JP2006502982A5 - - Google Patents

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Publication number
JP2006502982A5
JP2006502982A5 JP2004517759A JP2004517759A JP2006502982A5 JP 2006502982 A5 JP2006502982 A5 JP 2006502982A5 JP 2004517759 A JP2004517759 A JP 2004517759A JP 2004517759 A JP2004517759 A JP 2004517759A JP 2006502982 A5 JP2006502982 A5 JP 2006502982A5
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Japan
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catalyst
organic halide
mol
concentration
feedstock
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JP2004517759A
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English (en)
Japanese (ja)
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JP2006502982A (ja
JP4624101B2 (ja
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Priority claimed from PCT/US2003/019828 external-priority patent/WO2004002971A1/en
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Publication of JP2006502982A5 publication Critical patent/JP2006502982A5/ja
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Publication of JP4624101B2 publication Critical patent/JP4624101B2/ja
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JP2004517759A 2002-06-28 2003-06-24 エポキシ化法の始動方法、触媒及びオレフィンのエポキシ化法 Expired - Fee Related JP4624101B2 (ja)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US39249902P 2002-06-28 2002-06-28
PCT/US2003/019828 WO2004002971A1 (en) 2002-06-28 2003-06-24 A method for the start-up of an epoxidation process, a catalyst and a process for the epoxidation of an olefin

Related Child Applications (1)

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JP2010165897A Division JP5431262B2 (ja) 2002-06-28 2010-07-23 エポキシ化法の始動方法、触媒及びオレフィンのエポキシ化法

Publications (3)

Publication Number Publication Date
JP2006502982A JP2006502982A (ja) 2006-01-26
JP2006502982A5 true JP2006502982A5 (https=) 2010-09-24
JP4624101B2 JP4624101B2 (ja) 2011-02-02

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JP2004517759A Expired - Fee Related JP4624101B2 (ja) 2002-06-28 2003-06-24 エポキシ化法の始動方法、触媒及びオレフィンのエポキシ化法
JP2010165897A Expired - Lifetime JP5431262B2 (ja) 2002-06-28 2010-07-23 エポキシ化法の始動方法、触媒及びオレフィンのエポキシ化法

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JP2010165897A Expired - Lifetime JP5431262B2 (ja) 2002-06-28 2010-07-23 エポキシ化法の始動方法、触媒及びオレフィンのエポキシ化法

Country Status (14)

Country Link
EP (1) EP1532125B1 (https=)
JP (2) JP4624101B2 (https=)
KR (1) KR101098051B1 (https=)
CN (1) CN100376561C (https=)
AU (1) AU2003243758A1 (https=)
BR (1) BR0312011B1 (https=)
CA (1) CA2490892C (https=)
DE (1) DE60304197T2 (https=)
IN (1) IN2004DE03915A (https=)
MX (1) MX257124B (https=)
MY (1) MY134316A (https=)
RU (1) RU2311229C2 (https=)
TW (1) TWI340743B (https=)
WO (1) WO2004002971A1 (https=)

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US8148555B2 (en) 2003-06-26 2012-04-03 Shell Oil Company Method for improving the selectivity of a catalyst and a process for the epoxidation of an olefin
US8536083B2 (en) 2004-09-01 2013-09-17 Shell Oil Company Olefin epoxidation process, a catalyst for use in the process, a carrier for use in preparing the catalyst, and a process for preparing the carrier
EP2013194A2 (de) * 2006-04-21 2009-01-14 Basf Se Verfahren zur herstellung von ethylenoxid in einem mikrokanalreaktor
AR066469A1 (es) 2007-05-09 2009-08-19 Shell Int Research Un proceso de produccion de oxido de olefina , 1,2- diol, 1,2- diol eter, 1,2- carbonato o alcanolamina
CN101715444B (zh) * 2007-05-09 2012-11-21 国际壳牌研究有限公司 环氧化催化剂及其制备方法和生产环氧烷、1,2-二醇、1,2-二醇醚、1,2-碳酸酯或烷醇胺的方法
JP5542659B2 (ja) 2007-05-09 2014-07-09 シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー エポキシ化触媒、触媒を調製する方法、および酸化オレフィン、１，２−ジオール、１，２−ジオールエーテル、１，２−カーボネートまたはアルカノールアミンの製造方法
RU2452564C2 (ru) * 2007-05-11 2012-06-10 Барри Дж. БИЛЛИГ Активация высокоселективных катализаторов в установках синтеза оксидов олефинов
US7553980B2 (en) * 2007-09-26 2009-06-30 Sd Lizenzverwertungsgesellschaft Mbh & Co. Kg Process for initiating a highly selective ethylene oxide catalyst
DE102008011767B4 (de) 2008-02-28 2012-07-26 Basf Se Verfahren zur Herstellung von olefinisch ungesättigten Carbonylverbindungen durch oxidative Dehydrierung von Alkoholen
DE102008014910A1 (de) 2008-03-19 2009-09-24 Basf Se Verwendung eines geträgerten edelmetallhaltigen Katalysators zur oxidativen Dehydrierung
KR101629037B1 (ko) 2008-05-07 2016-06-09 셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이 에폭시화 방법의 스타트업 방법, 산화에틸렌, 1,2-디올, 1,2-디올 에테르, 1,2-카보네이트 또는 알칸올아민의 생산방법
CA2723592C (en) 2008-05-07 2016-08-16 Shell Internationale Research Maatschappij B.V. A process for the production of an olefin oxide, a 1,2-diol, a 1,2-diol ether, a 1,2-carbonate, or an alkanolamine
CN102099345A (zh) * 2008-07-14 2011-06-15 万罗赛斯公司 使用微通道工艺技术制造环氧乙烷的方法
US8933254B2 (en) 2008-07-14 2015-01-13 Basf Se Process for making ethylene oxide
CN101497045B (zh) * 2009-03-11 2011-03-30 华东理工大学 一种丙烯液相一步氧化制环氧丙烷用催化剂及制备方法
CA2759397C (en) 2009-04-21 2019-01-29 Dow Technology Investments Llc Improved method of achieving and maintaining a specified alkylene oxide production parameter with a high efficiency catalyst
US8524927B2 (en) 2009-07-13 2013-09-03 Velocys, Inc. Process for making ethylene oxide using microchannel process technology
EP2513077B1 (en) * 2009-12-17 2014-06-11 Scientific Design Company Inc. Process for epoxidation start-up
CN102666515B (zh) * 2009-12-23 2015-05-20 科学设计公司 高选择性氧化乙烯催化剂启动的方法
US8742147B2 (en) 2010-12-08 2014-06-03 Shell Oil Company Process for improving the selectivity of an EO catalyst
US8742146B2 (en) * 2010-12-08 2014-06-03 Shell Oil Company Process for improving the selectivity of an EO catalyst
SG190901A1 (en) 2010-12-15 2013-07-31 Dow Technology Investments Llc Method of starting-up a process of producing an alkylene oxide using a high-efficiency catalyst
WO2012141942A1 (en) 2011-04-11 2012-10-18 Dow Technology Investments Llc Process for conditioning a high efficiency ethylene oxide catalyst
BR112013027585B1 (pt) 2011-04-29 2020-09-29 Shell Internationale Research Maatschappij B.V Método para melhorar a seletividade de um catalisador de alta seletividade suportado usado na epoxidação de etileno e método para preparar um 1,2-diol, um 1,2-diol éter, um 1,2-carbonato ou uma alcanolamina
WO2013043458A1 (en) * 2011-09-22 2013-03-28 Shell Oil Company A process for the start-up of an epoxidation process
CN103360346B (zh) * 2012-04-06 2015-02-11 中国石油化工股份有限公司 一种高选择性银催化剂催化乙烯氧化制环氧乙烷的方法
KR102155068B1 (ko) 2012-12-31 2020-09-11 사이언티픽 디자인 컴파니 인코포레이티드 고 선택성 산화에틸렌 촉매를 위한 스타트-업 공정
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US11801493B2 (en) 2016-12-02 2023-10-31 Shell Usa, Inc. Methods for conditioning an ethylene epoxidation catalyst and associated methods for the production of ethylene oxide
CN113121474A (zh) * 2019-12-30 2021-07-16 中国石油化工股份有限公司 乙烯环氧化银催化剂的开车方法

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