MX2012007440A - Un proceso para iniciar un catalizador de oxido de etileno altamente selectivo. - Google Patents
Un proceso para iniciar un catalizador de oxido de etileno altamente selectivo.Info
- Publication number
- MX2012007440A MX2012007440A MX2012007440A MX2012007440A MX2012007440A MX 2012007440 A MX2012007440 A MX 2012007440A MX 2012007440 A MX2012007440 A MX 2012007440A MX 2012007440 A MX2012007440 A MX 2012007440A MX 2012007440 A MX2012007440 A MX 2012007440A
- Authority
- MX
- Mexico
- Prior art keywords
- temperature
- hours
- initiating
- catalyst
- ethylene oxide
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title abstract 4
- 238000000034 method Methods 0.000 title abstract 3
- 230000000977 initiatory effect Effects 0.000 title abstract 2
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 title 1
- 238000006735 epoxidation reaction Methods 0.000 abstract 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 abstract 1
- 239000005977 Ethylene Substances 0.000 abstract 1
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 230000001105 regulatory effect Effects 0.000 abstract 1
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
Se proporciona un proceso de arranque para la epoxidación de etileno. El proceso incluye la iniciación de una reacción de epoxidación para hacer reaccionar una composición deI gas de alimentación en la presencia de un catalizador de epoxidación en una primera temperatura de aproximadamente 180°C hasta aproximadamente 210°C. La primera temperatura es aumentada a una segunda temperatura de aproximadamente 230°C hasta aproximadamente 290°C, por un período de tiempo de aproximadamente seis horas hasta aproximadamente 50 horas, mientras se agrega simultáneamente una concentración suficiente del moderador de modo que la cantidad del moderador adsorbida en el catalizador después de lograr la segunda temperatura es de aproximadamente 10 g/m3 hasta aproximadamente 50 g/m3 de catalizador. La segunda temperatura es mantenida por un período de aproximadamente 50 horas hasta aproximadamente 350 horas, mientras se regula la composición del gas de alimentación para contener de aproximadamente el 0.5% hasta aproximadamente el 25% de CO2. La segunda temperatura es disminuida a una tercera temperatura, mientras se aumenta simultáneamente la concentración del moderador a un nivel mayor que la concentración suficiente.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US28971909P | 2009-12-23 | 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 (1)
| Publication Number | Publication Date |
|---|---|
| MX2012007440A true MX2012007440A (es) | 2012-07-23 |
Family
ID=44152005
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MX2012007440A MX2012007440A (es) | 2009-12-23 | 2010-12-20 | Un proceso para iniciar un catalizador de oxido de etileno altamente selectivo. |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US8487123B2 (es) |
| EP (1) | EP2521718B1 (es) |
| JP (1) | JP2013515730A (es) |
| KR (1) | KR101815664B1 (es) |
| CN (1) | CN102666515B (es) |
| BR (1) | BR112012015219B1 (es) |
| CA (1) | CA2784603C (es) |
| IN (1) | IN2012DN05077A (es) |
| MX (1) | MX2012007440A (es) |
| RU (1) | RU2538969C2 (es) |
| TW (1) | TWI485142B (es) |
| WO (1) | WO2011079056A2 (es) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2012141942A1 (en) * | 2011-04-11 | 2012-10-18 | Dow Technology Investments Llc | Process for conditioning a high efficiency ethylene oxide catalyst |
| 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 |
| CN105008339B (zh) * | 2013-01-11 | 2017-09-12 | 科学设计公司 | 具有后调节步骤的环氧化工艺 |
| US9221776B2 (en) * | 2013-12-23 | 2015-12-29 | Scientific Design Company, Inc. | Epoxidation process |
| WO2019055773A1 (en) | 2017-09-15 | 2019-03-21 | MultiPhase Solutions, Inc. | GAS PHASE CHROMATOGRAPHY OF SELECTIVE HALOGEN DETECTION FOR ONLINE ANALYSIS AND CONTROL OF SELECTIVE OXIDATION CHEMICAL PRODUCTION PROCESSES |
| CN114057670B (zh) * | 2020-07-29 | 2024-06-07 | 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 |
| 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 |
| 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 (es) | 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 |
| US4908343A (en) * | 1987-02-20 | 1990-03-13 | Union Carbide Chemicals And Plastics Company Inc. | Catalyst composition for oxidation of ethylene to ethylene oxide |
| US5057481A (en) * | 1987-02-20 | 1991-10-15 | Union Carbide Chemicals And Plastics Technology Corporation | Catalyst composition for oxidation of ethylene to ethylene oxide |
| US4874879A (en) * | 1988-07-25 | 1989-10-17 | Shell Oil Company | Process for starting-up an ethylene oxide reactor |
| CA1339317C (en) | 1988-07-25 | 1997-08-19 | Ann Marie Lauritzen | Process for producing ethylene oxide |
| EP0357292A1 (en) * | 1988-08-30 | 1990-03-07 | Imperial Chemical Industries Plc | Production of ethylene oxide and catalysts therefor |
| 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 |
| 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 |
| CA2490892C (en) * | 2002-06-28 | 2012-03-20 | Shell Internationale Research Maatschappij B.V. | A method for the start-up of an epoxidation process, a catalyst and a process for the epoxidation of an olefin |
| 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 |
| US6992209B2 (en) * | 2002-12-09 | 2006-01-31 | Battelle Memorial Institute | Methods of forming alpha, beta-unsaturated acids and esters |
| ATE483701T1 (de) * | 2003-09-29 | 2010-10-15 | Dow Technology Investments Llc | Verfahren zur herstellung von alkylenoxid unter anwendung eines gasphasenpromotorsystems |
| 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 |
| JP2010527352A (ja) | 2007-05-11 | 2010-08-12 | ビリッグ,バリー,ジェイ. | 酸化オレフィンプラントにおける高選択性触媒の開始 |
| US7553980B2 (en) * | 2007-09-26 | 2009-06-30 | Sd Lizenzverwertungsgesellschaft Mbh & Co. Kg | Process for initiating a highly selective ethylene oxide catalyst |
| BRPI0912381A2 (pt) * | 2008-05-07 | 2017-07-04 | Shell Int Research | processo para a partida de um processo de epoxidação, processo para a produção de óxido de etileno, 1,2-diol, 1, 2-diol éter, 1, 2-carbonato, ou uma alcanolamina |
-
2010
- 2010-12-20 WO PCT/US2010/061192 patent/WO2011079056A2/en not_active Ceased
- 2010-12-20 MX MX2012007440A patent/MX2012007440A/es unknown
- 2010-12-20 IN IN5077DEN2012 patent/IN2012DN05077A/en unknown
- 2010-12-20 CN CN201080058923.2A patent/CN102666515B/zh not_active Expired - Fee Related
- 2010-12-20 RU RU2012131369/04A patent/RU2538969C2/ru not_active IP Right Cessation
- 2010-12-20 EP EP10840020.1A patent/EP2521718B1/en not_active Revoked
- 2010-12-20 CA CA2784603A patent/CA2784603C/en not_active Expired - Fee Related
- 2010-12-20 BR BR112012015219-0A patent/BR112012015219B1/pt not_active IP Right Cessation
- 2010-12-20 KR KR1020127019490A patent/KR101815664B1/ko not_active Expired - Fee Related
- 2010-12-20 JP JP2012546098A patent/JP2013515730A/ja not_active Ceased
- 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 |
|---|---|
| IN2012DN05077A (es) | 2015-10-09 |
| EP2521718A4 (en) | 2013-06-19 |
| TWI485142B (zh) | 2015-05-21 |
| EP2521718A2 (en) | 2012-11-14 |
| CA2784603C (en) | 2018-06-12 |
| US20110152549A1 (en) | 2011-06-23 |
| KR20120108029A (ko) | 2012-10-04 |
| EP2521718B1 (en) | 2014-07-02 |
| BR112012015219B1 (pt) | 2018-04-03 |
| US8487123B2 (en) | 2013-07-16 |
| CN102666515A (zh) | 2012-09-12 |
| RU2538969C2 (ru) | 2015-01-10 |
| WO2011079056A2 (en) | 2011-06-30 |
| WO2011079056A3 (en) | 2011-11-17 |
| CA2784603A1 (en) | 2011-06-30 |
| TW201139392A (en) | 2011-11-16 |
| CN102666515B (zh) | 2015-05-20 |
| RU2012131369A (ru) | 2014-01-27 |
| JP2013515730A (ja) | 2013-05-09 |
| KR101815664B1 (ko) | 2018-01-05 |
| BR112012015219A2 (pt) | 2015-09-22 |
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