BR112012015219A2 - processo para iniciar um catalisador de óxido de etileno altamente seletivo - Google Patents
processo para iniciar um catalisador de óxido de etileno altamente seletivoInfo
- Publication number
- BR112012015219A2 BR112012015219A2 BR112012015219A BR112012015219A BR112012015219A2 BR 112012015219 A2 BR112012015219 A2 BR 112012015219A2 BR 112012015219 A BR112012015219 A BR 112012015219A BR 112012015219 A BR112012015219 A BR 112012015219A BR 112012015219 A2 BR112012015219 A2 BR 112012015219A2
- Authority
- BR
- Brazil
- Prior art keywords
- temperature
- initiating
- hours
- catalyst
- ethylene oxide
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D301/00—Preparation of oxiranes
- C07D301/02—Synthesis of the oxirane ring
- C07D301/03—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
- C07D301/04—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen
- C07D301/08—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen in the gaseous phase
- C07D301/10—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen in the gaseous phase with catalysts containing silver or gold
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/32—Manganese, technetium or rhenium
- B01J23/36—Rhenium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/04—Ethylene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D301/00—Preparation of oxiranes
- C07D301/02—Synthesis of the oxirane ring
- C07D301/03—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D303/00—Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
- C07D303/02—Compounds containing oxirane rings
- C07D303/04—Compounds containing oxirane rings containing only hydrogen and carbon atoms in addition to the ring oxygen atoms
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Epoxy Compounds (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
processo para iniciar um catalisador de óxido de etileno altamente seletivo é provido de partida para epoxidação de etileno. o processo inclui iniciar uma reação de epoxidação reagindo uma composição de gás de alimentação na presença de um catalisador de epoxidação a um primeira temperatura de cerca de 108 °c a cerca de 210 °c. a primeira temperatura é aumentada para uma segunda temperatura de cerca de 230 °c a cerca de 290 °c, por um período de tempo de cerca de 6 horas a cerca de 50 horas, simultaneamente adicionando uma concentração suficiente de moderador de forma que a quantidade de moderador absorvida no catalisador depois de atingir a segunda temperatura seja cerca de 10 a cerca de 50 g/m ^3^ de catalisador. a segunda temperatura é mantida por cerca de 50 horas a cerca de 350 horas, regulando ao mesmo tempo a composição de gás de alimentação para conter cerca de 0,5 % a cerca de 25 % de co ~2~. a segunda temperatura é diminuída para uma terceira temperatura, simultaneamente aumentando a concentração do moderador para um nível maior que a concentração suficiente.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US28971909P | 2009-12-23 | 2009-12-23 | |
US61/289,719 | 2009-12-23 | ||
PCT/US2010/061192 WO2011079056A2 (en) | 2009-12-23 | 2010-12-20 | A process for initiating a highly selective ethylene oxide catalyst |
Publications (2)
Publication Number | Publication Date |
---|---|
BR112012015219A2 true BR112012015219A2 (pt) | 2015-09-22 |
BR112012015219B1 BR112012015219B1 (pt) | 2018-04-03 |
Family
ID=44152005
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BR112012015219-0A BR112012015219B1 (pt) | 2009-12-23 | 2010-12-20 | Processo para iniciar um catalisador de óxido de etileno altamente seletivo |
Country Status (12)
Country | Link |
---|---|
US (1) | US8487123B2 (pt) |
EP (1) | EP2521718B1 (pt) |
JP (1) | JP2013515730A (pt) |
KR (1) | KR101815664B1 (pt) |
CN (1) | CN102666515B (pt) |
BR (1) | BR112012015219B1 (pt) |
CA (1) | CA2784603C (pt) |
IN (1) | IN2012DN05077A (pt) |
MX (1) | MX2012007440A (pt) |
RU (1) | RU2538969C2 (pt) |
TW (1) | TWI485142B (pt) |
WO (1) | WO2011079056A2 (pt) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103547365B (zh) * | 2011-04-11 | 2016-03-16 | 陶氏技术投资有限责任公司 | 调节高效环氧乙烷催化剂的方法 |
EP2768815B2 (en) * | 2011-10-18 | 2021-12-29 | Scientific Design Company, Inc. | Epoxidation process with added moderator |
EP2920159B1 (en) | 2012-12-31 | 2020-02-12 | Scientific Design Company Inc. | Start-up process for high selectivity ethylene oxide catalysts |
KR102155073B1 (ko) * | 2013-01-11 | 2020-09-11 | 사이언티픽 디자인 컴파니 인코포레이티드 | 후-컨디셔닝 단계를 이용하는 에폭시화 공정 |
US9221776B2 (en) * | 2013-12-23 | 2015-12-29 | Scientific Design Company, Inc. | Epoxidation process |
US11059017B2 (en) | 2017-09-15 | 2021-07-13 | MultiPhase Solutions, Inc. | Halogen selective detection gas chromatography for the on-line analysis and control of selective oxidation chemical production processes |
CN114057669B (zh) * | 2020-07-29 | 2023-12-08 | 中国石油化工股份有限公司 | 一种乙烯环氧化恒温开车方法 |
CN114057670A (zh) * | 2020-07-29 | 2022-02-18 | 中国石油化工股份有限公司 | 一种用于启动乙烯环氧化工艺的方法 |
CN114436998A (zh) * | 2020-11-05 | 2022-05-06 | 中国石油化工股份有限公司 | 一种乙烯环氧化开车方法 |
Family Cites Families (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2279469A (en) * | 1942-04-14 | Process of making olefin oxides | ||
SE321462B (pt) | 1962-10-10 | 1970-03-09 | Halcon International Inc | |
GB1170663A (en) * | 1967-03-22 | 1969-11-12 | Shell Int Research | Process for preparing Silver Catalysts |
US3702259A (en) * | 1970-12-02 | 1972-11-07 | Shell Oil Co | Chemical production of metallic silver deposits |
US4761394A (en) * | 1986-10-31 | 1988-08-02 | Shell Oil Company | Ethylene oxide catalyst and process for preparing the catalyst |
US4766105A (en) * | 1986-10-31 | 1988-08-23 | Shell Oil Company | Ethylene oxide catalyst and process for preparing the catalyst |
US5057481A (en) * | 1987-02-20 | 1991-10-15 | Union Carbide Chemicals And Plastics Technology Corporation | Catalyst composition for oxidation of ethylene to ethylene oxide |
US4908343A (en) * | 1987-02-20 | 1990-03-13 | Union Carbide Chemicals And Plastics Company Inc. | Catalyst composition for oxidation of ethylene to ethylene oxide |
CA1339317C (en) | 1988-07-25 | 1997-08-19 | Ann Marie Lauritzen | Process for producing ethylene oxide |
US4874879A (en) * | 1988-07-25 | 1989-10-17 | Shell Oil Company | Process for starting-up an ethylene oxide reactor |
DE68925767T2 (de) * | 1988-08-30 | 1996-08-14 | Union Carbide Corp | Katalysatoren für die Herstellung von Ethylenoxid und Verfahren zur deren Herstellung |
US5187140A (en) * | 1989-10-18 | 1993-02-16 | Union Carbide Chemicals & Plastics Technology Corporation | Alkylene oxide catalysts containing high silver content |
US5102848A (en) * | 1990-09-28 | 1992-04-07 | Union Carbide Chemicals & Plastics Technology Corporation | Catalyst composition for oxidation of ethylene to ethylene oxide |
US5155242A (en) * | 1991-12-05 | 1992-10-13 | Shell Oil Company | Process for starting-up an ethylene oxide reactor |
US5407888A (en) * | 1992-05-12 | 1995-04-18 | Basf Aktiengesellschaft | Silver catalyst |
US6492065B2 (en) * | 1997-12-05 | 2002-12-10 | Victor Company Of Japan, Limited | Hologram color filter, production method of the same hologram color filter and space light modulating apparatus using the same hologram color filter |
US6008388A (en) * | 1998-04-16 | 1999-12-28 | Arco Chemical Technology, L.P. | Epoxidation process |
JP4042332B2 (ja) | 2001-02-27 | 2008-02-06 | 三菱化学株式会社 | レニウム含有触媒を用いるオレフィンオキシドの製造方法 |
CN100376561C (zh) * | 2002-06-28 | 2008-03-26 | 国际壳牌研究有限公司 | 环氧化方法的开车方法、烯烃环氧化的催化剂和方法 |
WO2004002954A2 (en) | 2002-06-28 | 2004-01-08 | Shell Internationale Research Maatschappij B.V. | A method for improving the selectivity of a catalyst and a process for the epoxidation of an olefin |
RU2005102097A (ru) * | 2002-06-28 | 2005-08-27 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL) | Способ введения в действие способа эпоксидирования и способ эпоксидирования олефина |
US6992209B2 (en) * | 2002-12-09 | 2006-01-31 | Battelle Memorial Institute | Methods of forming alpha, beta-unsaturated acids and esters |
WO2005035513A1 (en) * | 2003-09-29 | 2005-04-21 | Union Carbide Chemicals & Plastics Technology Corporation | A process for the production of alkylene oxide using a gas-phase promoter system |
US8791280B2 (en) * | 2005-08-10 | 2014-07-29 | Sd Lizenzverwertungsgesellschaft Mbh & Co. Kg | Process for preparation of catalyst carrier and its use in catalyst preparation |
WO2008140714A1 (en) | 2007-05-11 | 2008-11-20 | Billig Barry J | Start-up of high selectivity catalysts in olefin oxide plants |
US7553980B2 (en) * | 2007-09-26 | 2009-06-30 | Sd Lizenzverwertungsgesellschaft Mbh & Co. Kg | Process for initiating a highly selective ethylene oxide catalyst |
CA2723517C (en) * | 2008-05-07 | 2017-03-07 | Shell Internationale Research Maatschappij B.V. | A process for the start-up of an epoxidation process, a process for the production of ethylene oxide, a 1,2-diol, a 1,2-diol ether, a 1,2-carbonate, or an alkanolamine |
-
2010
- 2010-12-20 BR BR112012015219-0A patent/BR112012015219B1/pt not_active IP Right Cessation
- 2010-12-20 CN CN201080058923.2A patent/CN102666515B/zh not_active Expired - Fee Related
- 2010-12-20 KR KR1020127019490A patent/KR101815664B1/ko active IP Right Grant
- 2010-12-20 WO PCT/US2010/061192 patent/WO2011079056A2/en active Application Filing
- 2010-12-20 CA CA2784603A patent/CA2784603C/en not_active Expired - Fee Related
- 2010-12-20 RU RU2012131369/04A patent/RU2538969C2/ru not_active IP Right Cessation
- 2010-12-20 MX MX2012007440A patent/MX2012007440A/es unknown
- 2010-12-20 IN IN5077DEN2012 patent/IN2012DN05077A/en unknown
- 2010-12-20 JP JP2012546098A patent/JP2013515730A/ja not_active Ceased
- 2010-12-20 EP EP10840020.1A patent/EP2521718B1/en not_active Revoked
- 2010-12-22 TW TW099145234A patent/TWI485142B/zh not_active IP Right Cessation
- 2010-12-23 US US12/977,549 patent/US8487123B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP2521718B1 (en) | 2014-07-02 |
RU2538969C2 (ru) | 2015-01-10 |
TWI485142B (zh) | 2015-05-21 |
RU2012131369A (ru) | 2014-01-27 |
WO2011079056A2 (en) | 2011-06-30 |
MX2012007440A (es) | 2012-07-23 |
US20110152549A1 (en) | 2011-06-23 |
US8487123B2 (en) | 2013-07-16 |
CA2784603C (en) | 2018-06-12 |
CN102666515A (zh) | 2012-09-12 |
JP2013515730A (ja) | 2013-05-09 |
CA2784603A1 (en) | 2011-06-30 |
CN102666515B (zh) | 2015-05-20 |
TW201139392A (en) | 2011-11-16 |
IN2012DN05077A (pt) | 2015-10-09 |
EP2521718A2 (en) | 2012-11-14 |
KR101815664B1 (ko) | 2018-01-05 |
KR20120108029A (ko) | 2012-10-04 |
BR112012015219B1 (pt) | 2018-04-03 |
WO2011079056A3 (en) | 2011-11-17 |
EP2521718A4 (en) | 2013-06-19 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
B09A | Decision: intention to grant [chapter 9.1 patent gazette] | ||
B16A | Patent or certificate of addition of invention granted [chapter 16.1 patent gazette] | ||
B21F | Lapse acc. art. 78, item iv - on non-payment of the annual fees in time |
Free format text: REFERENTE A 9A ANUIDADE. |
|
B24J | Lapse because of non-payment of annual fees (definitively: art 78 iv lpi, resolution 113/2013 art. 12) |
Free format text: EM VIRTUDE DA EXTINCAO PUBLICADA NA RPI 2545 DE 15-10-2019 E CONSIDERANDO AUSENCIA DE MANIFESTACAO DENTRO DOS PRAZOS LEGAIS, INFORMO QUE CABE SER MANTIDA A EXTINCAO DA PATENTE E SEUS CERTIFICADOS, CONFORME O DISPOSTO NO ARTIGO 12, DA RESOLUCAO 113/2013. |