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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 62643. Отображено 100.
05-01-2012 дата публикации

Hydrophobic magnetic particles

Номер: US20120003689A1

A process for making a particulate material comprising mesoporous particles having granules of a metal containing species in at least some of the pores thereof, said process comprising: allowing a compound of the metal to enter pores of hydrophobic mesoporous particles, said compound being thermally decomposable at a decomposition temperature to form a metal containing species and said particles being substantially thermally stable at said decomposition temperature; and heating the hydrophobic mesoporous particles having the compound in the pores thereof to the decomposition temperature so as to decompose the compound and to form the mesoporous particles having granules of the metal containing species in at least some of the pores thereof.

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19-01-2012 дата публикации

Antistaining sheet

Номер: US20120015165A1
Автор: Noriaki Ogawa
Принадлежит: Daiwabo Holdings Co Ltd, Kanbo Pras Corp

Disclosed is an antistaining sheet including a base material sheet and an antistaining layer formed on the base material sheet. The antistaining layer includes a photocatalyst and a thermoplastic resin to be decomposed by the photocatalyst, and thus has a self-collapsing property. The antistaining layer is stronger in self-collapsing property in the surface portion thereof than in the interior portion.

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09-02-2012 дата публикации

Organophosphorus compounds, catalytic systems comprising said compounds and method of hydrocyanation or of hydroformylation using said catalytic systems

Номер: US20120035377A1
Принадлежит: Rhodia Operations SAS

Organophosphorus compounds, catalytic systems comprising a metallic element forming a complex with the organophosphorus compounds and methods of hydrocyanation and of hydroformylation employed in the presence of the catalytic systems are described.

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23-02-2012 дата публикации

Terephthalic acid purge filtration rate by controlling % water in filter feed slurry

Номер: US20120042752A1
Автор: Kenny Randolph Parker
Принадлежит: Eastman Chemical Co

The process relates improving the recovery of a metal catalyst from an oxidizer purge stream produced in the synthesis of carboxylic acid, typically terephthalic acid, while utilizing pressure filtration.

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23-02-2012 дата публикации

Method for recovery of cobalt and manganese from spent cobalt-manganese-bromine (cmb) catalyst and method for producing cmb catalyst including the recovery method

Номер: US20120046159A1

Disclosed is a method for recovering cobalt and manganese from a spent cobalt-manganese-bromine (CMB) catalyst. The method includes (a) continuously leaching a spent CMB catalyst with sulfuric acid, (b) separating the leachate into a solution and a residue, (c) extracting the solution with a solvent, and (d) washing the extract with water. According to the method, high-purity cobalt and manganese can be recovered in high yield from a spent CMB catalyst while minimizing the amount of impurities. Further disclosed is a method for producing a CMB liquid catalyst from the extract containing cobalt and manganese obtained by the recovery method.

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23-02-2012 дата публикации

Intermediates in the enantioselective synthesis of 3-(aminomethyl)-5-methyl-hexanoic acid

Номер: US20120046468A1

(S)-(+)-3-(aminomethyl)-5-methyl-hexanoic acid or (S)-pregabalin is an anticonvulsive drug. In addition to its use as an anticonvulsive agent, pregabalin has also been indicated as a medicament in the treatment of anxiety, neuropathic pain and pain in patients with fibromyalgia. Provided herein are thioester intermediates in the synthesis of and processes for the synthesis of 3-(aminomethyl)-5-methyl-hexanoic acid in the (R) or (S) configuration.

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08-03-2012 дата публикации

Process for the treatment of an ion exchange resin

Номер: US20120059073A1
Автор: Trevor Huw Morris
Принадлежит: Lucite International UK Ltd

A process for the reactivation of an acidic ion exchange resin is described. The invention relates to the treatment of an at least partially deactivated resin which has been deactivated by contact with an impure ethylenically unsaturated acid or ester containing target impurities. The reactivation includes the step of contacting the at least partially deactivated resin with an alcohol to thereby increase the activity thereof. The invention extends to reactivating a resin deactivated by contact with an impure ethylenically unsaturated acid, ester or nitrile containing target impurities by contacting the at least partially deactivated resin with an alcohol and a carboxylic acid to thereby increase the activity thereof. A reactivated resin and a process for preparing and purifying an ethylenically unsaturated acid or ester of the following formula:— R 1 —C(═(CH 2 )—COOR 2 are also described.

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15-03-2012 дата публикации

Transfer Hydrogenation of Cyclopamine Analogs

Номер: US20120065400A1
Принадлежит: Infinity Pharmaceuticals Inc

Provided herein is a process for the transfer-hydrogenation of ketone analogs of members of the jervine type of Veratrum alkaloids, such as cyclopamine. Also provided herein are novel ruthenium transfer-hydrogenation catalysts.

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22-03-2012 дата публикации

Synthesis of terminal alkenes from internal alkenes and ethylene via olefin metathesis

Номер: US20120071676A1
Автор: Yann Schrodi
Принадлежит: Elevance Renewable Sciences Inc

This invention relates generally to olefin metathesis, and more particularly relates to the synthesis of terminal alkenes from internal alkenes using a cross-metathesis reaction catalyzed by a selected olefin metathesis catalyst. In one embodiment of the invention, for example, a method is provided for synthesizing a terminal olefin, the method comprising contacting an olefinic substrate comprised of at least one internal olefin with ethylene, in the presence of a metathesis catalyst, wherein the catalyst is present in an amount that is less than about 1000 ppm relative to the olefinic substrate, and wherein the metathesis catalyst has the structure of formula (II) wherein the various substituents are as defined herein. The invention has utility, for example, in the fields of catalysis, organic synthesis, and industrial chemistry.

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12-04-2012 дата публикации

Tetramerization ligands

Номер: US20120088933A1
Принадлежит: Nova Chemicals International SA

An ethylene oligomerization catalyst which contains a bridged diphosphine ligand having the formula (R 1 ) m (X 1 ) n P 1 -bridge-P 2 (R 2 )X 2 wherein R 1 and R 2 are independently selected from the group consisting of hydrocarbyl and heterohydrocarbyl; X 1 is selected from the group consisting of halogen, hydrocarbyl and heterohydrocarbyl; m is 1 or 2; n is 0 or 1; m+n=2; bridge is a divalent bridging group bonded to P 1 and P 2 ; and X 2 is halogen. The present ligands differ from prior diphosphine ligands used in olefin oligomerization processes in that at least one halide substituent is directly bonded to at least one P atom of the ligand.

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19-04-2012 дата публикации

Process for producing middle distillates by hydroisomerization and hydrocracking of a heavy fraction derived from a fischer-tropsch effluent

Номер: US20120091034A1
Принадлежит: Eni Spa, IFP Energies Nouvelles IFPEN

The present invention describes a process for producing middle distillates from a C5+ liquid paraffinic fraction, termed a heavy fraction, with an initial boiling point in the range 15° C. to 40° C. produced by Fischer-Tropsch synthesis, comprising the following steps in succession: passing said C5+ liquid paraffinic fraction, termed a heavy fraction, over at least one ion exchange resin at a temperature in the range 80° C. to 150° C., at a total pressure in the range 0.7 to 2.5 MPa, at an hourly space velocity in the range 0.2 to 2.5 h −1 ; eliminating at least a portion of the water formed in step a); hydrogenating the unsaturated olefinic type compounds of at least a portion of the effluent derived from step b) in the presence of hydrogen and a hydrogenation catalyst; and hydroisomerization/hydrocracking of at least a portion of the hydrotreated effluent derived from step c) in the presence of hydrogen and a hydroisomerization/hydrocracking catalyst.

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26-04-2012 дата публикации

Catalytic systems for immortal ring-opening polymerisation of cyclic esters and cyclic carbonates

Номер: US20120101233A1
Принадлежит: Total Petrochemicals Research Feluy SA

The present invention discloses new catalyst systems based on complexes of divalent metals supported by chelating phenoxy ligands for immortal ring-opening polymerisation of cyclic esters and cyclic carbonates.

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10-05-2012 дата публикации

Organic chlorohydrosilane and method for preparing them

Номер: US20120114544A1
Принадлежит: Samsung Fine Chemicals Co Ltd

Provided is an organic chlorohydrosilane, a useful starting material for preparing silicon polymers and a method for preparing the same. More particularly, the present invention enables the synthesis of various novel organic chlorohydrosilanes in high yield by an exchange reaction between an Si—H bond of a chlorosilane which can be obtained in an inexpensive and easy manner and an Si—Cl bond of an another organic chlorosilane using a quaternary organic phosphonium salt compound as a catalyst. Since the catalyst can be recovered after its use and reused, the present invention is very economical and thus effective for mass-producing silicon raw materials.

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10-05-2012 дата публикации

Metal organic framework compounds

Номер: US20120115961A1
Принадлежит: Universitetet I Oslo

The invention provides novel Zr MOFs, in particular compounds having a surface area of at least 1020 m 2 /g or if functionalized, having a surface area of at least 500 m 2 /g.

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10-05-2012 дата публикации

Solution polymerization process and procatalyst carrier systems useful therein

Номер: US20120116034A1
Принадлежит: Dow Global Technologies LLC

A procatalyst carrier system which includes one or more paraffinic solvents, one or more paraffin-insoluble procatalysts, and optionally one or more cocatalysts wherein the carrier system is in the form of a slurry is provided. Also provided is a process including selecting one or more paraffin-insoluble organometallic procatalysts; adding the one or more procatalysts to a sufficient quantity of paraffinic solvent to form a slurry of the one or more procatalysts in the paraffinic solvent; introducing one or more first cocatalysts into a polymerization reactor; and introducing the slurry into the polymerization reactor; a reaction product of the process and articles made from the reaction product.

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17-05-2012 дата публикации

Hydroconversion multi-metallic catalyst and method for making thereof

Номер: US20120122659A1
Принадлежит: Chevron USA Inc

In a process for forming a bulk hydroprocessing catalyst by sulfiding a catalyst precursor made in a co-precipitation reaction, up to 60% of the metal precursor feeds end up in the supernatant. The metals can be recovered via any of chemical precipitation, ion exchange, electro-coagulation, and combinations thereof to generate an effluent stream containing less than 50 mole % of metal ions in at least one of the metal residuals, and for at least one of the metal residuals recovered as a metal precursor feed for use in the co-precipitation reaction. In one embodiment, the resin functions as an anion exchange resin with an acidic supernatant to recover Group VIB metal residuals, and a cation exchange resin with a basic supernatant to recover Promoter metal residuals. An effluent stream from the process to waste treatment contains less than 50 ppm metals.

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17-05-2012 дата публикации

Methane aromatization catalyst, method of making and method of using the catalyst

Номер: US20120123176A1
Принадлежит: Shell Oil Co

A catalyst for converting methane to aromatic hydrocarbons is described herein. The catalyst comprises an active metal or a compound thereof, and an inorganic oxide support wherein the active metal is added to the support in the form of metal oxalate. The metal oxalate-derived catalyst exhibits superior performance in the conversion of methane-rich feed to aromatics products relative to catalysts prepared from non-oxalate metal precursors. A method of making the catalyst and a method of using the catalyst are also described.

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24-05-2012 дата публикации

Highly Active and Selective Ethylene Oligomerization Catalyst and Method of Preparing Hexene or Octene Using the Same

Номер: US20120130086A1

This invention relates to a chromium complex compound for selective ethylene oligomerization including a chiral ligand, and to a method of selectively preparing 1-hexene or 1-octene from ethylene using the same.

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31-05-2012 дата публикации

Process

Номер: US20120136165A1
Принадлежит: SOUTH BANK UNIVERSITY ENTERPRISES LTD

The present invention provides a continuous process for the epoxidation of an olefinic compound with an oxidant, which process comprises reaction of an olefinic compound with an oxidant in the presence of a catalyst in an apparatus that comprises a reactive distillation column, which column comprises (i) a reactive section, which comprises the catalyst (ii) a rectifying section situated above the reactive section and adapted to allow separation of reagents and/or by-products from products (ix) a stripping section situated below the reactive section and adapted to allow separation of product from reagents and/or by-products (x) a vessel situated below the stripping section and adapted to provide a source of heat for the column and in which initial vaporisation of one or more of the reagents can occur, wherein the temperature in the reactive section (i) is a temperature at which the reaction between the olefinic compound and the oxidant takes place and the temperature in the stripping section (iii) is higher than the temperature in the rectifying section (ii).

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31-05-2012 дата публикации

Imprinted Biomimetic Catalysts for Cellulose Hydrolysis

Номер: US20120136180A1
Автор: Daeyeon Lee, Stephen Roth
Принадлежит: University of Pennsylvania Penn

The present disclosure describes methods and biomimetic catalysts useful for hydrolyzing glucose polymers, such as cellulose, and oligomers, such as cellobiose, to glucose for the subsequent production of ethanol.

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07-06-2012 дата публикации

Removal of light fluoroalkanes from hydrocarbon streams

Номер: US20120142792A1
Принадлежит: ExxonMobil Research and Engineering Co

The removal of fluoroalkanes from fluoroalkane-containing hydrocarbon streams, preferably C 3 to C 5 hydrocarbon streams. The fluoroalkane-containing hydrocarbon stream is contacted with an adsorbent containing a strong acid function, preferably a silica gel or a strong cation ion-exchange resin having sulfonic acid functionality.

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28-06-2012 дата публикации

Synthesis of fluorocarbofunctional alkoxysilanes and chlorosilanes

Номер: US20120165565A1

The subject of invention is the method of synthesis of fluorocarbofunctional alkoxysilanes and chlorosilanes of the general formula HCF 2 (CF 2 ) n (CH 2 ) m OC 3 H 7 SiR 1 R 2 R 3 in which -n takes values from 1 to 12, m takes values from 1 to 4,—R 1 stands for an alkoxy group or halogen, if R 1 stands for an alkoxy group, then R 2 and R 3 can be the same or different and stand for an alkoxy group containing C=1-4, alkyl group containing C=1-12 or an aryl group, if R 1 stands for a halogen, then R 2 and R 3 can be the same or different and stand for based on hydrosilylation of an appropriate fluoroalkyl-allyl ether with an appropriate trisubstituted silane of the general formula HSiR 1 R 2 R 3 in the presence of siloxide rhodium complex [{Rh(OSiMe 3 )(cod)} 2 ] as a catalyst.

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05-07-2012 дата публикации

Compositions comprising functionalized carbon-based nanostructures and related methods

Номер: US20120171093A1
Принадлежит: Massachusetts Institute of Technology

The present invention generally relates to compositions comprising and methods for forming functionalized carbon-based nanostructures.

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05-07-2012 дата публикации

Zinc cluster

Номер: US20120172601A1
Принадлежит: Takasago International Corp

Disclosed is a novel zinc cluster compound represented by general formula (1): Zn 4 O (OCOR) 6 (RCOOH) n , wherein R represents an alkyl group which has 1 to 4 carbon atoms and may be substituted with a halogen atom, and n represents 0.1 to 1, and also disclosed are a method for producing the compound and a reaction using the compound.

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26-07-2012 дата публикации

Process for producing diphenyl carbonate

Номер: US20120190878A1
Автор: J. Yong Ryu
Принадлежит: Shell Oil Co

Processes for producing diaryl carbonates are disclosed, where such processes may provide for the production of diaryl carbonates from green house gases, such as carbon dioxide. The processes disclosed advantageously integrate diethyl carbonate and diaryl carbonate production, eliminating the need for solvent-based extractive distillation, as is commonly required when producing diaryl carbonates from dimethyl carbonate, providing for the integration of separation equipment and raw material usage, and reducing the operating and capital requirements for such processes. In some embodiments, processes disclosed herein may be operated essentially closed-loop with respect to ethanol usage, for example.

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09-08-2012 дата публикации

Method for manufacturing catalyst

Номер: US20120203048A1
Принадлежит: Mitsubishi Chemical Corp

A method for manufacturing a catalyst, which comprises regenerating a catalyst comprising a zeolite as an active ingredient and having an ethylene conversion lowered through reaction of producing propylene by bringing into contact with ethylene in a vapor phase, by bringing the catalyst into contact with a gas which does not comprise oxygen and comprises hydrogen having a hydrogen partial pressure of 0.01 MPa or more as an absolute pressure thereof.

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23-08-2012 дата публикации

Preparation of metal-catecholate frameworks

Номер: US20120215015A1
Принадлежит: UNIVERSITY OF CALIFORNIA

The disclosure provides for metal catecholate frameworks, and methods of use thereof, including gas separation, gas storage, catalysis, tunable conductors, supercapacitors, and sensors.

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30-08-2012 дата публикации

Molecular Molybdenum Persulfide and Related Catalysts for Generating Hydrogen from Water

Номер: US20120217169A1
Принадлежит: UNIVERSITY OF CALIFORNIA

New metal persulfido compositions of matter are described. :In one embodiment the metal is molybdenum and the metal persulfido complex mimics the structure and function of the triangular active edge site fragments of MoS 2 , a material that is the current industry standard for petroleum hydro desulfurization, as well as a promising low-cost alternative to platinum for electrocatalytic hydrogen production. This molecular [(PY5W 2 )MoS 2 ] x+ containing catalyst is capable of generating hydrogen from acidic-buffered water or even seawater at very low overpotentials at a turnover frequency rate in excess of 500 moles H 2 per mole catalyst per second, with a turnover number (over a 20 hour period) of at least 19,000,000 moles H 2 per mole of catalyst.

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04-10-2012 дата публикации

Methods For Coating Ceramic Catalyst Supports With Base Coatings And Ceramic Catalyst Supports Having Base Coatings

Номер: US20120252664A1
Принадлежит: Corning Inc

The disclosure relates to methods for coating ceramic catalyst supports with a base coating, said method comprising, in part, providing an aqueous mixture comprising at least one polyvinyl alcohol homopolymer and at least one blocked isocyanate crosslinker, and to ceramic catalyst supports having a base coating comprising at least one polyvinyl alcohol homopolymer and at least one blocked isocyanate crosslinker.

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25-10-2012 дата публикации

Catalysts

Номер: US20120271016A1
Принадлежит: Oxford University Innovation Ltd

The present invention relates to novel metallocene catalysts of formula I, which is defined herein. The present invention also provides processes for making these catalysts and their use in olefin polymerisation reactions.

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25-10-2012 дата публикации

Process for the dehydration of aqueous bio-derived terminal alcohols to terminal alkenes

Номер: US20120271089A1
Автор: Michael E. Wright
Принадлежит: US Department of Navy

A method and apparatus for dehydrating bio-1-alcohols to bio-l-alkenes with high selectivity. The bio-1-alkenes are useful in preparing high flashpoint diesel and jet biofuels which are useful to civilian and military applications. Furthermore, the bio-1-alkenes may be converted to biolubricants useful in the transporation sector and other areas requiring high purity/thermally stable lubricants.

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22-11-2012 дата публикации

Oil and polar additive impregnated composition useful in the catalytic hydroprocessing of hydrocarbons, a method of making such catalyst, and a process of using such catalyst

Номер: US20120295786A1
Принадлежит: Shell Oil Co

A composition that comprises a support material having incorporated therein a metal component and impregnated with both hydrocarbon oil and a polar additive. The composition that is impregnated with both hydrocarbon oil and polar additive is useful in the hydrotreating of hydrocarbon feedstocks, and it is especially useful in applications involving delayed feed introduction whereby the composition is first treated with hot hydrogen, and, optionally, with a sulfur compound, prior to contacting it with a hydrocarbon feedstock under hydrodesulfurization process conditions.

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22-11-2012 дата публикации

Method for producing formic acid

Номер: US20120295991A1
Принадлежит: Individual

An object of the present invention is providing a method for producing formic acid under mild reaction conditions and by a simple procedure. As a means for achieving the object, the method for producing formic acid of the present invention is characterized by a reaction between carbon dioxide and hydrogen in the presence of an ionic liquid. According to the present invention, it is possible to generate formic acid effectively, because the method does not require that carbon dioxide be brought into a supercritical state and because no basic substances are required to be added to the reaction system.

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22-11-2012 дата публикации

Methods for monitoring ionic liquids using vibrational spectroscopy

Номер: US20120296145A1
Автор: Howard Steven Lacheen
Принадлежит: Chevron USA Inc

Methods for monitoring ionic liquids using vibrational spectroscopy may involve contacting an infrared (IR) transmissive medium with the ionic liquid, recording an IR spectrum of the ionic liquid, and quantifying at least one chemical characteristic of the ionic liquid based on the IR spectrum. The IR spectrum may be recorded ex situ or in situ. Methods for controlling ionic liquid catalyzed processes are also disclosed, wherein a condition of the ionic liquid may be determined during such processes based on IR spectral analysis of the ionic liquid.

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29-11-2012 дата публикации

Magnesium halide adducts, catalyst components and catalysts comprising the same, and preparation processes thereof

Номер: US20120302708A1

A magnesium halide adduct is provided, comprising at least one compound of the formula MgXY, at least one compound of the formula ROH, methanol, at least one modifying agent chosen from DOE and o-hydroxy benzoates, and optionally water. Also provided herein are a catalyst component comprising the magnesium halide adduct, a catalyst for olefin polymerization comprising the catalyst component; the respective processes for preparing the magnesium halide adduct and the catalyst component; use of the magnesium halide adduct for preparing the catalyst component, use of the catalyst component in a catalyst for olefin polymerization and use of the catalyst in olefin polymerization; and a process of olefin polymerization.

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06-12-2012 дата публикации

Magnetic catalyst

Номер: US20120309612A1

Disclosed is a magnetic catalyst formed by a single or multiple nano metal shells wrapping a carrier, wherein at least one of the metal shells is iron, cobalt, or nickel. The magnetic catalyst with high catalyst efficiency can be applied in a hydrogen supply device, and the device can be connected to a fuel cell. Because the magnetic catalyst can be recycled by a magnet after generating hydrogen, the practicability of the noble metals such as Ru with high catalyst efficiency is dramatically enhanced.

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27-12-2012 дата публикации

Method for producing substituted fluorine-containing olefin

Номер: US20120330072A1
Принадлежит: Daikin Industries Ltd, Osaka University NUC

This invention relates to a method of reacting fluoroolefin with an organic magnesium compound in the presence of a catalyst comprising nickel or palladium so as to efficiently produce fluoroolefin, such as TFE, in which a fluorine (F) atom or atoms bonded to the sp 2 hybridized carbon atom are substituted with an organic group.

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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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17-01-2013 дата публикации

Frustrated Lewis Pair Compositions

Номер: US20130018207A1
Принадлежит: Stephan Consulting Corp

A compound having the formula (I) where each of R 1 , R 2 , R 3 and R 4 is independently C 6 -C 18 aryl-, C 5 -C 8 cycloalkyl-, C 6 -C 18 aryl having at least one C 1 -C 20 alkyl substituent, C 5 -C 8 cycloalkyl having at least one C 1 -C 20 alkyl sυbstituent, C 4 -C 20 branched alkyl-, C 16 -C 20 linear alkyl-, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof: and R 5 is C 6 -C 18 aryl-, C 5 -C 8 cycloalkyl-, C 6 -C 18 aryl having at least one C 1 -C 20 alkyl substituent, C 5 -C 8 cycloalkyl having at least one C 1 -C 20 alkyl substituent, C 3 -C 20 branched alkyl-, C 2 -C 30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; where R and R′ are each independently C 6 -C 18 aryl-, C 5 -C 8 cycloalkyl-, C 6 -C 18 aryl having at least one C 1 -C 20 alkyl substituent, C 5 -C 8 cycloalkyl having at least one C 1 -C 20 alkyl substituent, C 4 -C 20 branched alkyl-, C 2 -C 30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; A is N, P, S, or O with the proviso that when A is S, R 2 is a nullity; and M is B, Al, Ga or In.

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24-01-2013 дата публикации

Catalysts based on heterocyclic-8-anilinoquinoline ligands

Номер: US20130023635A1
Принадлежит: EQUISTAR CHEMICALS LP

A catalyst system useful for polymerizing olefins is disclosed. The catalyst system comprises an activator and a Group 4 metal complex. The complex incorporates a dianionic, tridentate heterocyclic-8-anilinoquinoline ligand. In one aspect, a supported catalyst system is prepared by first combining a boron compound having Lewis acidity with excess alumoxane to produce an activator mixture, followed by combining the activator mixture with a support and the dianionic, tridentate Group 4 metal complex. The Group 4 metal complexes are easy to synthesize, support, and activate, and they enable facile production of high-molecular-weight polyolefins.

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14-02-2013 дата публикации

Propylene-based polymer, articles, and process for producing same

Номер: US20130041113A1
Принадлежит: Linfeng Chen, William G. Sheard

Disclosed are propylene-based polymer compositions and processes for producing same. Polymerization with an improved catalyst composition provides a propylene-based polymer with improved stiffness.

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21-02-2013 дата публикации

Polymeric acid catalysts and uses thereof

Номер: US20130042859A1
Принадлежит: Midori Renewables Inc

Polymers useful as catalysts in non-enzymatic saccharification processes are provided. Provided are also methods for hydrolyzing cellulosic materials into monosaccharides and/or oligosaccharides using these polymeric acid catalysts.

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21-02-2013 дата публикации

Method of preparing a polymer and compositions therefor

Номер: US20130046066A1
Принадлежит: JOHNSON MATTHEY PLC

The invention provides a method of making a polymer in the presence of a catalyst composition having an empirical formula M(glycerol) a (X) b , where M represents a metal atom selected from titanium, zirconium, hafnium or aluminium, X is a ligand derived from acetylacetone or a peroxo ion; a is a number between 1 and 2.5; b is a number in the range from 1 to 2. Reactive compositions containing the catalyst composition are also described.

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28-02-2013 дата публикации

Polymerization Process for Producing Bimodal Polymers

Номер: US20130053523A1
Принадлежит: Chevron Phillips Chemical Co LP

Catalyst compositions comprising a first metallocene compound, a second metallocene compound, an activator-support, and an organoaluminum compound are provided. An improved method for preparing cyclopentadienyl complexes used to produce polyolefins is also provided.

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28-02-2013 дата публикации

Gas separations with redox-active metal-organic frameworks

Номер: US20130053585A1
Принадлежит: UNIVERSITY OF CALIFORNIA

Fe 2 (dobdc) has a metal-organic framework with a high density of coordinatively-unsaturated Fe II centers lining the pore surface. It can be effectively used to separate O 2 from N 2 and in a number of additional separation applications based on selective, reversible electron transfer reactions. In addition to being an effective O 2 separation material, it can be used for many other processes, including paraffin/olefin separation, nitric oxide/nitrous oxide separation, acetylene storage, and as an oxidation catalyst.

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14-03-2013 дата публикации

Hydroisomerization and selective hydrogenation of feedstock in ionic liquid-catalyzed alkylation

Номер: US20130066121A1
Принадлежит: Chevron USA Inc

A process for producing alkylate comprising contacting a first hydrocarbon stream comprising at least one olefin having from 2 to 6 carbon atoms which contains 1,3-butadiene and 1-butene with a hydroisomerization catalyst in the presence of hydrogen under conditions favoring the simultaneous selective hydrogenation of 1,3-butadiene to butenes and the isomerization of 1-butene to 2-butene and contacting the resulting stream and a second hydrocarbon stream comprising at least one isoparaffin having from 3 to 6 carbon atoms with an acidic ionic liquid catalyst under alkylation conditions to produce an alkylate is disclosed.

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21-03-2013 дата публикации

CATALYST CONTAINING OXYGEN TRANSPORT MEMBRANE

Номер: US20130072374A1
Принадлежит:

A composite oxygen transport membrane having a dense layer, a porous support layer and an intermediate porous layer located between the dense layer and the porous support layer. Both the dense layer and the intermediate porous layer are formed from an ionic conductive material to conduct oxygen ions and an electrically conductive material to conduct electrons. The porous support layer has a high permeability, high porosity, and a microstructure exhibiting substantially uniform pore size distribution as a result of using PMMA pore forming materials or a bi-modal particle size distribution of the porous support layer materials. Catalyst particles selected to promote oxidation of a combustible substance are located in the intermediate porous layer and in the porous support adjacent to the intermediate porous layer. The catalyst particles can be formed by wicking a solution of catalyst precursors through the porous support toward the intermediate porous layer. 1. A composite oxygen transport membrane , said composite oxygen transport membrane comprising:{'b': '20', 'a porous support layer comprised of an fluorite structured ionic conducting material having a porosity of greater than percent and a microstructure exhibiting substantially uniform pore size distribution throughout the porous support layer;'}an intermediate porous layer capable of conducting oxygen ions and electrons to separate oxygen from an oxygen containing feed, the intermediate porous layer applied adjacent to the porous support layer and comprising a mixture of a fluorite structured ionic conductive material and electrically conductive materials to conduct the oxygen ions and electrons, respectively;a dense layer capable of conducting oxygen ions and electrons to separate oxygen from an oxygen containing feed, the dense layer applied adjacent to the intermediate porous layer and also comprising a mixture of a fluorite structured ionic conductive material and electrically conductive materials to ...

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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

METHOD AND SYSTEM FOR FORMING PLUG AND PLAY METAL CATALYSTS

Номер: US20130079216A1
Принадлежит: SDCmaterials, Inc.

A metal catalyst is formed by vaporizing a quantity of metal and a quantity of carrier forming a vapor cloud. The vapor cloud is quenched forming precipitate nanoparticles comprising a portion of metal and a portion of carrier. The nanoparticles are impregnated onto supports. The supports are able to be used in existing heterogeneous catalysis systems. A system for forming metal catalysts comprises means for vaporizing a quantity of metals and a quantity of carrier, quenching the resulting vapor cloud and forming precipitate nanoparticles comprising a portion of metals and a portion of carrier. The system further comprises means for impregnating supports with the nanoparticles. 1. A method of making a metal catalyst comprising:a. providing a quantity of nanoparticles, wherein at least some of the nanoparticles comprise a first portion comprising catalyst material bonded to a second portion comprising a carrier;b. providing a quantity of supports; andc. combining the supports with the nanoparticles.2. The method of wherein the supports comprise pores and voids.3. The method of wherein the catalyst material comprises any among a list of at least one metal claim 1 , at least one metal alloy claim 1 , and any combination thereof.4. The method of wherein providing a quantity of nanoparticles comprises:a. loading a quantity of catalyst material and a quantity of carrier into a plasma gun in a desired ratio;b. vaporizing the quantity of catalyst material and quantity of carrier thereby forming a vapor cloud; andc. quenching the vapor cloud, thereby forming a quantity of nanoparticles.5. The method of wherein the carrier comprises an oxide.6. The method of wherein the oxide comprises silica claim 5 , alumina claim 5 , yttria claim 5 , zirconia claim 5 , titania claim 5 , ceria claim 5 , baria claim 5 , and any combination thereof.7. The method of wherein combining the supports with the nanoparticles comprises:a. suspending the nanoparticles in a solution, thereby forming a ...

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28-03-2013 дата публикации

Novel materials as additives for advanced lubrication

Номер: US20130079262A1
Принадлежит: UChicago Argonne LLC

This invention relates to carbon-based materials as anti-friction and anti-wear additives for advanced lubrication purposes. The materials have various shapes, sizes, and structures and are synthesized by autogenic reactions under extreme conditions of high temperature and pressure. The lubricant compositions comprise carbon-based particles suspended in a liquid hydrocarbon carrier. Optionally, the compositions further comprise a surfactant (e.g., to aid in dispersion of the carbon particles). Specifically, the novel lubricants have the ability to significantly lower friction and wear, which translates into improved fuel economies and longer durability of mechanical devices and engines.

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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

Synthesis of Alkyl Cyclopentadiene Compounds

Номер: US20130085289A1
Принадлежит: UNIVATION TECHNOLOGIES, LLC

A method of synthesizing an alkyl cyclopentadiene compound is disclosed. The method includes contacting at least one cyclopentadienyl anion source and at least one alkyl group source to form at least one alkyl cyclopentadiene compound. The method further includes extracting the alkyl cyclopentadiene compound with a hydrocarbon solvent. The alkyl cyclopentadiene compound may be converted to a metallocene catalyst compound. 1. A method of synthesizing at least one alkyl cyclopentadiene compound comprising:contacting at least one cyclopentadienyl anion source and at least one alkyl group source to form at least one alkyl cyclopentadiene compound; andextracting the alkyl cyclopentadiene compound with a hydrocarbon solvent.2. The method of wherein the cyclopentadienyl anion source comprises at least one reagent selected from group consisting of a cyclopentadienyl Grignard reagent claim 1 , sodium cyclopentadienyl claim 1 , lithium cyclopentadienyl claim 1 , potassium cyclopentadienyl claim 1 , and any combination thereof.3. The method of or wherein the cyclopentadienyl anion source comprises a cyclopentadienyl Grignard reagent.4. The method of any preceding claim wherein the alkyl group source comprises at least one reagent selected from the group consisting of an alkyl halide and an alkyl sulfonate.5. The method of any preceding claim wherein a mole ratio of the alkyl group source to the cyclopentadienyl anion source is less than 1:1.6. The method of any preceding claim wherein a mole ratio of the alkyl group source to the cyclopentadienyl anion source is in the range of from 0.5:1 to 1:1.7. The method of any preceding claim wherein the alkyl cyclopentadiene compound comprises a Cto Calkyl group.8. The method of any preceding claim wherein the alkyl cyclopentadiene compound comprises an alkyl group substituted with one or more heteroatoms or one or more heteroatom-containing groups.9. The method of any preceding claim wherein the alkyl cyclopentadiene compound comprises ...

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11-04-2013 дата публикации

TRANSESTERIFICATION PROCESS USING MIXED SALT ACETYLACETONATES CATALYSTS

Номер: US20130090492A1
Принадлежит: ECOSYNTH BVBA

This invention is directed to a general catalyst of high activity and selectivity for the production of a variety of esters, particularly acrylate and methacrylate-based esters, by a transesterification reaction. This objective is achieved by reaction of an ester of a carboxylic or a carbonic acid, in particular of a saturated or unsaturated, typically, a 3 to 4 carbon atom carboxylic acid; with an alcohol in the presence of a catalyst comprising the combination of a metal 1,3-dicarbonyl complex (pref. Zn or Fe acetylacetonate) and a salt, in particular an inorganic salt, pref. ZnCl2, LiCI, NaCI, NH4CI or Lil. These catalysts are prepared from readily available starting materials within the reaction medium without the need for isolation (in-situ preparation). 1. A process for the transesterification of an ester of a carboxylic or a carbonic acid , comprising reacting the ester of the carboxylic or carbonic acid with an alcohol in the presence of a catalyst consisting of a mixture of a Zn or Fe 1 ,3-dicarbonyl complex and an inorganic salt.4. The process according to claim 2 , wherein R″ is alkyl; substituted alkyl; cycloalkyl; alkoxyalkyl; alkylpolyalkoxyalkyl; alkylphenoxyalkyl; alkylpolyphenoxyalkyl; phenylalkyl; alkylphenylalkyl; alkylmorpholinoalkyl; alkylpiperidinoalkyl; haloalkyl; cyanoalkyl; alkylthioalkyl; alkylimidazolidinones; mono- or di-alkyl-aminoalkyl; alkyl oxazolidines; hydroxy alkyl claim 2 , hydroxybutyl; and alkyls derived from ethylene glycol claim 2 , butanediol claim 2 , and polyoxyethyleneols.5. The process according to wherein the alcohol (R″OH) is selected from the group consisting of butanol claim 1 , pentanol claim 1 , isodecyl claim 1 , lauryl claim 1 , cetyl claim 1 , stearyl claim 1 , alkyl ether of polyoxyethylene claim 1 , dimethylaminoethanol claim 1 , 2-N-oxazolidinyl)ethyl claim 1 , 2-(N-morpholino)ethyl claim 1 , and dicyclopentenyloxyethyl.7. (canceled)8. The process of wherein the salt contains an inorganic cation selected from ...

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18-04-2013 дата публикации

Chiral Heterogeneous Catalyst for Assymmetric Nitroaldol Reaction

Номер: US20130096333A1

The present invention relates to the preparation of highly efficient chiral heterogeneous catalyst for asymmetric nitroaldol reaction, wherein Henry reactions of various aldehydes such as aromatic, aliphatic, α,β-unsaturated aldehydes, alicyclic aldehydes and nitroalkenes were carried out to produce optically active β-nitroalcohols in high yield, with moderate to excellent enantioselectivity (ee up to >99%) in presence of a base and an optically active chiral heterogeneous catalyst. 2. A chiral heterogeneous catalyst of formula 1 as claimed in claim 1 , wherein mesoporous silica used is selected from the group consisting of silica gel claim 1 , Mobile Crystalline Materials (MCM-41) claim 1 , Santa Barbara Amorphous (SBA-15) and Meso Cellular Foams (MCF) having porosity in the range of 30 to 120 Å.3. A chiral heterogeneous catalyst of formula 1 as claimed in claim 1 , wherein catalysts of formula 1 are represented as (S)-aminopropyl alcohol-copper-support-41 claim 1 , (R)-aminopropyl alcohol-copper-support-41 claim 1 , (S)-aminopropyl alcohol-copper-support-15 claim 1 , (R)-aminopropyl alcohol-copper-support-15 claim 1 , (S)-aminopropyl alcohol-copper-support-MCF claim 1 , (R)-aminopropyl alcohol-copper-support-Mesocellular Foams (MCF) claim 1 , (S)-aminopropyl alcohol-copper-support-Mesocellular Foams (MCF) claim 1 , (R)-aminopropyl alcohol-copper-support-Mesocellular Foams (MCF) claim 1 , (S)—N-methyl aminopropyl alcohol-copper-support-41 claim 1 , (R)—N-methyl aminopropyl alcohol-copper-support-41 claim 1 , (S)—N claim 1 ,N′-dimethyl aminopropyl alcohol-copper-support-41 claim 1 , (S)—N claim 1 ,N′-dimethyl aminopropyl alcohol-copper-support-15 claim 1 , (S)—N-methyl aminopropyl alcohol-copper-support-15 claim 1 , (S)-aminopropyl alcohol-copper-support-silicagel and (R)-aminopropyl alcohol-copper-support-silicagel.4. A process for the preparation of chiral heterogeneous catalyst of formula 1 as claimed in claim 1 , wherein the said process comprises of steps:i. ...

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18-04-2013 дата публикации

Magnetic Nanoparticle-Supported Glutathione as a Sustainable Organocatalyst

Номер: US20130096334A1

This invention relates to the use of nano-organocatalysts, and, more specifically, to the use of magnetic nanomaterial-supported organocatalysts. It is an object of the present invention to provide “green” catalysts and protocols. According to one embodiment of the invention, a nano-organocatalyst in the form of a magnetic nanomaterial-supported organocatalyst is provided. According to other embodiments of the invention, glutathione and cysteine are provided as organocatalysts and magnetic nanomaterial-supported glutathione and magnetic nanomaterial-supported cysteine are provided for use as nano-organocatalysts. According to another embodiment of the invention, a method of using a recyclable magnetic nanomaterial-supported organocatalyst using a totally benign aqueous protocol, without using any organic solvent in the reaction or during the workup, is provided. According to a further embodiment of the invention, a recyclable magnetic nanomaterial-supported organocatalyst for various organocatalytic reactions, including but not limited to Paal-Knorr reactions, aza-Michael addition and pyrazole synthesis, is provided. 1. A nano-organocatalyst comprising a magnetic nanomaterial-supported organocatalyst , wherein an organocatalyst comprises a compound having a thiol group and wherein the organocatalyst is anchored to a magnetic nanomaterial through the thiol group.2. The nano-organocatalyst of claim 1 , wherein the organocatalyst is selected from the group consisting of glutathione and cysteine.3. The nano-organocatalyst of claim 1 , wherein the magnetic nanomaterial is selected from the group consisting of nano-ferrite claim 1 , nano-nickel ferrite claim 1 , nano-cobalt ferrite claim 1 , nano-iron claim 1 , and nano-cobalt and their bimetallic derivatives.4. A nano-organocatalyst comprising magnetic nanomaterial-supported glutathione claim 1 , wherein glutathione is anchored to magnetic nanomaterial. The present application is a division of commonly assigned U.S. ...

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25-04-2013 дата публикации

Nanoparticles and nanoparticle compositions

Номер: US20130101516A1
Автор: YAN Zhao

The invention provides multivalent surface-crosslinked micelle (SCM) particles, crosslinked reverse micelle (CRM) particles, and methods of making and using them. The SCM particles can be used, for example, to inhibit a virus or bacteria from binding to a host cell. The inhibition can be used in therapy for the flu, cancer, or AIDS. The CRM particles can be used, for example, to prepare metal nanoparticles or metal alloy nanoparticles, or they can be used in catalytic reactions.

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25-04-2013 дата публикации

Catalytic adsorbents obtained from municipal sludges, industrial sludges, compost and tobacco waste and process for their production

Номер: US20130102456A1
Автор: Teresa J. Bandosz

Industrial waste derived adsorbents were obtained by pyrolysis of sewage sludge, metal sludge, waste oil sludge and tobacco waste in some combination. The materials were used as media to remove hydrogen sulfide at room temperature in the presence of moisture. The initial and exhausted adsorbents after the breakthrough tests were characterized using sorption of nitrogen, thermal analysis, XRD, ICP, and surface pH measurements. Mixing tobacco and sludges result in a strong synergy enhancing the catalytic properties of adsorbents. During pyrolysis new mineral phases are formed as a result of solid state reaction between the components of the sludges. High temperature of pyrolysis is beneficial for the adsorbents due to the enhanced activation of carbonaceous phase and chemical stabilization of inorganic phase. Samples obtained at low temperature are sensitive to water, which deactivates their catalytic centers.

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02-05-2013 дата публикации

PARTICLES, PARTICLE DISPERSION, PARTICLE-DISPERSED RESIN COMPOSITION, PRODUCING METHOD THEREFOR, RESIN MOLDED ARTICLE, PRODUCING METHOD THEREFOR, CATALYST PARTICLES, CATALYST SOLUTION, CATALYST COMPOSITION, CATALYST MOLDED ARTICLE, TITANIUM COMPLEX, TITANIUM OXIDE PARTICLES AND PRODUCING METHOD THEREFOR

Номер: US20130109770A1
Принадлежит: NITTO DENKO CORPORATION

Organic-inorganic composite particles that can be dispersed in a solvent and/or a resin as primary particles having an organic group on the surface of inorganic particles, the organic-inorganic composite particles having negative birefringence. 110-. (canceled)11. Organic-inorganic composite particles that can be dispersed in a solvent and/or a resin as primary particles having an organic group on the surface of inorganic particles , the organic-inorganic composite particles having negative birefringence.12. The particles according to claim 11 , wherein the inorganic particles comprise a carbonate containing an alkaline earth metal and/or a composite oxide containing an alkaline earth metal.13. The particles according to claim 11 , wherein the primary particles are obtained by surface-treating the inorganic particles with an organic compound claim 11 , andthe organic compound contains a binding group capable of binding to the surface of the inorganic particles and a hydrophobic group and/or a hydrophilic group serving as the organic group.14. The particles according to claim 11 , having an aspect ratio of 1000 or less.15. The particles according to claim 11 , having a maximum length of 200 μm or less.16. The particles according to claim 11 , obtained by hydrothermal synthesis.17. The particles according to claim 16 , wherein an inorganic compound for forming inorganic particles and the organic compound are subjected to a hydrothermal synthesis.18. The particles according to claim 16 , wherein a metal hydroxide containing an alkaline earth metal claim 16 , a carbonic acid source and the organic compound are subjected to a hydrothermal synthesis.19. The particles according to claim 18 , wherein the carbonic acid source is formic acid and/or urea.20. The particles according to claim 16 , wherein a metal hydroxide containing an alkaline earth metal claim 16 , a metal complex and the organic compound are subjected to a hydrothermal synthesis.21. The particles according ...

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09-05-2013 дата публикации

Accelerator Mixture for Peroxide Hardener and Two-Component Mortar System Containing Same

Номер: US20130112432A1
Автор: BUERGEL Thomas
Принадлежит: Hilti Aktiengesellschaft

An accelerator mixture for peroxide hardeners, in particular an accelerator mixture for an organic peroxide-curing resin mixture, a two-component mortar system containing the same for chemical fastening and use of the same for chemical fastening of anchoring elements in boreholes are disclosed. Using a mixture of bis-N-substituted p-toluidines with bis-N-substituted anilines or bis-N-substituted m-toluidines, it is possible to provide a mortar composition for chemical fastening of anchoring elements in boreholes, which will have an improved low-temperature curing and improved load ratings at high temperatures with an extended gel time. 2. The accelerator mixture according to claim 1 , wherein the main accelerator (I) is N claim 1 ,N-bis(2-hydroxyethyl)-p-toluidine claim 1 , N claim 1 ,N-bis(2-hydroxypropyl)-p-toluidine or an ethoxylated or propoxylated derivative thereof.3. The accelerator mixture according to claim 1 , wherein the co-accelerator (II) is N claim 1 ,N-diethylaniline claim 1 , N claim 1 ,N-bis(2-hydroxyethyl)aniline claim 1 , N-ethyl-N-hydroxyethylaniline claim 1 , N claim 1 ,N-bis(2-hydroxyethyl)-m-toluidine or N claim 1 ,N-bis(2-hydroxypropyl)-m-toluidine.4. The accelerator mixture according to claim 3 , wherein the main accelerator (I) is N claim 3 ,N-bis(2-hydroxypropyl)-p-toluidine and the co-accelerator (II) is N claim 3 ,N-bis(2-hydroxyethyl)-m-toluidine.5. The accelerator mixture according to claim 1 , wherein a molar ratio of the main accelerator (I) to the co-accelerator (II) is 3:1.6. A resin mixture claim 1 , comprising:a radically polymerizable compound;{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'an accelerator according to ; and'}optionally an inhibitor and a reactive diluent.7. The resin mixture according to claim 6 , wherein the main accelerator (I) is N claim 6 ,N-bis(2-hydroxypropyl)-p-toluidine and the co-accelerator (II) is N claim 6 ,N-bis(2-hydroxyethyl)-m-toluidine.8. The resin mixture according to claim 6 , wherein a ...

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09-05-2013 дата публикации

IRIDIUM COMPLEX AND METHOD FOR PRODUCING OPTICALLY ACTIVE COMPOUND

Номер: US20130116438A1
Автор: Nara Hideki, Shimizu Hideo
Принадлежит: TAKASAGO INTERNATIONAL CORPORATION

An object of the present invention is to provide a novel iridium complex, and to provide a novel catalyst having excellent performances in terms of enantioselectivity, catalytic activity, and the like. Provided is an iridium complex of the following general formula (1): 111.-. (canceled)12. An iridium complex of the following general formula (1):{'br': None, 'sub': 2', 'm, 'IrHZ(PP)(Q)\u2003\u2003(1)'}wherein Z represents a halogen atom,PP represents a bisphosphine,Q represents an amine, andm represents 1 or 2.13. The iridium complex according to claim 12 , whereinPP in the general formula (1) is an optically active bisphosphine.14. The iridium complex according to claim 13 , wherein {'br': None, 'sup': 1', '2', '3, 'NRRR\u2003\u2003(2)'}, 'Q in the general formula (1) is an amine represented by the following general formula (2){'sup': 1', '2', '3, 'wherein R, Rand Reach independently represent a hydrogen atom, an alkyl group having 1 to 6 carbon atoms, or an aryl group which optionally have a substituent.'}19. The production method according to claim 17 , wherein {'br': None, 'sup': 1', '2', '3, 'NRRR\u2003\u2003(2)'}, 'the amine is an amine represented by the following general formula (2){'sup': 1', '2', '3, 'wherein R, Rand Reach independently represent a hydrogen atom, an alkyl group having 1 to 6 carbon atoms, or an aryl group which optionally have a substituent.'}21. An asymmetric hydrogenation catalyst comprising the iridium complex according to .23. The production method according to claim 18 , wherein {'br': None, 'sup': 1', '2', '3, 'NRRR\u2003\u2003(2)'}, 'the amine is an amine represented by the following general formula (2){'sup': 1', '2', '3, 'wherein R, Rand Reach independently represent a hydrogen atom, an alkyl group having 1 to 6 carbon atoms, or an aryl group which optionally have a substituent.'} The present invention relates to an iridium complex and a method for producing an optically active compound.Synthetic methods based on catalytic ...

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09-05-2013 дата публикации

Process for preparing saturated amino acids or saturated amino esters comprising a metathesis step

Номер: US20130116458A1

The subject matter of the invention is a process for synthesizing a saturated long-chain o.,0)-amino ester (acid) obtained in a first step by cross-metathesis between an acrylic first compound and a monounsaturated second compound comprising at least one nitrile, acid or ester trivalent function, one of these compounds comprising a nitrile function and the other an acid or ester function, in the presence of a ruthenium carbene metathesis catalyst, and in a second step by hydrogenation of the monounsaturated nitrile ester (acid) obtained in the presence of the metathesis catalyst of the preceding stop, acting as a hydrogenation catalyst.

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09-05-2013 дата публикации

CONVERSION OF ALCOHOLS

Номер: US20130116481A1
Принадлежит: BP Biofuels UK Limited

A method is described for use in a process for the conversion of an alcohol, the method including the step of contacting a composition comprising a first alcohol with a catalyst composition. Catalyst composition described comprises: i) a source of a Group VIII transition metal; ii) a phosphine ligand of formula PRRR, wherein R, Rand Rare the same or different; and iii) a base. In examples described, the alcohol which is converted comprises ethanol and the product comprises butanol. 1. A method for use in a process for the conversion of an alcohol into a product , the method including the step of contacting a composition comprising a first alcohol with a catalyst composition , in which the catalyst composition comprises:i) a source of a Group VIII transition metal, wherein the Group VIII transition metal is selected from one or more of the group comprising Fe, Ru, Os;{'sup': 1', '2', '3', '1', '2', '3', '1', '2', '3, 'ii) a phosphine ligand of formula PR, RR, wherein R, Rand Rare the same or different, and wherein one or more of R, R, and Rinclude a heteroatom-substituted hydrocarbon group; and'}iii) abase.2. A method according to claim 1 , wherein the phosphine ligand of formula PR claim 1 , RRis a multi-dentate ligand with respect to the Group VIII metal.3. A method according to claim 1 , wherein the heteroatom comprises one or more selected from the group comprising O claim 1 , S claim 1 , N and P.4. A method according to claim 3 , wherein the heteroatom comprises one or more selected from the group comprising N and P.5. A method according to claim 1 , wherein only one of R claim 1 , R claim 1 , and Rinclude a heteroatom-substituted hydrocarbon group.6. A method according to claim 1 , wherein the phosphine ligand comprises a bi-dentate ligand with respect to the Group VIII metal.7. A method according to claim 1 , wherein the phosphine ligand comprises a diphosphine group —[P{link}P]— wherein a linking group {link} has a backbone including fewer than two atoms.8. A ...

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16-05-2013 дата публикации

SUPPORTED IRIDIUM CATALYSTS

Номер: US20130123097A1

A method of converting at least one first alkane to a mixture of at least one low molecular weight alkane (optionally also including additional lower and/or higher molecular weight alkanes) and at least one high molecular weight alkane, comprises: reacting a first alkane in the presence of dual catalyst system comprising a first catalyst (i.e., a hydrogen transfer catalyst) and a second catalyst (i.e., a metathesis catalyst) to produce a mixture of low and high molecular weight alkanes. 119-. (canceled)20. A composition comprising , alone or in combination ,(i) an iridium pincer complex hydrogen transfer catalyst immobilized on a solid support by (a) Lewis acid:Lewis base binding of said catalyst to a solid support; (b) covalent coupling of said catalyst to a solid support by a silicone or siloxane-containing linker; or (c) covalent coupling of said catalyst to a polystyrene support; and(ii) optionally a metathesis catalyst immobilized on a solid support.21. The composition of claim 20 , wherein said metathesis catalyst is selected from the group consisting of Schrock catalysts claim 20 , molybdenum catalysts claim 20 , tungsten oxide catalysts claim 20 , rhenium oxide catalysts claim 20 , and mixtures thereof22. The composition of claim 20 , wherein said hydrogen transfer catalyst and said metathesis catalyst are immobilized on the same solid support.23. The composition of claim 20 , wherein said hydrogen transfer catalyst and said metathesis catalyst are immobilized on a different solid support.2433-. (canceled) This invention was made with Government support under Grant No. CHE-0107810 from the National Science Foundation. The United States Government has certain rights to this invention.This application is related to Goldman et al., US Patent Application Publication No. 2007/0060781 (attorney docket no. 5470-437), the disclosure of which is incorporated by reference herein in its entirety.The present invention concerns methods of converting alkanes to higher ...

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16-05-2013 дата публикации

ZERO VALENT METAL COMPOSITE, MANUFACTURING, SYSTEM AND METHOD USING THEREOF, FOR CATALYTICALLY TREATING CONTAMINATED WATER

Номер: US20130123098A1
Принадлежит: Yeda Research and Development Co. Ltd.

Zero valent metal composite, manufacturing thereof, using thereof, and system including thereof, for (in-situ or ex-situ) catalytically treating contaminated water, such as sub-surface water, surface water, above-surface water, water vapor, or/and gaseous water. Composite includes powdered diatomite matrix incorporated with nanometer (1-1000 nm) sized particles of a zero valent (transition) metal (iron, cobalt, nickel, copper, zinc, palladium, platinum, or/and gold) and at least one electron transfer mediator (catalyst) from porphyrinogenic organometallic complexes (e.g., metalloporphyrins (chlorophylls, hemes, cytochromes) or metallocorrins (e.g., vitamin B), and optionally, includes vermiculite. System includes composite and in-situ or/and ex-situ unit containing the composite, enabling exposure of contaminated water thereto. Applicable to in-situ sub-surface permeable reactive barriers (PRBs). Treatable water contaminants are organics (halogenated organic compounds), or/and inorganics (metal elements, metal element containing inorganic species, nonmetal elements, and nonmetal element containing inorganic species). Applicable to non-aqueous fluids (liquids, vapors, gases), for removing contaminants therefrom. 1. A system for catalytically treating contaminated water , comprising:(a) a zero valent metal composite comprised of a powdered diatomite matrix on or/and in which is incorporated zero valent metal particles having a size in a range of between about 1 nm and about 1000 nm and at least one electron transfer mediator; and(b) at least one unit for containing a catalytically effective amount of said zero valent metal composite, for exposing the contaminated water to said zero valent metal composite.2. The system of claim 1 , wherein said powdered diatomite matrix has a particle size in a range of between about 1 micron and about 150 microns.3. The system of claim 1 , wherein said metal in said zero valent metal particles comprises at least one transition metal.4 ...

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16-05-2013 дата публикации

PROCESS FOR PREPARING FORMIC ACID BY REACTION OF CARBON DIOXIDE WITH HYDROGEN

Номер: US20130123526A1
Принадлежит: BASF SE

The invention relates to a process for preparing formic acid by reaction of carbon dioxide with hydrogen in a hydrogenation reactor in the presence of a transition metal complex as a catalyst comprising at least one element from group 8, 9 or 10 of the Periodic Table and at least one phosphine ligand with at least one organic radical having at least 13 carbon atoms, of a tertiary amine and of a polar solvent to form a formic acid-amine, adduct, which is subsequently dissociated thermally to formic acid and the corresponding tertiary amine. on unit. 115.-. (canceled)16. A process for preparing formic acid , comprising the steps of [{'br': None, 'sup': 1', '2', '3, 'NRRR\u2003\u2003(A1)'}, 'in which', {'sup': 1', '2', '3, 'R, R, Rare each independently an unbranched or branched, acyclic or cyclic, aliphatic, araliphatic or aromatic radical having in each case 1 to 16 carbon atoms, where individual carbon atoms may each independently also be substituted by a hetero group selected from the —O— and >N— groups, and two or all three radicals may also be joined to one another to form a chain comprising at least four atoms in each case,'}, 'in the presence of at least one transition metal complex as a catalyst, comprising at least one element selected from groups 8, 9 and 10 of the Periodic Table and at least one phosphine ligand with at least one organic radical having at least 13 carbon atoms,', 'in a hydrogenation reactor', 'to obtain, optionally after addition of water, a biphasic hydrogenation mixture (H) comprising', 'an upper phase (U1) comprising the catalyst and the tertiary amine (A1), and', {'br': None, 'sup': 1', '2', '3, 'i': '*x', 'sub': 'i', 'NRRRHCOOH\u2003\u2003(A2)'}, 'a lower phase (L1) comprising the at least one polar solvent, residues of the catalyst and a formic acid-amine adduct of the general formula (A2)'}, 'in which', {'sub': 'i', 'xis in the range from 0.4 to 5 and'}, {'sup': 1', '2', '3, 'R, R, Rare each as defined above,'}], '(a) homogeneously ...

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23-05-2013 дата публикации

CARBON SUPPORTED TETRAAMIDO MACROCYCLIC LIGAND CATALYTIC ACTIVATORS AND METHODS FOR MAKING THE SAME

Номер: US20130126443A1
Принадлежит: CARNEGIE MELLON UNIVERSITY

Embodiments of the invention provide a tetraamido macrocyclic ligand catalytic activator bound to a carbon containing support. When combined with an oxidant, such as a peroxy compound, the carbon supported catalytic activator is a long-lived, robust oxidizing agent useful for oxidizing oxidizable compounds, such as aromatic groups, conjugated pi systems, natural and synthetic hormones, pesticides, pathogens, and dyes. 2. The oxidant activator recited in wherein the carbon-containing support is selected from the group consisting of activated carbon claim 1 , amorphous carbon claim 1 , graphite claim 1 , charcoal claim 1 , and carbon-rich compositions.3. The oxidant activator recited in wherein the counterion is selected from the group consisting of tetraarylphosphonium claim 1 , bis-(triphenylphosphorananylidene)-ammonium claim 1 , and tetraalkylammonium cations.4. The oxidant activator recited in wherein the counterion is selected from the group consisting of tetraphenylphosphonium and tetraethyl ammonium claim 3 , tetrapropyl ammonium claim 3 , tetrabutylammonium.6. The oxidant activator recited in wherein M is iron.7. The oxidant activator recited in wherein the carbon-containing support is selected from the group consisting of activated carbon claim 5 , amorphous carbon claim 5 , graphite claim 5 , charcoal claim 5 , and carbon-rich compositions.9. The oxidant activator recited in wherein the axial ligand is selected from the group consisting of aqua ligands and Cl.10. The oxidant activator recited in wherein M is iron (III).11. A method for making a supported catalytic activator comprising:adsorbing a tetraamido macrocyclic metal ligand having a counterion onto a carbon-containing support.12. The method recited in wherein the carbon-containing support is selected from the group consisting of activated carbon claim 11 , amorphous carbon claim 11 , graphite claim 11 , charcoal claim 11 , and carbon-rich compositions.13. The method recited in wherein the step of ...

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23-05-2013 дата публикации

SULFOXIDATION CATALYSTS AND METHODS AND SYSTEMS OF USING SAME

Номер: US20130130892A1
Принадлежит: AUTERRA, INC.

Catalysts amenable to oxidizing sulfur compounds and systems and methods of using these catalysts to effect the removal of sulfur from crude oil and crude oil distillates are disclosed. The catalyst is disposed with a titanyl moiety which serves to selectively coordinate sulfur compounds and affect their oxidation. The titanyl may be bound within a polymer or on the surface of a polymer or on the surface or in the pores of an inorganic support. The resulting oxidized sulfur compounds are readily separated from the initial crude oil or crude oil distillate streams by traditional separation techniques arrayed as described in the systems and methods disclosed. 1. A catalytic sulfoxidation reagent comprising:a phase transfer agent/solvent{'sub': m', 'm', 'n, 'a catalyst comprising a metal complex represented by the general formula MO(OR), wherein M is a metal complex; R is carbon group having at least 3 carbon atoms, where at each occurrence R may individually be a substituted alkyl group containing at least one OH group, a substituted cycloalkyl group containing at least one OH group, a substituted cycloalkylalkyl group containing at least one OH group, a substituted heterocyclyl group containing at least one OH group, or a heterocyclylalkyl containing at least one OH group; and the subscripts m and n may each independently be integers between about 1 and about 8; and'}an oxidant dissolved in the phase transfer agent/solvent.2. The reagent of wherein the catalyst comprises:bis(polyol)oxotitanium(IV);wherein the catalyst is selected from the group consisting of bis(glycerol)oxotitanium(IV), bis(ethyleneglycol)oxotitanium(IV), bis(erythritol)oxotitanium(IV), bis(sorbitol)oxotitanium(IV), and mixtures thereof.3. The reagent of claim 1 , wherein the catalyst is dissolved in the phase transfer agent/solvent.4. The reagent of claim 1 , wherein M is titanium and/or zirconium. This application is a continuation of U.S. application Ser. No. 12/933,898 filed Sep. 22, 2010 ...

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23-05-2013 дата публикации

OPTICALLY ACTIVE AMMONIUM SALT COMPOUND, PRODUCTION INTERMEDIATE THEREOF, AND PRODUCTION METHOD THEREOF

Номер: US20130131337A1
Принадлежит: NIPPON SODA CO., LTD.

An optically active bisbenzyl compound or a racemic bisbenzyl compound represented by formula (2) that has axial chirality. An optically active azepine derivative or a racemic azepine derivative represented by formula (3). Methods of producing an optically active quaternary ammonium salt compound represented by formula (8). This is a divisional of application Ser. No. 11/817,585 filed Sep. 25, 2009, which is a National Stage application of PCT/JP2006/304091 filed Mar. 3, 2006, and claims the benefit of Japanese Patent Application Nos. 2005-059694 and 2005-192757 filed Mar. 3, 2005 and Jun. 30, 2005. The entire disclosures of the prior applications are hereby incorporated by reference herein in their entirety.The present invention relates to a compound of an optically active quaternary ammonium salt which is useful as a chiral phase transfer catalyst and more specifically, relates to a novel optically active quaternary ammonium salt, and an intermediate and production method for producing said compound.Priority is claimed on Japanese Patent Applications No. 2005-059694, filed Mar. 3, 2005, and No. 2005-192757, filed Jun. 30, 2005, the contents of which are incorporated herein by reference.Many compounds regarding optically active spiro quaternary ammonium salts have been known to date. Examples thereof include the compound described in Patent document 1 and represented by the following formulaand the compound described in Patent document 3, and the documents disclose that these compounds perform extremely effectively as a phase transfer catalyst for synthesizing optically active α-amino acids regardless of being natural or not. However, the optically active Spiro quaternary ammonium salts described in these documents are expensive since they are constituted from two kinds of binaphthyl derivatives having different substituents, and thus they are not necessarily satisfactory for industrial use.Moreover, the compound represented by the following formula is described in ...

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23-05-2013 дата публикации

Catalysts for ring-closing metathesis

Номер: US20130131353A1

A catalyst composition is provided, which may be used for ring closing metathesis. In the composition, a catalyst is immobilized on a siliceous mesocellular foam support. A suitable catalyst for use in the composition is a Grubbs-type catalyst or a Hoveyda-Grubbs-type catalyst.

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23-05-2013 дата публикации

Metal Complex Compound and Process for Producing Amides Utilizing the Metal Complex Compound

Номер: US20130131366A1

A catalyst contains a metal complex compound represented by the following general formula (I). In the formula (I), M is a metal ion such as ruthenium, Lis a cyclic or acyclic, neutral or minus 1-valent unsaturated hydrocarbon group of 1 to 30 carbon atoms which may have a substituent, Land Lare each independently chlorine or the like, and Lis a compound bonded to M through phosphorus or arsenic and represented by the following general formula (IIa) or (IIb). In the formulas (IIa) and (IIb), E is phosphorus or arsenic, Yis oxygen or sulfur, Y, Yand Yare each independently a hydrogen atom, an aryl group or the like, and H is a hydrogen atom. 3. The hydration catalyst as claimed in claim 1 , wherein Lis cyclic diene claim 1 , triene or tetraene of 1 to 30 carbon atoms which may have a substituent and is a neutral or minus 1-valent unsaturated hydrocarbon group.4. The hydration catalyst as claimed in claim 1 , wherein Lis acyclic diene claim 1 , triene or tetraene of 1 to 30 carbon atoms which may have a substituent and is a neutral or minus 1-valent unsaturated hydrocarbon group.5. The hydration catalyst as claimed in claim 1 , wherein the compound represented by the general formula (IIa) or (IIb) is any one of secondary phosphine oxide claim 1 , an aliphatic phosphoric acid ester claim 1 , an aliphatic phosphorous acid ester claim 1 , an aromatic phosphoric acid ester and an aromatic phosphorous acid ester of 1 to 30 carbon atoms which may have a substituent.6. The hydration catalyst as claimed in claim 1 , wherein the compound represented by the general formula (IIa) or (IIb) is any one of diarylphosphine oxide which may have a substituent claim 1 , dialkylphosphine oxide which may have a substituent claim 1 , secondary phosphine oxide having a phenyl group which may have a substituent and having an alkyl group which may have a substituent claim 1 , a phosphorous acid dialkyl ester of 1 to 30 carbon atoms claim 1 , a phosphorous acid diphenyl ester which may have a ...

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30-05-2013 дата публикации

Reducing Emissions in Polyurethane Foam

Номер: US20130137787A1
Принадлежит: AIR PRODUCTS AND CHEMICALS, INC.

This invention disclosure relates to a process to make flexible open cell polyurethane foam with optimum mechanical properties and lowest chemical emissions. Using the selection of tertiary amine catalysts together with a group of carboxylic acids according to this disclosure can produce foam products with optimum properties and lowest chemical emanations. 1. A catalyst comprising at least one acid selected from the group consisting of carboxylic diacids and carboxylic triacids , and at least one tertiary amine comprising at least one functionality selected from the group consisting of urea , amide , secondary-amine , primary amine or secondary-hydroxyl and wherein the acid has no isocyanate reactive groups and tertiary amine is substantially free of primary hydroxyl groups.2. The catalyst of wherein the acid comprises at least one member selected from the group consisting of fumaric claim 1 , malonic claim 1 , maleic claim 1 , succinic claim 1 , glutaric claim 1 , adipic claim 1 , pimelic claim 1 , suberic claim 1 , azelaic claim 1 , sebacic claim 1 , glutaconic claim 1 , traumatic claim 1 , muconic claim 1 , phthalic claim 1 , isophthalic and therephthalic acids.3. The catalyst of wherein the tertiary amine comprises at least one member selected from the group consisting of N claim 1 ,N-bis(3-dimethylamino-propyl)-N-(2-hydroxypropyl)amine; N claim 1 ,N-dimethyl-N′ claim 1 ,N′-bis(2-hydroxypropyl)-1 claim 1 ,3-propylenediamine; dimethylaminopropylamine (DMAPA); N-methyl-N′-2-hydroxypropyl-piperazine; bis(dimethylaminopropyl)amine claim 1 , dimethylaminopropyl urea; N claim 1 ,N′-bis(3-dimethylaminopropyl)urea claim 1 , bis(dimethylamino)-2-propanol claim 1 , N-(3-aminopropyl)imidazole claim 1 , N-(2-hydroxypropyl)imidazole claim 1 , N-(2-hydroxyethylimidazole) claim 1 , N claim 1 ,N′-bis(2-hydroxypropyl)piperazine claim 1 , N-(2-hydroxypropyl)-morpholine.4. The catalyst of further comprising at least one member selected from the group consisting of 2-[N-( ...

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30-05-2013 дата публикации

Catalyst for Akili-Free Purification of Oil Raw Materials from Mercaptans

Номер: US20130137888A1
Принадлежит: Greendane Ltd

A catalyst for alkali-free purification of oil raw materials includes a solid metalocomplex or a liquid metalocomplex with a general formula (Cu M Cl)20(Li)2̂(L 2 )î, where Li is amino alcohol, L2 is acetonitryl or single atom alcohol.

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30-05-2013 дата публикации

CATALYTIC COMPOSITION AND PROCESS FOR THE SELECTIVE DIMERIZATION OF ISOBUTENE

Номер: US20130137911A1
Принадлежит: IFP ENERGIES NOUVELLES

Catalytic composition comprising at least one Brønsted acid, designated HB, dissolved in a non-aqueous liquid medium of general formula QA, in which Q represents an organic cation and A represents an anion, said composition also comprising an additive QA in which Q represents an organic cation containing at least one alcohol function and A represents an anion. The invention also relates to an isobutene dimerization process using the catalytic composition. 1. Catalytic composition comprising at least one Brønsted acid , designated HB , dissolved in a non-aqueous liquid medium of general formula QA , in which Q represents an organic cation and A represents an anion , said composition also comprising an additive QAin which Q represents an organic cation comprising at least one alcohol function and A represents an anion.2. Catalytic composition according to claim 1 , in which the anion A or A is chosen from the following anions: tetrafluoroborate claim 1 , tetraalkylborates claim 1 , hexafluorophosphate claim 1 , hexafluoroantimonate claim 1 , alkylsulphonates claim 1 , arylsulphonates claim 1 , perfluoroalkylsulphonates claim 1 , fluorosulphonate claim 1 , sulphates claim 1 , phosphates claim 1 , perfluoroacetates claim 1 , perfluoroalkylsulphonamides claim 1 , fluorosulphonamides claim 1 , perfluoroalkylsulphomethides and carboranes claim 1 , Aand A being identical or different.3. Catalytic composition according to claim 1 , in which Q represents a quaternary ammonium and/or a quaternary phosphonium and/or a trialkylsulphonium claim 1 , and Qrepresents a quaternary ammonium and/or a quaternary phosphonium and/or a trialkylsulphonium comprising at least one alcohol function claim 1 , and Aor Arepresent any anion known to be non-coordinating and capable of forming a liquid salt below 150° C.5. Catalytic composition according to claim 4 , in which the quaternary ammonium and/or phosphonium cation Q is chosen from the group formed by N-butylpyridinium claim 4 , N- ...

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30-05-2013 дата публикации

CATALYTIC COMPOSITION CONTAINING AN ACID FUNCTION AND A PROCESS FOR THE SELECTIVE DIMERIZATION OF ISOBUTENE

Номер: US20130137912A1
Принадлежит: IFP ENERGIES NOUVELLES

Catalytic composition comprising at least one non-aqueous ionic liquid medium of general formula QA, in which Q represents an organic cation and A represents an anion, and at least one ionic component of general formula QA, in which Q represents an organic cation comprising at least one sulphonic acid or carboxylic acid function, and A represents an anion. The invention also relates to an isobutene dimerization process using the catalytic composition. 1. Catalytic composition comprising at least one non-aqueous ionic liquid medium of general formula QA , in which Q represents an organic cation and A represents an anion , and at least one ionic component of general formula QA , in which Q represents an organic cation comprising at least one sulphonic acid or carboxylic acid function , and A represents an anion.2. Catalytic composition according to claim 1 , in which the anion A or A is chosen from the following anions: tetrafluoroborate claim 1 , tetraalkylborates claim 1 , hexafluorophosphate claim 1 , hexafluoroantimonate claim 1 , alkylsulphonates claim 1 , arylsulphonates claim 1 , perfluoroalkylsulphonates claim 1 , fluorosulphonate claim 1 , sulphates claim 1 , phosphates claim 1 , perfluoroacetates claim 1 , perfluoroalkylsulphonamides claim 1 , fluorosulphonamides claim 1 , perfluoroalkylsulphomethides and carboranes claim 1 , A and A being identical or different.3. Catalytic composition according to claim 1 , in which Q represents a quaternary ammonium and/or a quaternary phosphonium and/or a trialkylsulphonium claim 1 , and Q represents a quaternary ammonium and/or a quaternary phosphonium and/or a trialkylsulphonium comprising at least one sulphonic acid or carboxylic acid function claim 1 , and A or A represent any anion known to be non-coordinating and capable of forming a liquid salt below 150° C.5. Catalytic composition according to claim 4 , in which the quaternary ammonium and/or phosphonium cation Q is chosen from the group formed by N- ...

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06-06-2013 дата публикации

PROCESS FOR PRODUCING DISPERSION OF PARTICLES OF RUTILE TITANIUM OXIDE

Номер: US20130143729A1
Принадлежит:

The invention provides a process for producing an aqueous dispersion of particles of rutile titanium oxide, which comprises: 1. A process for producing an aqueous dispersion of particles of rutile titanium oxide , which comprises:a first step in which after a chloride ion concentration of an aqueous solution of titanium tetrachloride is adjusted to 0.5 mole/L or more, and less than 4.4 mole/L, the aqueous solution of titanium tetrachloride is heated at a temperature in a range of from 25° C. to 75° C. to hydrolyze the titanium tetrachloride, thereby obtaining a slurry containing the thus precipitated particles of rutile titanium oxide;a second step in which the slurry obtained in the first step is filtered and washed with water to remove water-soluble salts dissolved therein from the slurry;a third step in which the slurry obtained in the second step is subjected to a hydrothermal reaction in the presence of an organic acid;a fourth step in which the slurry obtained in the third step is filtered and washed with water to remove water-soluble salts dissolved therein from the slurry;a fifth step in which an acid is added to the slurry obtained in the fourth step to deflocculate the slurry, and the resulting slurry is subjected to wet dispersion treatment, thereby obtaining a dispersion;a sixth step in which excess acid and water-soluble salts are removed from the dispersion obtained in the fifth step.2. The process for producing an aqueous dispersion of particles of rutile titanium oxide according to claim 1 , which further comprises a pre-third step between the second step and the third step claim 1 , wherein in the pre-third step the slurry obtained in the second step is subjected to wet grinding treatment in the presence of an organic acid.3. The process for producing an aqueous dispersion of particles of rutile titanium oxide according to claim 1 , wherein in the fifth step claim 1 , after an acid is added to the slurry obtained in the fourth step to deflocculate ...

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06-06-2013 дата публикации

Metal-ligand catalyst formation

Номер: US20130143730A1
Принадлежит: Invista North America LLC

As described herein, nickel treated with sulfur provides a surprisingly effective source of nickel atoms for generating nickel-phosphorus-containing ligand complexes useful as hydrocyanation catalysts.

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06-06-2013 дата публикации

Ruthenium-Based Catalytic Complexes and the Use of Such Complexes for Olefin Metathesis

Номер: US20130144060A1
Принадлежит: UMICORE AG & CO. KG

Disclosed herein are compounds of the formula (I) or (II) in which: L is a neutral ligand; X, X′ are anionic ligands; Rand Rare, separately, a hydrogen, a C-Calkyl, a C-Cperhalogenoalkyl, a aldehyde, a ketone, an ester, a nitrile, an aryl, a pyridinium alkyl, an optionally substituted Cor Cpyridinium alkyl, perhalogenoalkyl or cyclohexyl, a Ch2Y radical 10 with n between 1 and 6 and y an iconic marker, or a radical having the formula: wherein Rcan be a radical of formula (Ibis) when the compound has formula (I) or of formula (IIbis) when the compound has formula (II), Ris a C-Calkyl, or a Cor Ccycloalkyl or a Cor Caryl; R, R, R, R, R, R, R, R, R, are, separately, a hydrogen, C-Calkyl, a C-Cperhalogenoalkyl, or a Cor Caryl; wherein R, R, Rcan be a heterocycle; Xis anion. Rand Rcan form, with the N and the C to which they are attached, a heterocycle. 124-. (canceled)26. Compound according to claim 25 , wherein L is P(R) claim 25 , with Rbeing a Cto Calkyl or an aryl or a Cor Ccycloalkyl.28. Compound according to claim 25 , wherein L is PCy claim 25 , with Cy being cyclohexyl claim 25 , or L is a ligand of formula 7a or 7b.X is a chlorine,X′ is a chlorine.30. Compound according to claim 28 , wherein Ris selected from the group consisting of CF claim 28 , CF claim 28 , and pNOCH.31. Compound according to claim 30 , wherein in (I) Ris CF.47. Method according to claim 46 , wherein said compound of formula (III) is the Grubbs precatalyst (2b) or the Nolan precatalyst (2c) This invention relates to new activated and recyclable ruthenium-based catalytic complexes as well as a method for synthesis of same.The invention also relates to the use of such catalytic complexes for olefin metathesis.The development of recyclable or activated ruthenium-based catalytic complexes is based on the work of R. Grubbs of the University of California (USA) relating to the ruthenium complex 2a (precatalyst 2b) called the Grubbs II catalyst.Thus, the first recyclable complex 3a (precatalyst 3b) ...

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06-06-2013 дата публикации

CALCINATION AND REDUCTION PROCESS INCLUDING A FLUIDIZING BED REACTOR

Номер: US20130144079A1
Принадлежит: INVISTA North America S.a.r.l.

These disclosures relate to preparing nickel metal (Ni(0)) suited for use in catalyst systems, such as nickel complexes with phosphorus-containing ligands, useful to catalyze the hydrocyanation of ethylenically unsaturated compounds. The methods described herein can include use of steam during reduction of nickel. 1. A method for the production of nickel metal (Ni(0)) from a nickel(II)-containing composition comprising steps of:providing a nickel(II)-containing composition and a gas to a fluidizing bed reactor, wherein the gas is flowing and substantially supporting solids from the composition;wherein the gas comprises steam; andreducing nickel in the nickel(II)-containing composition to thereby produce nickel metal (Ni(0)) from the nickel(II)-containing composition;wherein the composition comprises nickel(II)-containing substances selected from a group consisting of: basic nickel carbonate, nickel carbonate, nickel bicarbonate, nickel oxalate, nickel formate, nickel squarate, nickel oxide and nickel hydroxide.2. The method of claim 1 , further comprising calcining the nickel(II)-containing composition prior to reducing the nickel.3. The method of claim 1 , further comprising calcining the nickel(II)-containing composition under calcining conditions.4. The method of claim 1 , further comprising calcining the nickel(II)-containing composition by a method comprising providing a gas to the fluidizing bed reactor that comprises oxygen.5. The method of claim 1 , further comprising calcining the nickel(II)-containing composition by a method comprising operating the fluidized bed for a time and at a temperature sufficient for generating nickel oxide within the nickel(II)-containing composition.6. The method of claim 1 , further comprising calcining the nickel(II)-containing composition using calcining conditions that yield a calcined product with a carbon:nickel atomic ratio of less than one.7. The method of claim 1 , further comprising calcining the nickel(II)-containing ...

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06-06-2013 дата публикации

NICKEL FORM FOR PREPARATION OF CATALYTIC NICKEL-LIGAND COMPLEXES

Номер: US20130144082A1
Принадлежит: INVISTA NORTH AMERICA S.A R.L.

A novel nickel particulate form is provided that efficiently forms a zero-valent nickel complex with a phosphorus-containing ligands in an organic liquid to form a hydrocyanation catalyst. Particles in the nickel particulate form comprise nickel crystallites. For example, the nickel particulate form can have a BET Specific Surface Area of at least about 1 m/gm; an average crystallite size less than about 20-25 nm, the nickel particulate form can have at least 10% of the crystallites in the nickel form can have can have a diameter (C10) of less than about 10 nm, and/or there are on average at least about 10surface crystallites per gram nickel. A ratio of BET SSA to C50 for the nickel particulate form can be at least about 0.1×10m/gm and preferably at least about 0.4×10m/gm. Methods of preparation and use are also provided. 1. A nickel particulate form comprising nickel crystallites , wherein the nickel particulate form has a BET Specific Surface Area of at least about 1 m/gm; at least 10% of the nickel crystallites have a size (C10) that is less than about 20 nm; the nickel crystallites have an average crystallite size of no greater than about 100 nm; and the nickel crystallite size distribution span is greater than about 1.0.2. The nickel particulate form of claim 1 , wherein the nickel particulate form has a BET Specific Surface Area/C50 ratio of not less than 0.07×10m/gm.3. The nickel particulate form of claim 1 , wherein the nickel particulate form on average has at least about 10surface crystallites per gram of nickel.4. The nickel particulate form of claim 1 , wherein at least 10% of the particles of the form have a size (D10) of no greater than about 6 μm.5. The nickel particulate form of claim 1 , which has a Laser Diffraction Specific Surface Area of at least about 0.4 m/gm.6. The nickel particulate form of claim 1 , which has a BET Specific Surface Area to D10 ratio of about 0.3×10m/gm to about 10.0×10m/gm.7. The nickel particulate form of claim 1 , which ...

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06-06-2013 дата публикации

CATALYSTS FOR THE ALKYNE METATHESIS

Номер: US20130144102A1
Принадлежит: STUDIENGESELLSCHAFT KOHLE MBH

Organometallic compounds of the general formula (I), in which M=Mo, W, are claimed. 2. Metal-organic compound according to , characterized in that the residues Rand Rare linked together while forming a 5-8 membered saturated , unsaturated or aromatic ring , and thus form a bridge , which selected from CRR , CR═CR , CRR—CRR , CRR—CRR—CRR , CRR═CR—CRR , CRR—CRR—CRR—CRCR , CR═CR—CRR—CRCRor CRR—CR═CR—CRCRin which R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , R , Rand Rare independently selected from one other and may have the same meaning as Ras defined in .4. Metal-organic compounds according to claim 2 , characterized in that the phenanthroline ligand in Formula 11 is selected from: 1 claim 2 ,10-phenanthroline claim 2 , 4-methyl-1 claim 2 ,20-phenanthroline claim 2 , 5-methyl-1 claim 2 ,10-phenanthroline claim 2 , 2 claim 2 ,9-dimethyl[1 claim 2 ,10]-phenanthroline claim 2 , 5 claim 2 ,6-dimethyl-1 claim 2 ,10-phenanthroline claim 2 , 5-chloro[1 claim 2 ,10]phenanthroline claim 2 , 4 claim 2 ,7-dichloro-1 claim 2 ,10-phenanthroline claim 2 , 4 claim 2 ,7-dichloro-1 claim 2 ,10-phenanthroline claim 2 , 3 claim 2 ,4 claim 2 ,7 claim 2 ,8-tetramethyl-1 claim 2 ,10-phenanthroline claim 2 , 4 claim 2 ,7-diphenyl[1 claim 2 ,10]phenanthroline claim 2 , 2 claim 2 ,9-dimethyl-4 claim 2 ,7-diphenyl[1 claim 2 ,10]phenanthroline claim 2 , 5-nitro-1 claim 2 ,10-phenanthroline claim 2 , or 4 claim 2 ,7-dimethoxy-1 claim 2 ,10-phenanthroline.6. Metal-organic compounds according to claim 1 , characterized in that the bipyridyl ligand is selected from: 2 claim 1 ,2′-bipyridine claim 1 , 5 claim 1 ,5′-dimethyl-2 claim 1 ,2′-dipyridyl claim 1 , 4 claim 1 ,4′-dimethyl-2 claim 1 ,2′-dipyridyl claim 1 , 6 claim 1 ,6′-dimethyl-2 claim 1 ,2′-dipyridyl claim 1 , 4 claim 1 ,4′-dimethoxy-2 claim 1 ,2′-bipyridine claim 1 , 2 claim 1 ,2′-biquinoline claim 1 , 4 claim 1 ,4′-di-tert-butyl-2 claim ...

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13-06-2013 дата публикации

GRAPHENE OXIDE AND GRAPHITE OXIDE CATALYSTS AND SYSTEMS

Номер: US20130149211A1
Принадлежит: GRAPHEA, INC.

A carbocatalyst for use in oxidation and polymerization reactions includes particles having a carbon and oxygen-containing material, such as catalytically-active graphene oxide and/or catalytically-active graphite oxide. In some cases, the particles are disposed on a solid support formed of a carbon-containing material, such as graphene or graphite, or a non-carbon containing material, such as a metallic or insulating material. 1. A non-transition metal catalyst comprising catalytically-active graphene oxide or catalytically-active graphite oxide , the catalyst having a transition metal content less than about 1 part per million.235. The catalyst of claim 1 , wherein the transition metal content is less than about 100 parts per billion. cm -. (canceled)6. The catalyst of claim 1 , wherein the catalyst has a hydrogen peroxide-terminated surface.7. The catalyst of claim 1 , wherein the catalyst has an OH-terminated surface.8. A graphene oxide or graphite oxide catalyst having at least about 25% carbon and at least about 0.01% oxygen as measured by x-ray photoelectron spectroscopy (XPS).9. A graphene oxide or graphite oxide catalyst having graphene oxide or graphite oxide with a carbon-to-oxygen ratio of at least about 0.5:1.1013-. (canceled)14. The catalyst of claim 1 , wherein the catalyst includes at least one surface moiety selected from the group consisting of an alkyl group claim 1 , aryl group claim 1 , alkenyl group claim 1 , alkynyl group claim 1 , hydroxyl group claim 1 , epoxide group claim 1 , peroxide group claim 1 , peroxyacid group claim 1 , aldehyde group claim 1 , ketone group claim 1 , ether group claim 1 , carboxylic acid and carboxylate group.1518-. (canceled)19. The catalyst of claim 1 , having one or more Fourier Transform Infrared (FT-IR) features at about 3150 cm claim 1 , 1685 cm claim 1 , 1280 cmand 1140 cm.2066-. (canceled)67. A catalyst system comprising the catalyst of claim 1 , and further comprising:a source of a carbon-containing ...

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13-06-2013 дата публикации

HYDROCARBON CONVERSION SYSTEM, AND A PROCESS AND CATALYST COMPOSITION RELATING THERETO

Номер: US20130149213A1
Принадлежит: UOP LLC

One exemplary embodiment can be a process for making a catalyst including an effective amount of iron for catalyzing one or more reactions in a hydrocarbon conversion system. The process can include grinding and coating the particles. The ground particles can have an effective amount of iron, and substantially all the particles may have a maximum dimension no larger than about 130 microns. The coating can have an effective amount of one or more hydrocarbons to provide the catalyst with improved flowability. 1. A process for making a catalyst comprising an effective amount of iron for catalyzing one or more reactions in a hydrocarbon conversion system , comprising:A) grinding particles comprising the effective amount of iron so substantially all the particles have a maximum dimension no larger than about 130 microns; andB) coating the particles with an effective amount of one or more hydrocarbons to provide the catalyst with improved flowability.2. The process according to claim 1 , wherein the iron is at least partially comprised in at least one or more compounds of an iron oxide claim 1 , an iron sulfate claim 1 , and an iron carbonate.3. The process according to claim 1 , wherein the iron is comprised in an iron sulfate.4. The process according to claim 1 , wherein the iron is comprised in at least one of an iron sulfate monohydrate and an iron sulfate heptahydrate.5. The process according to claim 1 , wherein the one or more hydrocarbons is compatible with a feed for processing in the hydrocarbon conversion system.6. The process according to claim 1 , wherein the one or more hydrocarbons has a melting point temperature of no more than about 250° C.7. The process according to claim 1 , wherein the one or more hydrocarbons has a melting point temperature of no more than about 80° C.8. The process according to claim 1 , wherein the one or more hydrocarbons comprises at least one of a wax claim 1 , a pitch claim 1 , a deasphalted oil claim 1 , a petroleum resin claim ...

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13-06-2013 дата публикации

CATALYST FUNCTIONALIZED BUFFER SORBENT PEBBLES FOR RAPID SEPARATION OF CARBON DIOXIDE FROM GAS MIXTURES

Номер: US20130149768A1
Автор: Aines Roger D.

A method for separating COfrom gas mixtures uses a slurried media impregnated with buffer compounds and coating the solid media with a catalyst or enzyme that promotes the transformation of COto carbonic acid. Buffer sorbent pebbles with a catalyst or enzyme coating are provided for rapid separation of COfrom gas mixtures. 1. A catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture , comprising:a sorbent pebble, said sorbent pebbles includinga sorbent pebble body anda surface layer with an attached or embedded catalyst or enzyme, wherein said sorbent pebble provides separation of carbon dioxide from the gas mixture.2. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said sorbent pebble body is a material that absorbs carbon dioxide.3. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said surface layer with an attached catalyst or enzyme is an attached catalyst.4. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said surface layer with an attached catalyst or enzyme is an embedded catalyst.5. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said surface layer with an attached catalyst or enzyme is an attached enzyme.6. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said surface layer with an attached catalyst or enzyme is an embedded enzyme.7. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said surface layer with an attached catalyst or enzyme is a material that promotes the transformation of carbon dioxide to carbonic acid.8. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said ...

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13-06-2013 дата публикации

PHOSPHINATE RUTHENIUM COMPLEXES

Номер: US20130150572A1
Принадлежит: IDENIX PHARMACEUTICALS, INC.

Provided herein are ruthenium complexes of Formula I, and processes of preparation thereof. Also provided are methods of their use as a metathesis catalyst. 5. The method of claim 1 , wherein L is a heterocyclic carbene or phosphine claim 1 ,wherein the heterocyclic carbene is optionally substituted with one or more substituents.7. The method of claim 6 , wherein Ror Ris hydrogen or methyl.8. The method of claim 6 , wherein Ror Ris hydrogen or methyl.9. The method of claim 6 , wherein Ris Caryl.10. The method of claim 6 , wherein Ris Caryl claim 6 , substituted with one or more Calkyl.11. The method of claim 10 , wherein Ris 2-methylphenyl claim 10 , 2 claim 10 ,4 claim 10 ,6-trimethylphenyl claim 10 , or 2 claim 10 ,6-di(isopropyl)phenyl.12. The method of claim 6 , wherein Ris Caryl.13. The method of claim 6 , wherein Ris Caryl claim 6 , substituted with one or more Calkyl.14. The method of claim 6 , wherein Ris 2-methylphenyl claim 6 , 2 claim 6 ,4 claim 6 ,6-trimethylphenyl claim 6 , or 2 claim 6 ,6-di(isopropyl)phenyl.16. The method of claim 5 , wherein the phosphine is PRRR claim 5 , wherein R claim 5 , R claim 5 , and Rare each independently Calkyl or Caryl claim 5 , each optionally substituted with one or more substituents.17. The method of claim 16 , wherein Ris phenyl or cyclohexyl.18. The method of claim 16 , wherein Ris phenyl or cyclohexyl.19. The method of claim 16 , wherein Ris phenyl or cyclohexyl.20. The method of claim 16 , wherein the phosphine is triphenylphosphine or tricyclohexylphosphine.21. The method of claim 1 , wherein Xis halide claim 1 , —C(O)R claim 1 , or —OC(O)R claim 1 , wherein Ris alkyl claim 1 , optionally substituted with one or more halides.22. The method of claim 21 , wherein Xis chloride.23. The method of claim 1 , wherein Xis halide claim 1 , —C(O)R claim 1 , or —OC(O)R claim 1 , wherein Ris alkyl claim 1 , optionally substituted with one or more halides.24. The method of claim 1 , wherein Xis chloride.25. The method of claim ...

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20-06-2013 дата публикации

Electrocatalysts For Carbon Dioxide Conversion

Номер: US20130157174A1
Принадлежит:

Electrocatalysts for carbon dioxide conversion include at least one catalytically active element with a particle size above 0.6 nm. The electrocatalysts can also include a Helper Catalyst. The catalysts can be used to increase the rate, modify the selectivity or lower the overpotential of electrochemical conversion of CO. Chemical processes and devices using the catalysts also include processes to produce CO, HCO, HCO, (HCO), HCO, CHOH, CH, CH, CHCHOH, CHCOO, CHCOOH, CH, (COOH), or (COO), and a specific device, namely, a COsensor. 1. A catalyst for the electrochemical conversion of COinto useful products comprising at least one catalytically active element wherein said catalytically active element is in the form of supported or unsupported particles and the particles of the at least one catalytically active element have an average size between 0.6 nm and 100 nm.2. The catalyst of claim 1 , wherein the average particle size is between about 0.6 nm and 40 nm.3. The catalyst of wherein the average particle size is between about 0.6 nm and 20 nm.4. The catalyst of wherein the average particle size is between about 0.6 nm and 10 nm.5. The catalyst of further comprising a Helper Catalyst.6. The catalyst of wherein said catalytically active element comprises at least one of V claim 1 , Cr claim 1 , Mn claim 1 , Fe claim 1 , Co claim 1 , Ni claim 1 , Cu claim 1 , Zr claim 1 , Nb claim 1 , Mo claim 1 , Ru claim 1 , Rh claim 1 , Pd claim 1 , Ag claim 1 , Cd claim 1 , W claim 1 , Re claim 1 , Ir claim 1 , Pt claim 1 , Au claim 1 , Hg claim 1 , Pb claim 1 , and Bi.7. The catalyst of wherein said products comprise at least one of the following: CO claim 1 , HCO claim 1 , HCO claim 1 , (HCO) claim 1 , HCO claim 1 , CHOH claim 1 , CH claim 1 , CH claim 1 , CHCHOH claim 1 , CHCOO claim 1 , CHCOOH claim 1 , CH claim 1 , (COOH)and (COO).8. The catalyst of wherein said reaction products comprising one of CO or HCOOH.9. The catalyst of wherein said catalytically active element ...

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20-06-2013 дата публикации

PROCESS FOR THE SYNTHESIS OF IVABRADINE AND ADDITION SALTS THEREOF WITH A PHARMACEUTICALLY ACCEPTABLE ACID

Номер: US20130158256A1
Принадлежит: LES LABORATOIRES SERVIER

Process for the synthesis of ivabradine of formula (I): 9. The process according to claim 1 , wherein the amount of catalyst used in the reductive amination reaction is from 1 mol % to 10 mol % relative to the aldehyde.10. The process according to claim 1 , wherein the amount of trimethylamine N-oxide used in the reductive amination reaction is from 0 to 3 equivalents relative to the catalyst.11. The process according to claim 10 , wherein the amount of trimethylamine N-oxide used in the reductive amination reaction is from 0.5 to 1.5 equivalents relative to the catalyst.12. The process according to claim 1 , wherein the dihydrogen pressure in the reductive amination reaction is from 1 to 10 bars.13. The process according to claim 1 , wherein the solvent in the reductive amination reaction is an alcohol.14. The process according to claim 13 , wherein the solvent in the reductive amination reaction is ethanol.15. The process according to claim 1 , wherein the temperature of the reductive amination reaction is from 50 to 100° C. The present invention relates to a process for the synthesis of ivabradine of formula (I):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, addition salts thereof with a pharmaceutically acceptable acid, and hydrates thereof.Ivabradine, 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 those 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 ...

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20-06-2013 дата публикации

METHOD FOR PRODUCING PHENYL-SUBSTITUTED HETEROCYCLIC DERIVATIVE BY MEANS OF COUPLING METHOD USING PALLADIUM COMPOUND

Номер: US20130158272A1
Автор: Komiyama Masato
Принадлежит: TEIJIN PHARMA LIMITED

The present invention provides a method for producing a xanthine oxidase inhibitor, which is a therapeutic agent for hyperuricemia, or intermediates of the same, said method being efficient and using a short process. The present invention is a novel coupling method for obtaining a compound represented by formula (3) by bringing about a coupling reaction between a compound represented by formula (1) and a compound represented by formula (2), in the presence of a palladium compound, a ligand capable of coordinating to the palladium compound, a base, a C-Ccarboxylic acid, and at least one kind of additive. 2. The method of production according to claim 1 , wherein A is a Cto Calkyl group.3. The method of production according to claim 1 , wherein A is an isobutyl group.4. The method of production according to claim 1 , wherein X is an oxygen atom.5. The method of production according to claim 1 , wherein Ris a hydrogen atom.6. The method of production according to claim 1 , wherein Ris a cyano group.7. The method of production according to claim 1 , wherein Y represents a halogen atom claim 1 , —OCO—(Cto Calkyl group) claim 1 , —OCO— (phenyl group) claim 1 , —OSO—(Cto Calkyl group) claim 1 , —OSO-(phenyl group) claim 1 , or a diazonium group claim 1 , and claim 1 , in Y claim 1 , the Cto Calkyl group can be substituted with 1 to 3 halogen atoms claim 1 , and the phenyl group can be substituted with 1 to 5 optional substituents selected from halogen atoms and Cto Calkyl groups.9. The method of production according to claim 1 , wherein Ris COORand Ris a Cto Calkyl group.10. The method of production according to claim 1 , wherein Ris a methyl group.11. The method of production according to claim 1 , wherein the palladium compound is zerovalent palladium claim 1 , or a salt of monovalent or divalent palladium.12. The method of production according to claim 1 , wherein the palladium compound is palladium(II) acetate (Pd(OAc)) claim 1 , palladium(II) propionate (Pd(O(C═O)CHCH ...

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20-06-2013 дата публикации

Polyhedral oligomeric silsesquioxane (poss) bonded ligands and the use thereof

Номер: US20130158282A1
Принадлежит: Evonik Oxeno GmbH and Co KG

The present invention relates to POSS-modified ligands and to the use thereof in catalytically effective compositions in hydroformylation.

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27-06-2013 дата публикации

PROCESS FOR THE PREPARATION OF A CATALYST WHICH CAN BE USED IN HYDROTREATMENT AND HYDROCONVERSION

Номер: US20130165316A1
Принадлежит:

A process for the preparation of a catalyst from a catalytic precursor comprising a support based on alumina and/or silica-alumina and/or zeolite and comprising at least one element of group VIB and optionally at least one element of group VIII, by impregnation of said precursor with a solution of a C1-C4 dialkyl succinate. An impregnation step for impregnation of said precursor which is dried, calcined or regenerated, with at least one solution containing at least one carboxylic acid other than acetic acid, then maturing and drying at a temperature less than or equal to 200° C., optionally a heat treatment at a temperature lower than 350° C., followed by an impregnation step with a solution containing at least one C1-C4 dialkyl succinate followed by maturing and drying at a temperature less than 200° C. without subsequent calcination step. The catalyst is used in hydrotreatment and/or hydroconversion. 2. A process according to characterised in that the catalytic precursor is a catalyst which has been regenerated.3. A process according to characterised in that that the catalytic precursor contains all of the elements of groups GVIB and if they are present all of the elements of group V111.4. A process according to characterised in that the dialkyl succinate is dimethyl succinate.5. A process according to characterised in that the carboxylic acid is citric acid.6. A process according to characterised in that steps 1) and/or 2) are performed in the presence of water and/or ethanol.7. A process according to characterised in that the maturing steps are performed at a temperature between 17 and 60° C.8. A process according to characterised in that the drying operation in step 1) is performed at a temperature between 100 and 180° C.9. A process according to characterised in that the drying operation in step 2) is performed at a temperature between 50 and 160° C.10. A process according to characterised in that the solution of step 1) and/or step 2) contains at least one ...

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27-06-2013 дата публикации

COMPOSITION HAVING AN ACTIVE METAL OR PRECURSOR, AN AMINE COMPONENT AND A NON-AMINE CONTAINING POLAR ADDITIVE USEFUL IN THE CATALYTIC HYDROPROCESSING OF HYDROCARBONS, A METHOD OF MAKING SUCH CATALYST, AND A PROCESS OF USING SUCH CATALYST

Номер: US20130165317A1
Принадлежит: SHELL OIL COMPANY

A composition that comprises a support material that is loaded with an active metal or metal precursor, an amine component, and a non-amine containing polar additive. The composition is useful in the hydroprocessing of hydrocarbon feedstocks. The composition is prepared by incorporating a metal solution into a support material followed by incorporating therein an amine component and a non-amine containing polar additive. 1. A composition , comprising: a support material that is loaded with an active metal precursor , an amine component , and a non-amine containing polar additive.2. A composition as recited in claim 1 , wherein said amine component is selected from the group of compounds consisting of ether amine compounds claim 1 , alkyl amine compounds claim 1 , and amine oxide compounds.3. A composition as recited in claim 2 , wherein said ether amine compounds include those selected from the family of compounds having the following formula: R—O—(CH)NH claim 2 , wherein R is an alkyl functional group comprising from 4 to 14 carbon atoms and n is an integer of ranging from 1 to 6.4. A composition as recited in claim 3 , wherein said amine oxide compounds include those selected from the family of compounds having the following formula: [insert drawing of R1 claim 3 , R2 and R3] NO claim 3 , wherein R1 is either a hydrogen atom or an alkyl functional group claim 3 , R2 is either a hydrogen atom or an alkyl functional group claim 3 , and R3 is either a hydrogen atom or an alky functional group claim 3 , wherein the total number of carbon atoms included in R1 and R2 and R3 is in the range of from 8 carbon atoms to 40 carbon atoms.5. A composition as recited in claim 4 , wherein said alkyl amine compounds include those selected from the group of amine compounds consisting of primary amines having from 8 to 20 carbon atoms claim 4 , secondary amines having from 8 to 20 carbon atoms claim 4 , and tertiary amines having from 8 to 20 carbon atoms.6. A composition as recited ...

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27-06-2013 дата публикации

COMPLEXES

Номер: US20130165660A1
Принадлежит: JOHNSON MATTHEY PUBLIC LIMITED COMPANY

A complex of formula (1), 2. A complex according to claim 1 , wherein M is palladium.3. A complex according to claim 1 , wherein Rand Rare independently selected from the group consisting of substituted and unsubstituted straight-chain alkyl claim 1 , substituted and unsubstituted branched-chain alkyl claim 1 , substituted and unsubstituted cycloalkyl claim 1 , substituted and unsubstituted aryl claim 1 , and substituted and unsubstituted heteroaryl wherein the heteroatoms are selected from the group consisting of sulfur claim 1 , nitrogen and oxygen.4. A complex according to claim 1 , wherein Ris phenyl or dimethylaminophenyl.6. A complex according to claim 5 , wherein Ris a substituted or unsubstituted alkyl claim 5 , substituted or unsubstituted aryl claim 5 , substituted or unsubstituted (alkyl)HN— claim 5 , substituted or unsubstituted (dialkyl)N— claim 5 , substituted or unsubstituted (dialkyl)amino-alkyl or substituted or unsubstituted alkoxyalkyl.7. A complex according to claim 5 , wherein Ris a substituted or unsubstituted alkyl or substituted or unsubstituted aryl.9. A complex according to claim 5 , wherein Ris selected from the group consisting of phenyl claim 5 , napthyl claim 5 , methoxyphenyl claim 5 , halophenyl claim 5 , methylphenyl and FC-phenyl claim 5 , and q is 4 or 5.10. A complex according to claim 5 , wherein Ris selected from the group consisting of phenyl claim 5 , methoxyphenyl claim 5 , methylphenyl and FC-phenyl claim 5 , and q is 4 or 5.12. A complex according to claim 1 , wherein Ris selected from the group consisting of substituted and unsubstituted straight-chain alkyl claim 1 , substituted and unsubstituted branched-chain alkyl claim 1 , substituted and unsubstituted cycloalkyl claim 1 , substituted and unsubstituted aryl claim 1 , and substituted and unsubstituted heteroaryl wherein the heteroatoms are selected from the group consisting of sulfur claim 1 , nitrogen and oxygen.13. A complex according to claim 1 , wherein X is a halo ...

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04-07-2013 дата публикации

Organic templated nanometal oxyhydroxide

Номер: US20130168320A1
Принадлежит: INDIAN INSTITUTES OF TECHNOLOGY

Disclosed are granular composites comprising a biopolymer and one or more nanometal-oxyhydroxide/hydroxide/oxide particles, along with methods for the preparation and use thereof.

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04-07-2013 дата публикации

PLATING CATALYST AND METHOD

Номер: US20130171363A1
Принадлежит: Rohm and Haas Electronic Materials LLC

A catalyst solution includes a precious metal nanoparticle and a polymer having a carboxyl group and a nitrogen atom. The catalyst solution is useful for a catalyzing an electroless process for plating metal on non-conductive surfaces. 1. A solution comprising a precious metal nanoparticle and a polymer , the polymer comprises a carboxyl group and a nitrogen atom within the repeating unit of the polymer.2. The solution of claim 1 , wherein the polymer is polyamino acids.3. The solution of claim 1 , wherein the polymer is polyaspartate.4. The solution of claim 1 , wherein the precious metal is silver claim 1 , gold claim 1 , platinum claim 1 , palladium claim 1 , rhodium claim 1 , ruthenium claim 1 , iridium or osmium.5. A method for preparing a solution comprising a precious metal nanoparticle and a polymer having carboxyl group and nitrogen atom claim 1 , the method comprises;Preparing a solution comprising precious metal ion and a polymer having carboxyl group and nitrogen atom,Adding a reducing agent in the solution with stirring.6. A process for electroless plating a metal on non-conductive surface claim 1 , the process comprises the steps of;{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'dipping a substrate to be plated into the solution of ,'}conducting electroless plating of the substrate without an accelerating step. This application claims the benefit of priority under 35 U.S.C. §119(e) to U.S. Provisional Application No. 61/582,265, filed Dec. 31, 2011, the entire contents of which application are incorporated herein by reference.The present invention relates to a catalyst solution including a precious metal nanoparticle. More particularly, the present invention relates to a catalyst solution including a precious metal nanoparticle stabilized by specific compounds useful in electroless metal plating of non-conductive substrates used in the manufacture of electronic devices and decorative coating.Electroless metal deposition or plating is useful for the ...

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04-07-2013 дата публикации

PLATING CATALYST AND METHOD

Номер: US20130171366A1
Принадлежит: Rohm and Haas Electronic Materials LLC

A solution including a precious metal nanoparticle and a polymer polymerized from a monomer comprising at least a monomer having two or more carboxyl groups or carboxylic acid salt groups. The solution is useful for a catalyst for a process of electroless plating of a metal on non-conductive surface. 1. A solution comprising a precious metal nanoparticle and a polymer , the polymer is polymerized from a monomer comprising at least a monomer having two or more carboxyl groups or carboxylic acid salt groups.2. The solution of claim 1 , wherein the polymer has an oxygen atom as an ether bond in a principal chain.3. The solution of claim 2 , wherein the polymer is polyepoxysuccinic acid or salts thereof.4. The solution of claim 1 , wherein the polymer is polymaleic acid or polymer polymerized by a maleic acid and another polymerizable monomer chosen from acrylic acid claim 1 , methacrylic acid claim 1 , phosphonic acid and sulfonic acid.5. The solution of claim 1 , wherein the polymer comprises monomers of acrylic acid and citraconic acid or phosphonic acid and citraconic acid.6. The solution of claim 1 , wherein the precious metal is silver claim 1 , gold claim 1 , platinum claim 1 , palladium claim 1 , rhodium claim 1 , ruthenium claim 1 , iridium or osmium.7. A method for preparing a solution comprising a precious metal nanoparticle and a polymer polymerized from a monomer comprising at least a monomer having two or more carboxyl groups or carboxylic acid salt groups claim 1 , the method comprises;a) preparing a solution comprising precious metal ions and a polymer polymerized from a monomer comprising at least a monomer having two or more carboxyl groups or carboxylic acid salt groups; andb) adding a reducing agent in said solution, and stirring the solution.8. A process for electroless plating a metal on non-conductive surface claim 1 , the process comprises the steps of;{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'a) dipping a substrate to be plated into a ...

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04-07-2013 дата публикации

Catalyst compositions for the polymerization of olefins

Номер: US20130172497A1
Принадлежит: Chevron Phillips Chemical Co LP

Catalyst compositions containing N,N-bis[2-hydroxidebenzyl]amine transition metal compounds are disclosed. Methods for making these transition metal compounds and for using such compounds in catalyst compositions for the polymerization of olefins also are provided.

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04-07-2013 дата публикации

Chelating Carbene Ligand Precursors and Their Use in the Synthesis of Metathesis Catalysts

Номер: US20130172568A1
Принадлежит: Materia Inc

Chelating ligand precursors for the preparation of olefin methathesis catalysts are disclosed. The resulting catalysts are air stable monomeric species capable of promoting various methathesis reactions efficiently, which can be recovered from the reaction mixture and reused. Internal olefin compounds, specifically beta-substituted styrenes, are used as ligand precursors. Compared to terminal olefin compounds such as unsubstituted styrenes, the beta-substituted styrenes are easier and less costly to prepare, and more stable since they are less prone to spontaneous polymerization. Methods of preparing chelating-carbene methathesis catalysts without the use of CuCl are disclosed. This eliminates the need for CuCl by replacing it with organic acids, mineral acids, mild oxidants or even water, resulting in high yields of Hoveyda-type methathesis catalysts. The invention provides an efficient method for preparing chelating-carbene metathesis catalysts by reacting a suitable ruthenium complex in high concentrations of the ligand precursors followed by crystallization from an organic solvent.

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04-07-2013 дата публикации

METHODS FOR PRODUCING IRON METHACRYLATE AND HYDROXYALKYL METHACRYLATE

Номер: US20130172591A1
Принадлежит: MITSUBISHI RAYON CO., LTD.

There is provided a method for producing iron methacrylate being inexpensive, and being high in activity and selectivity and good in solubility to a reaction liquid when being used in production of a hydroxyalkyl methacrylate as a catalyst. The method for producing iron methacrylate for production of a hydroxyalkyl methacrylate according to the present invention includes subjecting a mixture of a metallic iron having an oxygen atom content by XRF analysis of the surface thereof of 6% by mass or lower, and methacrylic acid to a heat treatment at 95° C. or higher and lower than 110° C. for 100 to 600 min. The method for producing a hydroxyalkyl methacrylate according to the present invention includes reacting an alkylene oxide with methacrylic acid to produce the hydroxyalkyl methacrylate, wherein iron methacrylate produced by the method according to the present invention is used as a catalyst. 1. A method for producing iron methacrylate , the method comprising subjecting a mixture of a metallic iron and methacrylic acid to a heat treatment at a temperature of from 95° C. to 110° C. for 100 to 600 min ,wherein the metallic iron has an oxygen atom content by XRF analysis of a surface thereof of 6% by mass or lower.2. The method of claim 1 , further comprising:subjecting the mixture, after the heat treatment, to a further heat treatment at a temperature of from 110° C. to 125° C. for 30 to 300 min, andsubsequently cooling to 100° C. or lower.3. A method for producing a hydroxyalkyl methacrylate claim 1 , the method comprising reacting an alkylene oxide with a methacrylic acid and the iron methacrylate of claim 1 ,wherein the iron methacrylate is a catalyst.4. The method of claim 3 , further comprising reacting with a quaternary ammonium salt and an amine compound claim 3 ,wherein the quaternary ammonium salt and amine compound are catalysts.5. The method of claim 4 , wherein the quaternary ammonium salt is in an amount of from 0.5 to 1.5 mol with respect to 1 mol of the ...

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04-07-2013 дата публикации

IRIDIUM CATALYSTS FOR CARBONYLATION

Номер: US20130172601A1
Принадлежит: EASTMAN CHEMICAL COMPANY

A solid catalyst comprising an effective amount of iridium and at least one second metal selected from gallium, zinc, indium and germanium associated with a solid support material is useful for vapor phase carbonylation to produce carboxylic acids and esters from alkyl alcohols, esters, ethers or ester-alcohol mixtures. The iridium and at least one second metal are deposited on a support material. In some embodiments of the invention, the catalyst is useful for vapor phase carbonylation. 1. A carbonylation catalyst comprising an effective amount of iridium and at least one second metal selected from gallium , zinc , indium and germanium wherein the iridium and the at least one second metal are associated with a solid support material.2. The carbonylation catalyst according to wherein the solid support material is selected from pumice claim 1 , alumina claim 1 , silica claim 1 , silica-alumina claim 1 , magnesia claim 1 , diatomaceous earth claim 1 , bauxite claim 1 , titania claim 1 , zirconia claim 1 , clays claim 1 , magnesium silicate claim 1 , silicon carbide claim 1 , zeolites claim 1 , ceramics claim 1 , carbon and combinations of two or more of the foregoing.3. The carbonylation catalyst of wherein the solid support material comprises activated carbon.4. The carbonylation catalyst of wherein the catalyst includes from about 0.01 weight percent to about 10 weight percent each of the iridium and the at least one second metal.5. The carbonylation catalyst of wherein the catalyst includes from about 0.1 weight percent to about 3 weight percent each of the iridium and the at least one second metal.6. The carbonylation catalyst of wherein the molar ratio of the at least one second metal to iridium is from about 0.1:1 to about 10:1.7. The carbonylation catalyst of wherein the molar ratio of the at least one second metal to iridium is from about 0.5:1 to about 5:1.8. The carbonylation catalyst of claim 1 , further comprising at least one vaporous halogen promoting ...

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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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04-07-2013 дата публикации

Olefin Oligomerization Methods

Номер: US20130172651A1
Автор: Brooke L. Small
Принадлежит: Chevron Phillips Chemical Co LP

Processes for oligomerizing olefins utilizing a catalyst system including a) a transition metal complex that is transition metal compound complexed to a pyridine bisimine ligand and b) a metal alkyl and controlling the olefin oligomer product distribution K value by adjusting i) a transition metal of the transition metal complex concentration in the reactor, ii) a metal of the metal alkyl concentration in the reactor, iii) a metal of the metal alkyl to transition metal of the transition metal complex molar ratio in the reactor, and iv) any combination thereof.

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