RU2000109957A - CATALYSTS AND WAYS OF THEIR APPLICATION - Google Patents

CATALYSTS AND WAYS OF THEIR APPLICATION

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Publication number
RU2000109957A
RU2000109957A RU2000109957/04A RU2000109957A RU2000109957A RU 2000109957 A RU2000109957 A RU 2000109957A RU 2000109957/04 A RU2000109957/04 A RU 2000109957/04A RU 2000109957 A RU2000109957 A RU 2000109957A RU 2000109957 A RU2000109957 A RU 2000109957A
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RU
Russia
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paragraphs
copper
range
catalyst
cobalt
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RU2000109957/04A
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Russian (ru)
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RU2203880C2 (en
Inventor
БЮЭ Филипп
Франс Иво КАЭ Рафаэль
ФРЕННТ Альфред
ГЕННЕ Эрик
ЮБЕР Клод
КРУЗЕ Норберт
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Эксон Кемикэл Пейтентс Инк.
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Priority claimed from GBGB9720593.4A external-priority patent/GB9720593D0/en
Application filed by Эксон Кемикэл Пейтентс Инк. filed Critical Эксон Кемикэл Пейтентс Инк.
Publication of RU2000109957A publication Critical patent/RU2000109957A/en
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Publication of RU2203880C2 publication Critical patent/RU2203880C2/en

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Claims (22)

1. Способ получения спиртов и олефинов из монооксида углерода и водорода, который осуществляют в присутствии каталитической композиции, включающей катализатор синтеза высших спиртов, по меньшей мере один металл, выбранный из группы, включающей магний и марганец, и необязательный щелочной металл или щелочноземельный металл, причем эта каталитическая композиция может быть приготовлена соосаждением в качестве его существенного компонента металлических элементов в форме оксалатов.1. The method of producing alcohols and olefins from carbon monoxide and hydrogen, which is carried out in the presence of a catalytic composition comprising a catalyst for the synthesis of higher alcohols, at least one metal selected from the group consisting of magnesium and manganese, and an optional alkali metal or alkaline earth metal, this catalyst composition can be prepared by coprecipitation as its essential component of metal elements in the form of oxalates. 2. Способ по п. 1, в котором катализатор синтеза высших спиртов включает кобальт и медь. 2. The method according to p. 1, in which the catalyst for the synthesis of higher alcohols includes cobalt and copper. 3. Способ по п. 2, в котором каталитическая композиция включает кобальт, медь и марганец при атомных соотношениях Co: Cu: Mn в интервале 1: 1-10: 0,1-5. 3. The method according to p. 2, in which the catalytic composition comprises cobalt, copper and manganese at atomic ratios Co: Cu: Mn in the range of 1: 1-10: 0.1-5. 4. Способ по п. 1, в котором каталитическая композиция включает кобальт, медь и марганец при атомных соотношениях Co: Cu: Mn в интервале 1: 1-10: 0,15-5, а также включает в целом не более 1 мас. % щелочного металла и щелочноземельного металла в пересчете на общую массу металла в этой каталитической композиции. 4. The method according to p. 1, in which the catalytic composition comprises cobalt, copper and manganese at atomic ratios of Co: Cu: Mn in the range of 1: 1-10: 0.15-5, and also includes a total of not more than 1 wt. % alkali metal and alkaline earth metal, calculated on the total weight of the metal in this catalyst composition. 5. Способ по п. 2, в котором каталитическая композиция включает кобальт, медь и магний при атомных соотношениях Co: Cu: Mg в интервале 1: 1-10: 0,1-10. 5. The method according to p. 2, in which the catalytic composition comprises cobalt, copper and magnesium at atomic ratios of Co: Cu: Mg in the range of 1: 1-10: 0.1-10. 6. Способ по любому из пп. 1-5, в котором катализатор или каталитическая композиция включает щелочной металл или щелочноземельный металл. 6. The method according to any one of paragraphs. 1-5, in which the catalyst or catalytic composition comprises an alkali metal or alkaline earth metal. 7. Способ по п. 6, в котором каталитическая композиция включает калий. 7. The method of claim 6, wherein the catalyst composition comprises potassium. 8. Способ по п. 1, в котором каталитическая композиция включает кобальт, медь и магний при атомных соотношениях Co: Cu: Mg в интервале 1: 1-10: 0,15-10 и включает также в целом не более 1 мас. % щелочного металла и щелочноземельного металла в пересчете на общую массу металла в каталитической композиции. 8. The method according to p. 1, in which the catalytic composition comprises cobalt, copper and magnesium at atomic ratios of Co: Cu: Mg in the range of 1: 1-10: 0.15-10 and also includes a total of not more than 1 wt. % alkali metal and alkaline earth metal, calculated on the total weight of the metal in the catalyst composition. 9. Способ по п. 1, в котором каталитическая композиция включает кобальт, медь и марганец при атомных соотношениях Co: Cu: Mn в интервале 1: 1-10: 0,1-5 или включает кобальт, медь и магний при атомных соотношениях Co: Cu: Mg в интервале 1: 1-10: 0,1-10, причем совокупная молярная фракция кобальта и меди, которые в этом катализаторе находятся в смешанной фазе, составляет по меньшей мере 25%. 9. The method according to p. 1, in which the catalytic composition comprises cobalt, copper and manganese at atomic ratios Co: Cu: Mn in the range of 1: 1-10: 0.1-5 or includes cobalt, copper and magnesium at atomic ratios Co : Cu: Mg in the range of 1: 1-10: 0.1-10, wherein the total molar fraction of cobalt and copper, which are in the mixed phase in this catalyst, is at least 25%. 10. Способ по любому из пп. 1-9, в котором каталитическая композиция не нанесена на носитель. 10. The method according to any one of paragraphs. 1-9, in which the catalyst composition is not supported. 11. Способ по любому из пп. 1-10, в котором водород и монооксид углерода используют в молярном соотношении от 1: 1 до 3: 1. 11. The method according to any one of paragraphs. 1-10, in which hydrogen and carbon monoxide are used in a molar ratio of from 1: 1 to 3: 1. 12. Способ по любому из пп. 1-11, который осуществляют при температуре в интервале 200-350oС.12. The method according to any one of paragraphs. 1-11, which is carried out at a temperature in the range of 200-350 o C. 13. Способ по любому из пп. 1-12, который осуществляют под давлением в интервале 10-150 бар. 13. The method according to any one of paragraphs. 1-12, which is carried out under pressure in the range of 10-150 bar. 14. Способ по любому из пп. 1-13, который осуществляют при объемной среднечасовой скорости подачи в интервале 2000-9000 ч-1.14. The method according to any one of paragraphs. 1-13, which is carried out at a volume hourly space velocity in the range of 2000-9000 h -1 . 15. Способ по любому из пп. 1-14, в котором количество диоксида углерода, получаемого при его осуществлении, составляет не более 20% от количества углерода в монооксиде углерода, подвергнутом конверсии. 15. The method according to any one of paragraphs. 1-14, in which the amount of carbon dioxide obtained during its implementation is not more than 20% of the amount of carbon in the carbon monoxide subjected to conversion. 16. Способ по любому из пп. 1-15, в котором катализатор или каталитическая композиция представляет собой такую, которая обеспечивает возможность получения продукта, у которого значение α по Шульцу-Флори составляет по меньшей мере 0,60. 16. The method according to any one of paragraphs. 1-15, in which the catalyst or catalytic composition is one that provides the possibility of obtaining a product in which the value of α according to Schulz-Flory is at least 0.60. 17. Способ конверсии углеродистого источника энергии первого типа, к которому относятся углеродистые источники энергии, отличные от источников второго типа, в источник второго типа, к которому относятся материалы группы, включающей жидкие и способные сжижаться спирты и/или олефины, включающий конверсию этого источника первого типа в синтез-газ и конверсию синтез-газа в источник второго типа способом по любому из предыдущих пунктов. 17. A method for converting a carbon source of energy of the first type, which includes carbon sources of energy other than sources of the second type, into a source of the second type, which includes materials of the group comprising liquid and liquefiable alcohols and / or olefins, including the conversion of this source of first type to synthesis gas and the conversion of synthesis gas to a second type source by the method according to any one of the preceding paragraphs. 18. Способ по п. 17, в котором источник энергии первого типа является газообразным или сжиженным газом. 18. The method according to p. 17, in which the energy source of the first type is a gaseous or liquefied gas. 19. Способ по п. 17 или 18, в котором источник энергии первого типа включает серу, а способ включает удаление серы. 19. The method according to p. 17 or 18, in which the energy source of the first type includes sulfur, and the method includes removing sulfur. 20. Способ приготовления каталитической композиции по любому из пп. 2-7, который включает приготовление раствора соли кобальта, соли меди и соли по меньшей мере одного металла, выбранного из марганца и магния, и одновременное осаждение металлов из раствора в форме оксалатов добавлением оксалатных ионов. 20. A method of preparing a catalyst composition according to any one of paragraphs. 2-7, which includes preparing a solution of a cobalt salt, a copper salt and a salt of at least one metal selected from manganese and magnesium, and simultaneously precipitating the metals from the solution in the form of oxalates by adding oxalate ions. 21. Способ по п. 20, в котором оксалатные ионы вводят добавлением оксалата аммония. 21. The method according to p. 20, in which the oxalate ions are introduced by the addition of ammonium oxalate. 22. Способ по п. 20 или 21, в котором образующиеся оксалаты подвергают тепловой обработке. 22. The method according to p. 20 or 21, in which the resulting oxalates are subjected to heat treatment.
RU2000109957/04A 1997-09-26 1998-09-25 Method for production of alcohols and olefins RU2203880C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9720593.4 1997-09-26
GBGB9720593.4A GB9720593D0 (en) 1997-09-26 1997-09-26 Catalysts and processes using them

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RU2000109957A true RU2000109957A (en) 2002-03-20
RU2203880C2 RU2203880C2 (en) 2003-05-10

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US (2) US6362239B1 (en)
EP (1) EP1017657B1 (en)
CN (1) CN1154629C (en)
AU (1) AU743876B2 (en)
CA (1) CA2304469A1 (en)
DE (1) DE69810493T2 (en)
DK (1) DK1017657T3 (en)
DZ (1) DZ2616A1 (en)
GB (1) GB9720593D0 (en)
MY (1) MY117735A (en)
NO (1) NO20001552L (en)
RU (1) RU2203880C2 (en)
WO (1) WO1999016732A1 (en)
ZA (1) ZA988726B (en)

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