JP2001505129A5 - - Google Patents

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JP2001505129A5
JP2001505129A5 JP1999517553A JP51755399A JP2001505129A5 JP 2001505129 A5 JP2001505129 A5 JP 2001505129A5 JP 1999517553 A JP1999517553 A JP 1999517553A JP 51755399 A JP51755399 A JP 51755399A JP 2001505129 A5 JP2001505129 A5 JP 2001505129A5
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JP
Japan
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JP1999517553A
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JP2001505129A (ja
JP4596377B2 (ja
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Priority claimed from US08/932,075 external-priority patent/US6013597A/en
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Figure 2001505129
Figure 2001505129
Figure 2001505129
Figure 2001505129
JP51755399A 1997-09-17 1998-09-15 エタンから酢酸への酸化用触媒と、その形成方法およびその使用方法 Expired - Lifetime JP4596377B2 (ja)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US08/932,075 US6013597A (en) 1997-09-17 1997-09-17 Catalysts for the oxidation of ethane to acetic acid processes of making same and, processes of using same
US08/932,075 1997-09-17
PCT/GB1998/002791 WO1999013980A1 (en) 1997-09-17 1998-09-15 Catalysts for the oxidation of ethane to acetic acid, processes of making same and processes of using same

Publications (3)

Publication Number Publication Date
JP2001505129A JP2001505129A (ja) 2001-04-17
JP2001505129A5 true JP2001505129A5 (ja) 2006-01-05
JP4596377B2 JP4596377B2 (ja) 2010-12-08

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ID=25461731

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JP51755399A Expired - Lifetime JP4596377B2 (ja) 1997-09-17 1998-09-15 エタンから酢酸への酸化用触媒と、その形成方法およびその使用方法

Country Status (6)

Country Link
US (2) US6013597A (ja)
EP (1) EP0938378B1 (ja)
JP (1) JP4596377B2 (ja)
CN (1) CN1105599C (ja)
DE (1) DE69828026T2 (ja)
WO (1) WO1999013980A1 (ja)

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US6977064B1 (en) 2000-05-05 2005-12-20 Saudi Basic Industries Corporation Apparatus for the controlled optimized addition of reactants in continuous flow reaction systems
ES2192983B1 (es) * 2002-01-31 2004-09-16 Universidad Politecnica De Valencia. Un catalizador para la deshidrogenacion oxidativa de etano a eteno.
EP1691921A1 (en) * 2003-12-18 2006-08-23 Avantium International B.V. Catalysts for alkane or alkene oxidation and ammoxidation
BRPI0611208A2 (pt) * 2005-06-01 2010-08-24 Celanese Int Corp processo para preparar etileno a partir de alimentaÇço gasosa que compreende etano e oxigÊnio e processo para oxidar etano para produzir etileno e Ácido acÉtico
US7795469B2 (en) * 2006-12-21 2010-09-14 Rohm And Haas Company Process for the selective (AMM) oxidation of lower molecular weight alkanes and alkenes
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KR101939821B1 (ko) * 2013-08-30 2019-01-17 사빅 글로벌 테크놀러지스 비.브이. 방향족 알코올의 에스테르 교환반응을 위한 불균일계 촉매； 및 그의 제조 방법 및 용도
CN103920516B (zh) * 2014-04-15 2016-03-16 高丽娜 可用于烷烃氧化的催化剂制备方法
CN105727978B (zh) * 2014-12-06 2018-01-16 中国石油化工股份有限公司 一种用于乙烷氧化脱氢制乙烯的催化剂制备方法
CN108114731A (zh) * 2016-11-26 2018-06-05 中国科学院大连化学物理研究所 用于氧化反应的催化剂组合物
US10793502B2 (en) 2016-12-19 2020-10-06 Sabic Global Technologies B.V. Method of purifying acetic acid
WO2020194228A1 (en) 2019-03-26 2020-10-01 Sabic Global Technologies B.V. Method of reactivating catalyst
CN116328755A (zh) * 2021-12-22 2023-06-27 中国石油天然气股份有限公司 复合氧化物催化剂及其制备方法与应用
CN116408061A (zh) * 2021-12-31 2023-07-11 中国石油天然气股份有限公司 乙烷选择氧化制乙酸和乙烯的催化剂及其制备方法与应用
EP4342873A1 (de) 2022-09-26 2024-03-27 Linde GmbH Verfahren und anlage zur herstellung von ethylen und essigsäure, verfahren und anlage zur herstellung einer zielverbindung unter verwendung von ethylen und essigsäure

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