ES2647148T3 - Procedimiento para la producción de ésteres insaturados partiendo de aldehídos mediante esterificación oxidativa directa - Google Patents

Procedimiento para la producción de ésteres insaturados partiendo de aldehídos mediante esterificación oxidativa directa Download PDF

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Publication number
ES2647148T3
ES2647148T3 ES14809815.5T ES14809815T ES2647148T3 ES 2647148 T3 ES2647148 T3 ES 2647148T3 ES 14809815 T ES14809815 T ES 14809815T ES 2647148 T3 ES2647148 T3 ES 2647148T3
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Prior art keywords
procedure
production
reactor
liquid phase
value
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ES14809815.5T
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English (en)
Inventor
Steffen Krill
Alexander Lygin
Torsten Balduf
Rudolf Burghardt
Andreas Tepperis
Matthias Grömping
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Roehm GmbH Darmstadt
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Evonik Roehm GmbH
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00—Preparation of carboxylic acid esters
    • C07C67/39—Preparation of carboxylic acid esters by oxidation of groups which are precursors for the acid moiety of the ester
    • C07C67/42—Preparation of carboxylic acid esters by oxidation of groups which are precursors for the acid moiety of the ester by oxidation of secondary alcohols or ketones
    • 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
    • B01J23/02—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the alkali- or alkaline earth metals or beryllium
    • 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
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/48—Silver or gold
    • B01J23/52—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
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/892—Nickel and noble metals
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/19—Catalysts containing parts with different compositions
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
    • B01J35/45—Nanoparticles
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/48—Silver or gold
    • C07C2523/52—Gold
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00—Preparation of carboxylic acid esters
    • C07C67/39—Preparation of carboxylic acid esters by oxidation of groups which are precursors for the acid moiety of the ester
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/52—Esters of acyclic unsaturated carboxylic acids having the esterified carboxyl group bound to an acyclic carbon atom
    • C07C69/533—Monocarboxylic acid esters having only one carbon-to-carbon double bond
    • C07C69/54—Acrylic acid esters; Methacrylic acid esters
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/582—Recycling of unreacted starting or intermediate materials

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Dispersion Chemistry (AREA)

Abstract

Procedimiento para la producción de metacrilato de metilo a partir de metacroleína en una reacción de esterificación oxidativa continua con oxígeno y metanol, que se lleva a cabo en fase líquida a una presión de 2 a 100 bar con un catalizador heterogéneo, en cuyo caso se trata de nanopartículas que contienen oro soportadas con un tamaño de partícula menor que 20 nm, caracterizado por que la fase líquida se extrae continuamente del reactor, y el valor de pH tras la extracción se ajusta a un valor de pH entre 5 y 9 tras la extracción por medio de adición de disolución básica fuera del reactor, y por que la fase líquida extraída se devuelve al reactor con un valor de pH entre 5 y 9 en al menos un 50 %.

Description

imagen1
imagen2
imagen3
imagen4
imagen5
imagen6
(A)
Reactor
(B)
Cambiador de calor
(C)
Separador de fases
(D)
Depósito para el ajuste del valor de pH 5 (E) Cambiador de calor alternativo o adicional
(1)
Conducto de alimentación de la mezcla gaseosa que contiene O2 (10)
(2)
Conducto de alimentación de la mezcla constituida por metacroleína y metanol (12)
(3)
Conducto para el mezclado de la fase líquida (12) y la fase gaseosa (10) para introducción en el reactor (A)
(4)
Conducto para la transferencia de la fase líquida extraída del reactor (A) al separador de fases (C) a través 10 del cambiador de calor (B)
(5)
Conducto de descarga de gas de escape (13) del separador de fases (C)
(6)
Conducto para la fase líquida del separador de fases (C) al depósito (D)
(7)
Conducto de alimentación de la disolución básica (11) para el ajuste del valor de pH en el depósito (D)
(8)
Recirculación de la fase líquida de valor de pH ajustado del depósito (D) de vuelta al reactor (A) a través del 15 conducto (3) y bajo enriquecimiento (1) con oxígeno de la mezcla gaseosa (10)
(9) Descarga de la corriente de producto que contiene MMA (14) para la elaboración subsiguiente
8

Claims (1)

  1. imagen1
ES14809815.5T 2013-12-20 2014-12-05 Procedimiento para la producción de ésteres insaturados partiendo de aldehídos mediante esterificación oxidativa directa Active ES2647148T3 (es)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP13198863.6A EP2886528A1 (de) 2013-12-20 2013-12-20 Verfahren zur Herstellung von ungesättigten Estern ausgehend von Aldehyden durch Direkte Oxidative Veresterung
EP13198863 2013-12-20
PCT/EP2014/076682 WO2015091018A1 (de) 2013-12-20 2014-12-05 Verfahren zur herstellung von ungesättigten estern ausgehend von aldehyden durch direkte oxidative veresterung

Publications (1)

Publication Number Publication Date
ES2647148T3 true ES2647148T3 (es) 2017-12-19

Family

ID=49880519

Family Applications (1)

Application Number Title Priority Date Filing Date
ES14809815.5T Active ES2647148T3 (es) 2013-12-20 2014-12-05 Procedimiento para la producción de ésteres insaturados partiendo de aldehídos mediante esterificación oxidativa directa

Country Status (13)

Country Link
US (1) US9617199B2 (es)
EP (2) EP2886528A1 (es)
JP (1) JP6479017B2 (es)
KR (1) KR102336765B1 (es)
CN (1) CN105722816B (es)
BR (1) BR112016014331A2 (es)
ES (1) ES2647148T3 (es)
MY (1) MY171922A (es)
RU (1) RU2643369C2 (es)
SA (1) SA516371327B1 (es)
SG (1) SG11201602583PA (es)
TW (1) TWI651298B (es)
WO (1) WO2015091018A1 (es)

Families Citing this family (45)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3170558A1 (de) * 2015-11-19 2017-05-24 Evonik Röhm GmbH Gold-basierten katalysator für die oxidative veresterung von aldehyden zu carbonsäureestern
EP3235560A1 (de) 2016-04-22 2017-10-25 Evonik Röhm GmbH Verfahren zur durchführung einer heterogen-katalysierten reaktion
EP3621943B1 (de) * 2017-05-09 2023-01-18 Röhm GmbH Verfahren für oxidative veresterung von aldehyden zu carbonsäureester
WO2019022884A1 (en) * 2017-07-28 2019-01-31 Rohm And Haas Company PROCESS FOR THE PRODUCTION OF METHYL METHACRYLATE BY OXIDATIVE ESTERIZATION USING A HETEROGENEOUS CATALYST
SG11202000744UA (en) * 2017-07-28 2020-02-27 Rohm & Haas A method for production of methyl methacrylate by oxidative esterification using a heterogeneous catalyst
SG11202000692VA (en) 2017-07-28 2020-02-27 Rohm & Haas A method for production of methyl methacrylate by oxidative esterification using a heterogeneous catalyst
KR102639233B1 (ko) * 2017-07-28 2024-02-21 다우 글로벌 테크놀로지스 엘엘씨 불균일 촉매를 사용하여 산화적 에스터화에 의해 메틸 메타크릴레이트를 제조하는 방법
BR112020001575B1 (pt) 2017-07-28 2023-03-14 Rohm And Haas Company Catalisador heterogêneo, e, leito de catalisador
CA3071244A1 (en) 2017-07-28 2019-01-31 Rohm And Haas Company A method for production of methyl methacrylate by oxidative esterification using a heterogeneous catalyst
EP3658535B1 (en) * 2017-07-28 2024-03-20 Rohm and Haas Company A method for production of methyl methacrylate by oxidative esterification using a heterogeneous catalyst
WO2019022889A1 (en) * 2017-07-28 2019-01-31 Dow Global Technologies Llc PROCESS FOR THE PRODUCTION OF METHYL METHACRYLATE BY OXIDATIVE ESTERIZATION USING A HETEROGENEOUS CATALYST
EP3658532A1 (en) * 2017-07-28 2020-06-03 Rohm and Haas Company A method for production of methyl methacrylate by oxidative esterification using a heterogeneous catalyst
BR112020001710A2 (pt) * 2017-07-28 2020-07-21 Rohm And Haas Company método para preparar metil metacrilato de metacroleína e metanol.
EP3450422A1 (de) 2017-08-29 2019-03-06 Evonik Röhm GmbH Verfahren zur herstellung optischer formmassen
CA3075083A1 (en) * 2017-09-19 2019-03-28 Dow Global Technologies Llc Method for production of methyl methacrylate by oxidative esterification using a heterogeneous catalyst
EP3456704A1 (de) 2017-09-19 2019-03-20 Evonik Röhm GmbH Katalysator für die oxidative veresterung von aldehyden zu carbonsäureestern
KR102739478B1 (ko) * 2018-01-10 2024-12-09 다우 글로벌 테크놀로지스 엘엘씨 산화적 에스터화에 의한 메틸 메타크릴레이트 생산용 불균일 촉매
EP3587390A1 (de) * 2018-06-26 2020-01-01 Röhm GmbH Verfahren zur herstellung von mma in hohen ausbeuten
KR102755859B1 (ko) 2018-06-28 2025-01-15 다우 글로벌 테크놀로지스 엘엘씨 불균일 촉매
KR20210022620A (ko) * 2018-06-28 2021-03-03 다우 글로벌 테크놀로지스 엘엘씨 불균일 촉매
EP3608305A1 (en) 2018-08-10 2020-02-12 Röhm GmbH Process for producing methacrylic acid or methacrylic acid esters
CN111233667A (zh) * 2018-11-29 2020-06-05 中国科学院大连化学物理研究所 一种改进制备甲基丙烯酸甲酯的方法
CN109331839B (zh) * 2018-11-29 2021-11-02 中国科学院大连化学物理研究所 一种生产甲基丙烯酸甲酯的催化剂的制备方法及其应用
CN109772345B (zh) * 2019-01-05 2022-03-04 山东理工大学 醛氧化酯化合成酯的镍催化剂的制备及其与离子液体共催化体系的应用
EP3786148A1 (de) 2019-08-28 2021-03-03 Röhm GmbH Vereinfachte aufarbeitung des reaktoraustrags einer oxidativen veresterung
EP3798202A1 (de) 2019-09-25 2021-03-31 Röhm GmbH Verfahren zur aufreinigung von methylmethacrylat von leichtsiedenden komponenten
EP3798206A1 (de) 2019-09-25 2021-03-31 Röhm GmbH Verfahren zur herstellung von alkylmethacrylaten mit verbesserter wasser- und säureführung
CN112823876B (zh) * 2019-11-20 2022-07-12 万华化学集团股份有限公司 一种通过直接氧化酯化制备mma的催化剂及其制备方法
EP3945088A1 (de) * 2020-07-30 2022-02-02 Röhm GmbH Vorgehen zur minimierung des aktivitätsverlusts bei im kreislaufbetrieb ausgeführten reaktionsschritten
JP2024520502A (ja) 2021-05-28 2024-05-24 レーム・ゲーエムベーハー アルキル（メタ）アクリレートを製造するための反応器および方法
JP2024520503A (ja) 2021-05-28 2024-05-24 レーム・ゲーエムベーハー アルキルメタクリレートを製造するための反応器および方法
RU2761822C1 (ru) * 2021-06-16 2021-12-13 федеральное государственное бюджетное образовательное учреждение высшего образования «Санкт-Петербургский горный университет» СПОСОБ ПОЛУЧЕНИЯ КАРКАСНЫХ СТРУКТУР НА ОСНОВЕ SiO2-Al2O3
WO2023025676A1 (de) * 2021-08-23 2023-03-02 Röhm Gmbh Aufbereitung eines katalysators für die oxidative veresterung von methacrolein zu methylmethacrylat zur verlängerung der lebensdauer
MX2024004083A (es) 2021-10-08 2024-04-18 Rohm & Haas Proceso para la produccion de metacrilato de metilo.
EP4412983A1 (en) 2021-10-08 2024-08-14 Rohm and Haas Company Process for alkyl methacrylate production
KR20240089249A (ko) 2021-10-08 2024-06-20 롬 앤드 하스 캄파니 에탄올로부터 메틸 메타크릴레이트를 생산하는 방법
EP4412985A1 (en) 2021-10-08 2024-08-14 Rohm and Haas Company Process for an oxidative esterification reactor
MX2024004087A (es) 2021-10-08 2024-04-18 Dow Global Technologies Llc Proceso para una baja formacion de subproducto de un reactor de esterificacion oxidativa con adicion de base.
MX2024004086A (es) 2021-10-08 2024-04-18 Rohm & Haas Proceso para la produccion de metacrilato de metilo.
CN118076578A (zh) 2021-10-08 2024-05-24 罗门哈斯公司 用于由氧化酯化反应器以副产物较低的方式形成甲基丙烯酸甲酯的方法
KR20240108464A (ko) 2021-11-12 2024-07-09 룀 게엠베하 메타크롤레인의 직접 산화성 에스테르화에서의 성가신 2차 생성물의 제거 방법
WO2024123526A1 (en) 2022-12-08 2024-06-13 Dow Global Technologies Llc Process for preparing alkyl methacrylates
EP4605366A1 (en) 2022-12-08 2025-08-27 Dow Global Technologies LLC Process for preparing alkyl methacrylates
WO2024123529A1 (en) * 2022-12-08 2024-06-13 Dow Global Technologies Llc Supported gold-np and nickel oxide catalyst and method for producing methyl methacrylate using such
EP4611935A1 (en) * 2022-12-08 2025-09-10 Dow Global Technologies LLC Process for making supported gold np catalyst for the production of methyl methacrylate by oxidation esterification, catalyst obtained thereby and process of said oe

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55151533A (en) * 1979-05-17 1980-11-26 Asahi Chem Ind Co Ltd Preparation of carboxylic acid ester
JP3268022B2 (ja) 1992-09-03 2002-03-25 旭化成株式会社 カルボン酸エステルの製造方法
DE69633753T2 (de) 1995-07-18 2005-12-22 Asahi Kasei Chemicals Corp. Verfahren zur Herstellung von Carbonsäureestern
SG71815A1 (en) 1997-07-08 2000-04-18 Asahi Chemical Ind Method of producing methyl methacrylate
US7326806B2 (en) 2001-06-04 2008-02-05 Nippon Shokubai Co., Ltd. Catalyst for the preparation of carboxylic esters and method for producing carboxylic esters
JP4860065B2 (ja) * 2001-08-03 2012-01-25 旭化成ケミカルズ株式会社 反応器への重合禁止剤と鉛の供給方法
JP4860064B2 (ja) 2001-08-03 2012-01-25 旭化成ケミカルズ株式会社 カルボン酸エステル合成反応器内のｐＨ制御方法
US7012039B2 (en) 2001-12-21 2006-03-14 Asahi Kasei Chemicals Corporation Oxide catalyst composition
JP2007296429A (ja) * 2006-04-27 2007-11-15 Asahi Kasei Chemicals Corp 耐磨耗性、反応性に優れた金属担持粒子
CN1931824A (zh) 2006-09-18 2007-03-21 鲁东大学 一种由不饱和醛连续制备不饱和羧酸酯的方法及催化剂
WO2009022544A1 (ja) * 2007-08-13 2009-02-19 Asahi Kasei Chemicals Corporation カルボン酸エステル製造用触媒、その製造方法、並びにカルボン酸エステルの製造方法
EP2210664A4 (en) 2007-10-26 2011-12-21 Asahi Kasei Chemicals Corp COMPOSITE-LOADED ARTICLE, METHOD FOR PRODUCING THE COMPOSITE-RELATED ARTICLE, AND METHOD FOR PRODUCING THE COMPOUND FROM THE COMPOSITE-RELATED ARTICLE AS A CHEMICAL SYNTHETIC CATALYST
CN101332427A (zh) * 2008-08-06 2008-12-31 厦门大学 一种用于制备甲基丙烯酸甲酯的固体催化剂
JP5336235B2 (ja) * 2009-03-19 2013-11-06 旭化成ケミカルズ株式会社 貴金属担持物及びそれを触媒として用いるカルボン酸エステルの製造方法
JP5336234B2 (ja) * 2009-03-19 2013-11-06 旭化成ケミカルズ株式会社 複合粒子担持物及びその製造方法並びにカルボン酸エステルの製造方法
WO2012035637A1 (ja) * 2010-09-16 2012-03-22 旭化成ケミカルズ株式会社 シリカ系材料及びその製造方法、並びに貴金属担持物及びそれを触媒として用いるカルボン酸類の製造方法
CN103721744A (zh) * 2013-12-27 2014-04-16 天津大学 用于一步氧化酯化生产甲基丙烯酸甲酯的疏水催化剂及制备方法

Also Published As

Publication number Publication date
US9617199B2 (en) 2017-04-11
JP2017504607A (ja) 2017-02-09
SG11201602583PA (en) 2016-05-30
EP3083549B1 (de) 2017-09-20
MY171922A (en) 2019-11-07
WO2015091018A1 (de) 2015-06-25
KR102336765B1 (ko) 2021-12-07
RU2016129243A (ru) 2018-01-25
RU2643369C2 (ru) 2018-02-01
KR20160102498A (ko) 2016-08-30
JP6479017B2 (ja) 2019-03-06
EP3083549A1 (de) 2016-10-26
EP2886528A1 (de) 2015-06-24
US20160251301A1 (en) 2016-09-01
TW201536738A (zh) 2015-10-01
CN105722816B (zh) 2018-01-23
CN105722816A (zh) 2016-06-29
BR112016014331A2 (pt) 2017-10-31
TWI651298B (zh) 2019-02-21
SA516371327B1 (ar) 2019-01-16

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