AR106815A1 - Proceso para la epoxidación de propeno - Google Patents

Proceso para la epoxidación de propeno

Info

Publication number
AR106815A1
AR106815A1 ARP160103610A ARP160103610A AR106815A1 AR 106815 A1 AR106815 A1 AR 106815A1 AR P160103610 A ARP160103610 A AR P160103610A AR P160103610 A ARP160103610 A AR P160103610A AR 106815 A1 AR106815 A1 AR 106815A1
Authority
AR
Argentina
Prior art keywords
propene
propane
separation column
epoxidation
stream
Prior art date
Application number
ARP160103610A
Other languages
English (en)
Inventor
Dr Kleiber Michael
Brz Manfred
Dr Jaeger Bernd
Dr Brendel Marc
Dr Dietz Hans
Christian Dr Kolbe Brbel
Wll Wolfgang
Dr Haas Thomas
Hofen Willi
Original Assignee
Evonik Degussa Gmbh
Thyssenkrupp Ind Solutions Ag
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Evonik Degussa Gmbh, Thyssenkrupp Ind Solutions Ag filed Critical Evonik Degussa Gmbh
Publication of AR106815A1 publication Critical patent/AR106815A1/es

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
    • C07D301/12—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with hydrogen peroxide or inorganic peroxides or peracids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • 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
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
    • B01J29/7049—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D301/00—Preparation of oxiranes
    • C07D301/32—Separation; Purification
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/702—Hydrocarbons
    • B01D2257/7022—Aliphatic hydrocarbons
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/80—Water
    • 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
    • B01J23/24—Chromium, molybdenum or tungsten
    • B01J23/30—Tungsten

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Epoxy Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

En un proceso para la epoxidación de propeno, que comprende las etapas de hacer reaccionar el propeno con peróxido de hidrógeno, separar el óxido de propeno y un chorro de propeno recuperado de la mezcla de reacción, separar el propano de la totalidad o de una parte del chorro de propeno recuperado en una columna de separación C₃, y pasar el chorro de producto superior de la columna de separación C₃ a la etapa de epoxidación, se usa un material de partida propano con una fracción de propano de desde 0,002 hasta 0,10, la epoxidación opera para proporcionar una fracción de propano en la mezcla de reacción de desde 0,05 hasta 0,20 y la columna de separación C₃ se opera para proporcionar un chorro de producto superior que comprende una fracción de propano de al menos 0,04 con el fin de reducir el tamaño y el consumo de energía de la columna de separación C₃.
ARP160103610A 2015-11-26 2016-11-25 Proceso para la epoxidación de propeno AR106815A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP15196510 2015-11-26

Publications (1)

Publication Number Publication Date
AR106815A1 true AR106815A1 (es) 2018-02-21

Family

ID=54705120

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP160103610A AR106815A1 (es) 2015-11-26 2016-11-25 Proceso para la epoxidación de propeno

Country Status (13)

Country Link
US (1) US10428036B2 (es)
EP (1) EP3380461B1 (es)
KR (1) KR102655920B1 (es)
CN (2) CN112979586A (es)
AR (1) AR106815A1 (es)
EA (1) EA035905B1 (es)
ES (1) ES2746923T3 (es)
HU (1) HUE045534T2 (es)
MY (1) MY187663A (es)
PL (1) PL3380461T3 (es)
PT (1) PT3380461T (es)
TW (1) TWI707847B (es)
WO (1) WO2017089516A1 (es)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI707847B (zh) 2015-11-26 2020-10-21 德商贏創運營有限公司 丙烯之環氧化方法
WO2017089074A1 (en) 2015-11-26 2017-06-01 Evonik Degussa Gmbh Process for the epoxidation of an olefin
EP3405460B1 (en) 2016-01-19 2020-06-24 Evonik Operations GmbH Process for the epoxidation of an olefin
CN108884065B (zh) 2016-03-21 2022-06-07 赢创运营有限公司 丙烯的环氧化方法
EP3246323A1 (en) 2016-05-17 2017-11-22 Evonik Degussa GmbH Integrated process for making propene oxide from propane
EP3406603A1 (en) 2017-05-22 2018-11-28 Evonik Degussa GmbH Process for the epoxidation of propene
CN111467826A (zh) * 2020-05-27 2020-07-31 天津大沽化工股份有限公司 一种去除环氧丙烷产品醛类物质的装置及方法
WO2022140749A1 (en) * 2020-12-22 2022-06-30 Zymergen Inc. Decarboxylation of amino acids
CN115197171A (zh) * 2021-04-13 2022-10-18 中国石油化工股份有限公司 一种生产环氧丙烷的方法和***
CN113461474A (zh) * 2021-06-30 2021-10-01 中国石油化工股份有限公司 一种丙烷工业化连续制备环氧丙烷的***及方法

Family Cites Families (63)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4308409A (en) 1978-10-03 1981-12-29 Gulf Research & Development Company Preparation of propylene glycol from propylene
US5274140A (en) * 1979-07-19 1993-12-28 Instituto Guido Donegani, S.P.A. Process for catalytically epoxidizing olefin with hydrogen peroxide
IT1152299B (it) 1982-07-28 1986-12-31 Anic Spa Procedimento per l'espossidazione di composti olefinici
EP0230949B1 (en) 1986-01-28 1992-07-22 ENIRICERCHE S.p.A. A process for the epoxydation of olefinic compounds
CA2137310C (en) 1993-12-20 2004-02-17 John C. Jubin Jr. Catalytic converter and method for highly exothermic reactions
DE19507584C2 (de) 1995-03-04 1997-06-12 Geesthacht Gkss Forschung Strahlenchemisch modifizierte Silikonkompositmembran für die Ultrafiltration
US5591875A (en) 1995-08-02 1997-01-07 Chang; Te Epoxidation Process
US5599956A (en) 1996-02-22 1997-02-04 Uop Integrated process for the production of propylene oxide
BE1011577A3 (fr) 1997-11-27 1999-11-09 Solvay Catalyseur d'epoxydation, son utilisation et procede d'epoxydation en presence de catalyseur.
US6037484A (en) * 1998-09-22 2000-03-14 Arco Chemical Technology, L.P. Epoxidation process
DE19936547A1 (de) 1999-08-04 2001-02-15 Basf Ag Verfahren zur Umsetzung einer organischen Verbindung mit einem Hydroperoxid
DE19944839A1 (de) 1999-09-18 2001-03-22 Degussa Verfahren zur Herstellung von Epoxiden aus Olefinen
DE10052323A1 (de) 2000-10-21 2002-05-02 Degussa Kontinierliches Verfahren zur Hydrierung
EP1247805A1 (en) 2001-03-05 2002-10-09 Degussa AG Process for the epoxidation of olefins
EP1247806A1 (en) 2001-03-05 2002-10-09 Degussa AG Process for the epoxidation of olefins
EP1285915A1 (en) 2001-08-16 2003-02-26 Degussa AG Continuous process to make epoxide from olefins and hydrogen peroxide
EP1293505A1 (en) * 2001-08-22 2003-03-19 Degussa AG Process for the epoxidation of olefins
US6596883B2 (en) * 2001-08-23 2003-07-22 Degussa Ag Process for the epoxidation of olefins
JP2003081954A (ja) * 2001-09-12 2003-03-19 Sumitomo Chem Co Ltd プロピレンオキサイドの製造方法
EP1359148A1 (en) 2002-05-02 2003-11-05 Degussa AG Process for the epoxidation of olefins
DE10233385A1 (de) 2002-07-23 2004-02-12 Basf Ag Verfahren zur kontinuierlichen Herstellung von Propylenglykolen
US6914167B2 (en) * 2002-08-26 2005-07-05 Arco Chemical Technology, L.P. Vent recovery system
DE10240129B4 (de) 2002-08-30 2004-11-11 Basf Ag Integriertes Verfahren zur Synthese von Propylenoxid
EP1403219A1 (en) 2002-09-30 2004-03-31 Degussa AG Novel aqueous hydrogen peroxide solutions
DE10249378A1 (de) * 2002-10-23 2004-05-06 Basf Ag Verfahren zur kontinuierlichen Rückführung des bei der Oxidation von Olefinen mit Hydroperoxiden nicht umgesetzten Olefins mittels Verdichtung und Druckdestillation
DE10249377A1 (de) 2002-10-23 2004-05-06 Basf Ag Verfahren zu kontinuierlichen Herstellung von Epoxiden aus Olefinen und Hydroperoxiden an einem suspendierten Katalysator
DE10249379A1 (de) * 2002-10-23 2004-05-06 Basf Ag Verfahren zur kontinuierlichen Rückführung des bei der Oxidation von Olefinen mit Hydroperoxiden nicht umgesetzten Olefins mittels Lösungsmittelwäsche
TW200410921A (en) 2002-11-25 2004-07-01 Hoffmann La Roche Mandelic acid derivatives
EP1424331A1 (en) 2002-11-26 2004-06-02 Degussa AG Process for the epoxidation of olefins
US7169945B2 (en) 2002-11-26 2007-01-30 Degussa Ag Process for the epoxidation of olefins
EP1424332A1 (en) 2002-11-26 2004-06-02 Degussa AG Process for the purification of crude propene oxide
EP1489074A1 (en) 2003-06-18 2004-12-22 Degussa AG Process for the epoxidation of propene
DE10341896A1 (de) 2003-09-10 2005-04-14 Uhde Gmbh Mehrphasen-Flüssigkeitsverteiler für einen Rieselbettreaktor
DE102004003003A1 (de) 2004-01-20 2005-09-01 Basf Ag Verfahren und Vorrichtung zur kontinuierlichen Herstellung einer chemischen Verbindung
US7223876B2 (en) 2004-04-21 2007-05-29 Basf Aktiengesellschaft Method of separating an olefin from a gas stream
US20060005853A1 (en) * 2004-07-08 2006-01-12 Chien-Hung Shen Cosmetic compact
US20070004926A1 (en) 2005-06-29 2007-01-04 Basf Aktiengesellschaft Process for producing propylene oxide
DE102005031703B3 (de) 2005-07-05 2007-01-11 Gkss-Forschungszentrum Geesthacht Gmbh Kompositmembran
US20080132717A1 (en) * 2006-12-04 2008-06-05 Bernard Cooker Propylene oxide system
JP2008266304A (ja) * 2007-03-22 2008-11-06 Sumitomo Chemical Co Ltd プロピレンオキサイドの製造方法
DE102007024029A1 (de) 2007-05-22 2008-11-27 Evonik Degussa Gmbh Mehrphasen-Reaktorsumpf
CL2009000939A1 (es) 2008-04-30 2010-10-01 Evonik Degussa Gmbh Proceso para recuperar molibdato o tungstato desde una solucion acuosa que comprende a) contactar la solucion con un material portador inorganico cationizado e insoluble en agua, b) separar el material portador de molibdato o tungstato, c) contactarlo con una solucion acuosa con un ph entre 6 a 14 y d) separar el material saturado.
EP2343288A1 (en) * 2009-11-27 2011-07-13 Momentive Specialty Chemicals Research Belgium S.A. Process for the manufacture of propylene oxide
DE102009047351A1 (de) 2009-12-01 2011-06-09 Evonik Goldschmidt Gmbh Komposit-Siliconmembranen mit hoher Trennwirkung
US8785670B2 (en) * 2010-12-07 2014-07-22 Basf Se Process for the production of propylene oxide
CN103172486B (zh) * 2011-12-22 2015-07-29 中国石油化工股份有限公司 一种从直接环氧化反应产物中回收丙烯的方法
CN103172596B (zh) * 2011-12-22 2015-02-25 中国石油化工股份有限公司 一种环氧丙烷精制方法
DE102012200990A1 (de) 2012-01-24 2013-07-25 Evonik Industries Ag Verfahren zur Rückgewinnung von Molybdat bei einer mit Molybdat katalysierten Delignifizierung von Zellstoff mit Wasserstoffperoxid
CN103788025B (zh) * 2012-10-29 2015-10-28 中国石油化工股份有限公司 一种精制环氧丙烷的方法
CN104058920B (zh) * 2013-12-19 2016-03-23 武汉优立克新材料科技有限公司 一种以烷烃为萃取剂萃取精馏分离丙烯-丙烷的方法
ES2767100T3 (es) 2014-07-29 2020-06-16 Evonik Operations Gmbh Procedimiento para la epoxidación de una olefina
US10053438B2 (en) 2015-01-14 2018-08-21 Evonik Degussa Gmbh Integrated process for making propene oxide and an alkyl tert-butyl ether
WO2016113193A1 (en) 2015-01-14 2016-07-21 Evonik Degussa Gmbh Integrated process for making propene oxide and an alkyl tert-butyl ether
KR102441642B1 (ko) 2015-02-17 2022-09-07 에보닉 오퍼레이션스 게엠베하 과산화 수소를 이용한 올레핀의 에폭시화 방법
TW201700464A (zh) 2015-02-17 2017-01-01 贏創德固賽有限責任公司 使用過氧化氫之使烯烴環氧化方法
EP3059230A1 (en) 2015-02-17 2016-08-24 Evonik Degussa GmbH Method for the epoxidation of propene with hydrogen peroxide
EP3059229A1 (en) 2015-02-17 2016-08-24 Evonik Degussa GmbH Method for the epoxidation of an olefin with hydrogen peroxide
PL3288927T3 (pl) 2015-04-28 2020-03-31 Evonik Degussa Gmbh Sposób epoksydacji propenu
CN108779053B (zh) 2015-11-25 2021-08-31 赢创运营有限公司 由丙烯和过氧化氢产生丙二醇的方法
WO2017089074A1 (en) 2015-11-26 2017-06-01 Evonik Degussa Gmbh Process for the epoxidation of an olefin
TWI707847B (zh) 2015-11-26 2020-10-21 德商贏創運營有限公司 丙烯之環氧化方法
EP3380460B1 (en) 2015-11-26 2021-04-21 Evonik Operations GmbH Process and reactor for the epoxidation of propene
EP3405460B1 (en) 2016-01-19 2020-06-24 Evonik Operations GmbH Process for the epoxidation of an olefin

Also Published As

Publication number Publication date
CN108290852A (zh) 2018-07-17
US10428036B2 (en) 2019-10-01
EP3380461B1 (en) 2019-07-24
HUE045534T2 (hu) 2019-12-30
TWI707847B (zh) 2020-10-21
EA201891215A1 (ru) 2018-10-31
TW201730167A (zh) 2017-09-01
PT3380461T (pt) 2019-09-24
US20180346432A1 (en) 2018-12-06
CN112979586A (zh) 2021-06-18
MY187663A (en) 2021-10-08
WO2017089516A1 (en) 2017-06-01
CN108290852B (zh) 2022-02-22
ES2746923T3 (es) 2020-03-09
KR20180087328A (ko) 2018-08-01
PL3380461T3 (pl) 2020-01-31
EP3380461A1 (en) 2018-10-03
EA035905B1 (ru) 2020-08-28
KR102655920B1 (ko) 2024-04-09

Similar Documents

Publication Publication Date Title
AR106815A1 (es) Proceso para la epoxidación de propeno
BR112015015460A2 (pt) processo de separação de etileno
AR102062A1 (es) Proceso para la separación mejorada de etilbenceno
EA201201013A1 (ru) Переработка углеводородного газа
BR112017011211A2 (pt) método e aparelho para produzir hidrocarbonetos
PE20151709A1 (es) Eliminacion de nitrogeno integrada en la produccion de gas licuado utilizando circuito de reinyeccion dedicado
MX2015011073A (es) Procesamiento de gas de hidrocarburo.
AR110464A1 (es) Proceso integrado para producir propeno y óxido de propeno a partir de propano
BR112019000496A2 (pt) processo para preparar óxido de propileno.
AR027376A1 (es) Procedimiento para la epoxidacion de olefinas
BR112017012234A2 (pt) processo para separação de glicóis
BR112017021550A2 (pt) processo para a separação de glicóis
CO6531420A2 (es) Métodos de licuefacción de gas natural y plantas de licuefacción de gas natural que utilizan corriente de gas múltiples y variables
SA518400500B1 (ar) عمليات لتحضير أوليجومرات
MX2015000147A (es) Procedimiento de produccion de gas natural tratado, de corte rico en hidrocarburos en c3+, y eventualmente de corriente rica en etano, e instalacion asociada.
EA201800353A1 (ru) Способ эксплуатации мультициклона для разделения мелких и очень мелких гранул, а также мультициклон
MX2017004849A (es) Un proceso para producir alcanos clorados sumamente puros.
AR100300A1 (es) Proceso para la producción de 1,4-butanodiol
MY183713A (en) Process for the production of dialkyl succinate
MX2016012851A (es) Un metodo para producir 1,1,2,3-tetracloropropeno con alto rendimiento.
BR112018006749A2 (pt) processo para a purificação de metil metacrilato.
MX2019012401A (es) Procedimiento para la oligomerizacion de olefinas con flujos de sustancias con contenido de olefina reducido.
MY189781A (en) Method for preparing polythiols
AR108033A1 (es) Proceso para producir etileno a partir de metano
MY185595A (en) Process for recovering aldehyde obtained by hydroformulation in two columns with increasing pressure

Legal Events

Date Code Title Description
FB Suspension of granting procedure