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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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Применить Всего найдено 18. Отображено 17.
24-04-2014 дата публикации

Oxidative dehydrogenation of ethane to ethylene and preparation of multimetallic mixed oxide catalyst for such process

Номер: US20140114109A1
Принадлежит:

Oxidative dehydrogenation of light paraffins, such as ethane at moderate temperatures (<500° C.) to produce ethylene without the formation of side products such as acetic acid and/or other oxygenated hydrocarbons is achieved using tellurium-free, multimetallic catalysts possessing orthorhombic M1 phase and other crystalline structures that have an important role for obtaining high performance catalysts for the oxidative dehydrogenation of ethane to ethylene. Such catalysts are prepared using thermal and hydrothermal methods. 1. A process for the oxidative dehydrogenation of ethane to ethylene , which comprises contacting a feedstock comprising ethane and an oxidizing agent under oxidative dehydrogenation reaction conditions with a tellurium-free , multimetallic mixed oxide solid catalyst having the formula{'br': None, 'sub': h', 'i', 'j', 'x, 'MoVSbAO\u2003\u2003(I)'} 'B) a process which comprises forming a tellurium-free mixture of molybdenum, vanadium and antimony metallic precursors and thermally treating said tellurium-free mixture of mixture to form an MoVSb solid, doping said MoVSb solid with a metal cation represented by said A, and thermally activating the A metal cation-doped MoVSb solid to form a catalyst having one or more crystalline phases in addition to the M1 crystalline phase.', 'A) a process which comprises forming a tellurium-free mixture of molybdenum, vanadium and antimony metallic precursors and a structure-directing compound selected from the group consisting of primary amines, secondary amines, tertiary amines, ammonia, tetra-methyl ammonium and hydrazine, and subjecting said tellurium-free mixture to hydrothermal conditions to form a solid, washing and drying said solid, and thermally activating said dried solid to form a catalyst having one or more crystalline phases in addition to the M1 crystalline phase; or'}, 'wherein A represents Nb, W, Ga, Bi, Sn, Cu, Ti, Fe, Co, Ni, Cr, Zr, rare earth metals or rare earth alkaline metals or mixtures ...

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26-03-2015 дата публикации

Multimetallic mixed oxides, its preparation and use for the oxidative dehydrogenation of ethane for producing ethylene

Номер: US20150086471A1

A layered multimetallic oxide catalyst having the formula M1 M2 M3 O δ wherein: M1 is selected from the group of Ag, Au, Zn, Sn, Rh, Pd, Pt, Cu, Ni, Fe, Co, an alkaline metal, an alkaline earth metal, a rare earth metal, and mixtures thereof; M2 is selected from the group of Ti, Hf, Zr, Sn, Bi, Sb, V, Nb, Ta and P, and mixtures thereof; M3 is selected from the group of Mo, W and Cr, and mixtures thereof; and where said multilayered metallic oxide exhibits a major X-ray diffraction peak between 5<2θ<15, is prepared by a process of mixing metallic precursors of M 1 , M 2 and M 3 to form a precursor mixture, hydrothermal treatment of the resulting mixture to obtain a homogeneous solid mixture, and thermally treating the solid mixture to activate the solid mixture and obtain said catalyst.

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26-03-2015 дата публикации

OXIDATIVE DEHYDROGENATION OF ETHANE TO ETHYLENE AND PREPARATION OF MULTIMETALLIC MIXED OXIDE CATALYST FOR SUCH PROCESS

Номер: US20150087505A1
Принадлежит:

Oxidative dehydrogenation of light paraffins, such as ethane at moderate temperatures (<500° C.) to produce ethylene without the formation of side products such as acetic acid and/or other oxygenated hydrocarbons is achieved using tellurium-free, multimetallic catalysts possessing orthorhombic M1 phase and other crystalline structures that have an important role for obtaining high performance catalysts for the oxidative dehydrogenation of ethane to ethylene. Such catalysts are prepared using thermal and hydrothermal methods. 1. A method for the formation of a multimetallic mixed oxide having the formula{'br': None, 'sub': h', 'i', 'x, 'MoVSbO'}wherein h and i, respectively, are each between 0.001 and 4.0, the ratio i/h is between 0.3 and 10.0, and x represents the number determined by and consistent with the valence requirements of the other elements present in the multimetallic mixed oxide, which comprises, forming a tellurium-free aqueous solution of metallic precursors consisting of molybdenum, vanadium and antimony and a structure-directing compound selected from the group consisting of primary amines, secondary amines, tertiary amines, ammonia, tetra-methyl ammonium and hydrazine, and subjecting said tellurium-free mixture to hydrothermal conditions to form a solid, washing and drying said solid, and thermally activating said dried solid to form a catalyst having one or more crystalline phases in addition to the M1 crystalline phase.2. The process of claim 1 , wherein structure-directing compound is selected from the group consisting of methylamine claim 1 , dimethyl amine claim 1 , tri-methyl amine claim 1 , diethyl amine claim 1 , or mixtures thereof.3. The process of claim 1 , wherein said hydrothermal treatment is conducted at a temperature between 100-200° C. for 6-150 hours and the resulting solids are washed and dried at 80-120° C. claim 1 , prior to activation.4. The process of claim 3 , wherein said hydrothermal treatment is at a temperature between ...

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23-04-2015 дата публикации

MULTIMETALLIC MIXED OXIDES, ITS PREPARATION AND USE FOR THE OXIDATIVE DEHYDROGENATION OF ETHANE FOR PRODUCING ETHYLENE

Номер: US20150112109A1
Принадлежит:

A layered multimetallic mixed oxide (LMMO) is characterized by one or more diffraction peaks at 5<2θ<15, preferably between 10<2θ<15. The catalysts can be represented by the general formula: 113-. (canceled)14. A process for preparing a nanometer and micrometer layered multimetallic oxide catalyst having the formula{'br': None, 'sub': 'δ', 'M1 M2 M3 O'}wherein:M1 is selected from the group of Ag, Au, Zn, Sn, Rh, Pd, Pt, Cu, Ni, Fe, Co, an alkaline metal, an alkaline earth metal, a rare earth metal, and mixtures thereof;M2 is selected from the group of Ti, Hf, Zr, Sn, Bi, Sb, V, Nb, Ta and P, and mixtures thereof;M3 is selected from the group of Mo, W and Cr, and mixtures thereof;and where said multilayered metallic oxide exhibits a major X-ray diffraction peak between 5<2θ<15,said process comprising the steps of{'sub': 1', '2', '3, 'mixing metallic precursors of M, Mand Mto form a precursor mixture,'}hydrothermal treatment of the resulting mixture to obtain a homogeneous solid mixture, andthermally treating the solid mixture to activate the solid mixture and obtain said catalyst.15. The process of claim 14 , whereinthe precursors are mixed by mechanical mixing or by dissolution of the corresponding metal salts.17. The process of claim 14 , further comprising the steps ofadding a chemical agent to the precursor mixture selected from the group consisting of an amino acid, glycine, amines, urea or carboxylic acids, or a mixture thereof.18. The process of claim 14 , whereinsaid precursors are selected from the group consisting of pure metallic elements, metallic salts, metallic oxides, metallic hydroxides, metallic alkoxides, acids, and mixtures thereof.19. The process of claim 18 , whereinsaid precursors are selected from the group consisting of nitrates, oxalates, sulfates, carbonates, halides, and mixtures thereof.20. The process of claim 14 , whereinsaid catalyst exhibits at least one X-ray diffraction pattern selected from the group consisting of monoclinic lattice ...

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03-06-2021 дата публикации

Catalytic formulation for producing propylene cyclic carbonate from carbon dioxide using a potassium iodide catalyst

Номер: US20210162379A1
Принадлежит: INSTITUTO MEXICANO DEL PETROLEO

This invention is related to the synthesis of organic carbonates from carbon dioxide and epoxides. It is particularly focused on the production of propylene cyclic carbonate from propylene oxide. The proposed catalytic materials includes a support made of aluminum oxyhydroxide (Catapal B®), nitric acid, acetic acid and/or phosphoric acid. An important stage is the physical and chemical conditioning of the catalytic materials and to this end, experimental methodologies such as spheronization and thermal treatments were implemented prior the evaluation process.

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04-06-2015 дата публикации

OXIDATIVE DEHYDROGENATION OF ETHANE TO ETHYLENE AND PREPARATION OF MULTIMETALLIC MIXED OXIDE CATALYST FOR SUCH PROCESS

Номер: US20150151280A1
Принадлежит:

Oxidative dehydrogenation of light paraffins, such as ethane at moderate temperatures (<500° C.) to produce ethylene without the formation of side products such as acetic acid and/or other oxygenated hydrocarbons is achieved using tellurium-free, multimetallic catalysts possessing orthorhombic M1 phase and other crystalline structures that have an important role for obtaining high performance catalysts for the oxidative dehydrogenation of ethane to ethylene. Such catalysts are prepared using thermal and hydrothermal methods. 1. A method for the formation of a multimetallic mixed oxide having the formula{'br': None, 'sub': h', 'i', 'x, 'MoVSbO'}wherein h and i, respectively, are each between 0.001 and 4.0, the ratio i/h is between 0.3 and 10.0, and x represents the number determined by and consistent with the valence requirements of the other elements present in the multimetallic mixed oxide, which comprises, forming a tellurium-free aqueous solution of metallic precursors consisting of molybdenum, vanadium and antimony and a structure-directing compound selected from the group consisting of primary amines, secondary amines, tertiary amines, ammonia, tetra-methyl ammonium and hydrazine, and subjecting said tellurium-free mixture to hydrothermal conditions to form a solid, washing and drying said solid, and thermally activating said dried solid to form a catalyst having one or more crystalline phases in addition to the M1 crystalline phase.2. The process of claim 1 , wherein structure-directing compound is selected from the group consisting of methylamine claim 1 , dimethyl amine claim 1 , tri-methyl amine claim 1 , diethyl amine claim 1 , or mixtures thereof.3. The process of claim 1 , wherein said hydrothermal treatment is conducted at a temperature between 100-200° C. for 6-150 hours and the resulting solids are washed and dried at 80-120° C. claim 1 , prior to activation.4. The process of claim 3 , wherein said hydrothermal treatment is at a temperature between ...

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18-09-2014 дата публикации

MULTIMETALLIC MIXED OXIDES, ITS PREPARATION AND USE FOR THE OXIDATIVE DEHYDROGENATION OF ETHANE FOR PRODUCING ETHYLENE

Номер: US20140275685A1
Принадлежит:

A layered multimetallic mixed oxide (LMMO) is characterized by one or more diffraction peaks at 5<2θ<15, preferably between 10<2θ<15. The catalysts can be represented by the general formula: 1. A layered multimetallic mixed oxide catalyst adapted for the oxidative dehydrogenation of ethane to ethylene , said catalyst having the formula{'br': None, 'sub': 'δ', 'M1M2M3O'}wherein:M1 is selected from the group of Ag, Au, Zn, Sn, Rh, Pd, Pt, Cu, Ni, Fe, Co, an alkaline metal, an alkaline earth metal, a rare earth metal, and mixtures thereof;M2 is selected from the group of Ti, Hf, Zr, Sn, Bi, Sb, V, Nb, Ta and P, and mixtures thereof;M3 is selected from the group of Mo, W and Cr, and mixtures thereof;where δ depends on the amount, oxidation state and/or valence of the components;and where the catalyst exhibits at least one X-ray diffraction peak between 5<2θ<15.2. The catalyst of claim 1 , whereinsaid catalyst exhibits at least one X-ray diffraction pattern selected from the group consisting of monoclinic lattice of silver vanadium molybdenum oxide corresponding to ICDD-PDF 04-002-4830, or cesium vanadium molybdenum oxide corresponding to ICDD-PDF 00-030-0381, or monoclinic sodium vanadium molybdenum oxide corresponding to ICDD-PDF 04-011-9693, or monoclinic lithium vanadium molybdenum oxide corresponding to ICDD-PDF 04-006-7234, or orthorhombic calcium vanadium molybdenum oxide corresponding to ICDD-PDF 04-013-4035.3. The catalyst of claim 1 , whereinsaid catalyst exhibits at least one X-ray diffraction peak between 10<2θ<15.4. The catalyst of claim 1 , wherein said catalyst is prepared by a process comprising the steps of{'sub': 1', '2', '3, 'mixing metallic precursors of M, Mand Mto form a precursor mixture,'}hydrothermally treating the precursor mixture to obtain a homogeneous solid mixture, andthermally treating the homogeneous solid mixture to activate the solid mixture and obtain said catalyst.5. The catalyst of claim 1 , whereinsaid precursors are mixed by ...

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11-12-2017 дата публикации

Procedimiento para la preparación de óxidos mixtos multimetálicos y su uso como catalizadores de alto desempeño en la deshidrogenación oxidativa de etano para la producción de etileno, sin formación de ácido acético u otros hidrocarburos oxigenados.

Номер: MX353055B
Принадлежит: Mexicano Inst Petrol

La deshidrogenación oxidativa de parafinas ligeras, tal como etano, a temperaturas moderadas (<500°C) para producir etileno sin la formación de productos secundarios como ácido acético y/u otros hidrocarburos oxigenados, es lograda usando catalizadores multimetálicos libres de teluro, poseyendo la fase ortorrómbica M1 y otras estructuras cristalinas que tienen una función importante en la obtención de los catalizadores de alto rendimiento para la deshidrogenación oxidativa del etano a etileno. Tales catalizadores se prepararon usando métodos térmicos e hidrotérmicos.

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19-02-2014 дата публикации

Deshidrogenación oxidativa de etano a etileno y preparación de catalizador de óxido mezclado multimetálico para tal proceso.

Номер: ES2428442R1

Deshidrogenación oxidativa de etano a etileno y preparación de catalizador de óxido mezclado multimetálico para tal proceso.#La deshidrogenación oxidativa de parafinas ligeras, tal como etano, a temperaturas moderadas (<500ºC) para producir etileno sin la formación de productos secundarios como ácido acético y/u otros hidrocarburos oxigenados, es lograda usando catalizadores multimetálicos libres de teluro, poseyendo la fase ortorrómbica M1 y otras estructuras cristalinas que tienen una función importante en la obtención de los catalizadores de alto rendimiento para la deshidrogenación oxidativa del etano a etileno. Tales catalizadores se prepararon usando métodos térmicos e hidrotérmicos.

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09-02-2017 дата публикации

エチレンへのエタンの酸化脱水素及びこのようなプロセスのための触媒としての多金属混合酸化物の調製

Номер: JP2017031168A

【課題】酢酸及び/又は他の含酸素炭化水素のような副生成物の生成なしに、エチレンを製造するための方法の提供。 【解決手段】式(I)で表わされ組成式を有する熱的方法及び水熱法を使用して調製された斜方晶系M1相と、エチレンへのエタンの酸化脱水素のための高性能触媒を得るために重要な役割を有する他の結晶構造とを有する、テルルを含まない多金属触媒。前記触媒を使用し、適度の温度(<500℃)にて軽質パラフィン、例えばエタンの酸化脱水素を行う方法。MoV h Sb i A j O x ・・・・(I)(AはNb、W、Ga、Bi、Sn、Cu、Ti、Fe、Co、Ni、Cr、Zr、希土類金属或いは希土類アルカリ金属又はこれらの混合物;0.001≦h≦4.0;0.001≦i≦4.0;0≦j≦2.0;0.3≦i/h≦10.0;xは他の元素の原子価によって決まる値) 【選択図】図11

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07-11-2013 дата публикации

Deshidrogenación oxidativa de etano a etileno y preparación de catalizador de óxido mezclado multimetálico para tal proceso.

Номер: ES2428442A2

Deshidrogenación oxidativa de etano a etileno y preparación de catalizador de óxido mezclado multimetálico para tal proceso. La deshidrogenación oxidativa de parafinas ligeras, tal como etano, a temperaturas moderadas (<500ºC) para producir etileno sin la formación de productos secundarios como ácido acético y/u otros hidrocarburos oxigenados, es lograda usando catalizadores multimetálicos libres de teluro, poseyendo la fase ortorrómbica M1 y otras estructuras cristalinas que tienen una función importante en la obtención de los catalizadores de alto rendimiento para la deshidrogenación oxidativa del etano a etileno. Tales catalizadores se prepararon usando métodos térmicos e hidrotérmicos.

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24-04-2014 дата публикации

Oxidative dehydrogenation of ethane to ethylene and preparation of multimetallic mixed oxide catalyst for such process

Номер: CA2937242A1

Oxidative dehydrogenation of light paraffins, such as ethane at moderate temperatures (<500°C) to produce ethylene without the formation of side products such as acetic acid and/or other oxygenated hydrocarbons is achieved using tellurium-free, multimetallic catalysts possessing orthorhombic M1 phase and other crystalline structures that have an important role for obtaining high performance catalysts for the oxidative dehydrogenation of ethane to ethylene. Such catalysts are prepared using thermal and hydrothermal methods.

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04-12-2014 дата публикации

Deshidrogenación oxidativa de etano a etileno y preparación de catalizador de óxido mezclado multimetálico para tal proceso.

Номер: ES2428442B1

Deshidrogenación oxidativa de etano a etileno y preparación de catalizador de óxido mezclado multimetálico para tal proceso.#La deshidrogenación oxidativa de parafinas ligeras, tal como etano, a temperaturas moderadas (<500ºC) para producir etileno sin la formación de productos secundarios como ácido acético y/u otros hidrocarburos oxigenados, es lograda usando catalizadores multimetálicos libres de teluro, poseyendo la fase ortorrómbica M1 y otras estructuras cristalinas que tienen una función importante en la obtención de los catalizadores de alto rendimiento para la deshidrogenación oxidativa del etano a etileno. Tales catalizadores se prepararon usando métodos térmicos e hidrotérmicos.

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24-04-2014 дата публикации

Deshidrogenación oxidativa de etano a etileno y preparación de óxidos mixtos multimetálicos como catalizadores para tal proceso

Номер: WO2014062046A1

La deshidrogenación oxidativa de parafinas ligeras, tal como etano, a temperaturas moderadas (<500°C) para producir etileno sin la formación de productos secundarios como ácido acético y/u otros hidrocarburos oxigenados, es lograda usando catalizadores multimetálicos libres de teluro, poseyendo la fase ortorrómbica M1 y otras estructuras cristalinas que tienen una función importante en la obtención de los catalizadores de alto rendimiento para la deshidrogenación oxidativa del etano a etileno. Tales catalizadores se prepararon usando métodos térmicos e hidrotérmicos.

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22-11-2022 дата публикации

Catalytic formulation for producing propylene cyclic carbonate from carbon dioxide using a potassium iodide catalyst

Номер: US11504701B2
Принадлежит: INSTITUTO MEXICANO DEL PETROLEO

This invention is related to the synthesis of organic carbonates from carbon dioxide and epoxides. It is particularly focused on the production of propylene cyclic carbonate from propylene oxide. The proposed catalytic materials includes a support made of aluminum oxyhydroxide (Catapal B®), nitric acid, acetic acid and/or phosphoric acid. An important stage is the physical and chemical conditioning of the catalytic materials and to this end, experimental methodologies such as spheronization and thermal treatments were implemented prior the evaluation process.

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10-04-2018 дата публикации

Oxidative dehydrogenation of ethane to ethylene and preparation of multimetallic mixed oxide catalyst for such process

Номер: US09937486B2

Oxidative dehydrogenation of light paraffins, such as ethane at moderate temperatures (<500° C.) to produce ethylene without the formation of side products such as acetic acid and/or other oxygenated hydrocarbons is achieved using tellurium-free, multimetallic catalysts possessing orthorhombic M1 phase and other crystalline structures that have an important role for obtaining high performance catalysts for the oxidative dehydrogenation of ethane to ethylene. Such catalysts are prepared using thermal and hydrothermal methods.

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09-08-2016 дата публикации

Oxidative dehydrogenation of ethane to ethylene and preparation of multimetallic mixed oxide catalyst for such process

Номер: US09409156B2

Oxidative dehydrogenation of light paraffins, such as ethane at moderate temperatures (<500° C.) to produce ethylene without the formation of side products such as acetic acid and/or other oxygenated hydrocarbons is achieved using tellurium-free, multimetallic catalysts possessing orthorhombic M1 phase and other crystalline structures that have an important role for obtaining high performance catalysts for the oxidative dehydrogenation of ethane to ethylene. Such catalysts are prepared using thermal and hydrothermal methods.

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