound of the formula 1 is added.43. The process of claim 42 , wherein the compound of the formula 2 is initially ...

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19-12-2013 дата публикации

PROCESS FOR THE SELECTIVE META-CHLORINATION OF ALKYLANILINES

Номер: US20130338400A1
Принадлежит: Lonza Ltd.

A process for the chlorination of alkylanilines is provided allowing a highly selective chlorination in the meta-position of the aromatic ring. This is achieved by reacting a mixture comprising the alkylaniline and sulfuric acid with chlorine. This process allows a meta-chlorination with a selectivity of more than 90%. 2. The process of claim 1 , wherein Ris H.3. The process of claim 1 , wherein Rand Rindependently are alkyl groups.4. The process of claim 1 , wherein Rand Rare the same.5. The process of claim 1 , wherein the reaction is carried out in a closed system.6. The process of claim 1 , wherein the reaction is carried out in an open system.7. The process of claim 1 , wherein the reaction is carried out at a temperature of from 5° C. to 120° C.8. The process of claim 7 , wherein the reaction is carried out at a temperature of from 10° C. to 100° C.9. The process of claim 1 , wherein the sulfuric acid has an HSOconcentration of at least 70% by weight.10. The process of claim 9 , wherein the sulfuric acid has an HSOconcentration of at least 85% by weight.11. The process of claim 10 , wherein the sulfuric acid has an HSOconcentration of at least 95% by weight. The present invention is directed to a process for the preparation of chlorinated alkylanilines, in particular chlorinated 2,6-dialkylanilines.Meta-chlorinated 2,6-dialkylanilines are important starting materials for the preparation of chlorinated 4,4′-methylene-bis(2,6-dialkylanilines) which are used as chain extenders or cross linking agents in the polymer industry, for example in the preparation of polyurethanes and epoxy resins.Beard and Hickinbottom (1958, 2982-2986) describe meta-selective chlorination of 2,6-dialkylanilines starting from the corresponding N-chloro-acetanilides. This reaction, however, suffers from the disadvantage of additional protection and deprotection steps in order to obtain the free amine.U.S. Pat. No. 3,962,336 discloses the preparation of 5-chloro-2-toluidine by reacting 2- ...

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26-12-2013 дата публикации

PROCESS FOR THE RACEMIZATION OF OPTICALLY ACTIVE ARYLALKYLAMINES

Номер: US20130345475A1
Автор: Schrems Marcus Georg
Принадлежит:

Many optically active amines are valuable pharmaceuticals and intermediates for the preparation of active compounds. It is frequently the case that only one of the two enantiomers is active or not harmful, so that isolation of this enantiomer from the racemic mixture is necessary. Processes for racemate resolution make it possible to separate racemic mixtures into their enantiomers. Here, it is useful to once again racemize the enantiomer which is not required and recirculate it to racemate resolution and thus improve the yield of the desired enantiomer. The present invention relates to processes for the racemization of optically active amines, in particular arylalkylamines, in the presence of hydrogen and a hydrogenation/dehydrogenation catalyst comprising nickel, cobalt and copper as active components at elevated temperature. 2. The process of claim 1 , wherein the active components nickel claim 1 , cobalt and copper of the hydrogenation/dehydrogenation catalyst are present entirely or partly in a form of oxides before being activated by a reducing agent.3. The process of claim 1 , wherein the hydrogenation/dehydrogenation catalyst comprises an inert support material.4. The process of claim 1 , wherein the hydrogenation/dehydrogenation catalyst additionally comprises at least one further active component selected from the group consisting of zirconium claim 1 , molybdenum and palladium which further active component is present entirely or partly in a form of an oxide claim 1 , before being activated by a reducing agent.5. The process of claim 1 , wherein the reacting is carried out in the presence of an amine of formula R3NHin which R3 corresponds to the radical R3 of the optically active amine of formula I.6. The process of claim 1 , wherein the hydrogenation/dehydrogenation catalyst comprises less than 1% by weight of zinc-comprising compounds including metallic zinc claim 1 , calculated as ZnO claim 1 , based on a sum of oxygen-comprising compounds of nickel ...

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02-01-2014 дата публикации

POLYISOBUTYLENES AND PROCESS FOR MAKING SAME

Номер: US20140005349A1
Принадлежит: THE UNIVERSITY OF AKRON

The present invention generally relates to alcohol-terminated polyisobutylene (PIB) compounds, and to a process for making such compounds. In one embodiment, the present invention relates to primary alcohol-terminated polyisobutylene compounds, and to a process for making such compounds. In still another embodiment, the present invention relates to polyisobutylene compounds that can be used to synthesize polyurethanes, to polyurethane compounds made via the use of such polyisobutylene compounds, and to processes for making such compounds. In yet another embodiment, the present invention relates to primary alcohol-terminated polyisobutylene compounds having two or more primary alcohol termini and to a process for making such compounds. In yet another embodiment, the present invention relates to primary terminated polyisobutylene compounds having two or more primary termini selected from amine groups or methacrylate groups. 1. A primary alcohol-terminated polyisobutylene compound according to the following formula:{'br': None, 'sub': 3', '2', '2', '3', '2', 'n, '˜˜˜C(CH)—[CH—C(CH)]—R—OH'}{'sub': 3', '12', '3', '12, 'where ˜˜˜ represents the remaining portion of a linear, star, hyperbranched, or arborescent molecule, n is an integer from 2 to about 5,000, and R is a straight Cto Clinkage formed from a corresponding straight Cto Callyl group having a double bond present at the end of the allyl group, and where the primary alcohol-terminated polyisobutylene has at least two primary alcohol termini.'}2. The primary alcohol-terminated polyisobutylene compound of claim 1 , wherein n is an integer from about 7 to about 4 claim 1 ,500.3. The primary alcohol-terminated polyisobutylene compound of claim 1 , wherein n is an integer from about 100 to about 2 claim 1 ,000.4. The primary alcohol-terminated polyisobutylene compound of claim 1 , wherein n is an integer from about 250 to about 1 claim 1 ,500.5. A method for producing a primary methacrylate-terminated polyisobutylene ...

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09-01-2014 дата публикации

METHOD FOR PRODUCING CYCLIC SILANE COMPOUND OR SALT THEREOF, SALT HAVING CYCLIC SILANE DIANION, AND CYCLIC SILANE DIANION SALT-CONTAINING COMPOSITION

Номер: US20140012030A1
Принадлежит:

An object of the present invention is to provide a production method that can efficiently produce a cyclic silane compound or a salt thereof with a high yield and to provide a novel salt having a cyclic silane dianion that is easy to handle and a cyclic silane dianion salt-containing composition. The method for producing a cyclic silane compound or a salt thereof of the present invention includes the step of allowing a halosilane compound to react in the presence of at least one of a phosphonium salt and an ammonium salt, and a compound represented by a specific formula. 2. The method for producing a cyclic silane compound or a salt thereof according to claim 1 , wherein the reaction is carried out in the presence of a basic compound.3. The method for producing a cyclic silane compound or a salt thereof according to claim 1 , wherein the phosphonium salt or the ammonium salt is a quaternary phosphonium salt or a quaternary ammonium salt.7. The cyclic silane dianion salt-containing composition according to claim 6 , wherein the salt having a cyclic silane dianion represented by the general formula (vii) is contained in an amount of 1 to 10000 parts by mass claim 6 , based on the total amount of 100 parts by mass of the salt having a cyclic silane dianion represented by the general formula (vi).8. The method for producing a cyclic silane compound or a salt thereof according to claim 2 , wherein the phosphonium salt or the ammonium salt is a quaternary phosphonium salt or a quaternary ammonium salt. (1) Field of the InventionThe present invention relates to a production method that can efficiently obtain a cyclic silane compound or a salt thereof by a simple method, a novel salt having a cyclic silane dianion, and a cyclic silane dianion salt-containing composition.(2) Description of Related ArtA silane compound is widely utilized as a raw material of silicon and silica, and a water-reactive combustible gas such as monosilane and disilane is mostly used. On the other ...

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09-01-2014 дата публикации

PREPARATION OF DIAMINE VIA THE PREPARATION OF AMINONITRILE

Номер: US20140012045A1
Автор: Leconte Philippe
Принадлежит: Rhodia Operations

A continuous method (P) for preparing diamine is described. The method includes reacting the corresponding alkene nitrile with the corresponding monoamine in order to form the corresponding aminonitrile. The monoamine can be introduced in molecular excess with respect to the alkene nitrile, wherein the unreacted monoamine is recirculated to the reaction; followed by reducing the aminonitrile produced by hydrogen in the presence of at least one alkali-metal hydroxide, water, and a hydrogenation catalyst; and purifying the diamine. 1. A continuous process (P) for preparing a diamine , the process comprising the steps of:(a) reacting a corresponding alkenenitrile and a corresponding monoamine to form a corresponding aminonitrile, the monoamine being introduced in molar excess relative to the alkenenitrile, with recycling into the reaction of the unreacted monoamine;(b) reducing aminonitrile obtained in step (a) with hydrogen in the presence of at least one alkali metal hydroxide, water and a hydrogenation catalyst;(c) separating the at least one alkali metal hydroxide by evaporation of a diamine obtained in step (b) and of the water; and(d) distilling the diamine.2. The process as claimed in claim 1 , for which:the alkenenitrile is a linear or branched C2 to C4 alkene in which a hydrogen atom is replaced with a conjugated cyano group and/orthe monoamine is a secondary amine of general formula R1R2NH, in which R1 and R2, which can be identical or different, represent a C1 to C4 alkyl.3. The process as claimed in claim 1 , wherein the monoamine is dimethylamine claim 1 , the alkenenitrile is acrylonitrile claim 1 , the aminonitrile is 3-(dimethylamino)propanenitrile and the diamine is dimethylaminopropylamine.4. The process as claimed in claim 1 , wherein step (a) is performed in one or more reactors in series of piston type with recycling of the excess monoamine and recycling of some of the aminonitrile.5. The process as claimed in claim 1 , wherein in step (a) claim 1 ...

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