BR0008825A - Processo para a oxidação catalìtica em fase gasosa de acroleìna para ácido acrìlico - Google Patents

Processo para a oxidação catalìtica em fase gasosa de acroleìna para ácido acrìlico

Info

Publication number
BR0008825A
BR0008825A BR0008825-0A BR0008825A BR0008825A BR 0008825 A BR0008825 A BR 0008825A BR 0008825 A BR0008825 A BR 0008825A BR 0008825 A BR0008825 A BR 0008825A
Authority
BR
Brazil
Prior art keywords
acrolein
acrylic acid
gas phase
catalytically oxidizing
reaction
Prior art date
Application number
BR0008825-0A
Other languages
English (en)
Other versions
BR0008825B1 (pt
Inventor
Signe Unverricht
Heiko Arnold
Andreas Tenten
Ulrich Hammon
Original Assignee
Basf 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 Basf Ag filed Critical Basf Ag
Publication of BR0008825A publication Critical patent/BR0008825A/pt
Publication of BR0008825B1 publication Critical patent/BR0008825B1/pt

Links

Classifications

    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0215—Coating
    • B01J37/0221—Coating of particles
    • B01J37/0223—Coating of particles by rotation
    • 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
    • B01J23/002—Mixed oxides other than spinels, e.g. perovskite
    • 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
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85—Chromium, molybdenum or tungsten
    • B01J23/88—Molybdenum
    • B01J23/887—Molybdenum containing in addition other metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/8877—Vanadium, tantalum, niobium or polonium
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/25—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
    • C07C51/252—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring of propene, butenes, acrolein or methacrolein
    • 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
    • B01J2523/00—Constitutive chemical elements of heterogeneous catalysts

Abstract

"PROCESSO PARA A OXIDAçãO CATALìTICA EM FASE GASOSA DE ACROLEìNA PARA áCIDO ACRìLICO". A invenção diz respeito a um método para a oxidação catalitica de fase gasosa de acroleína em ácido acrilico em que a mistura inicial do gás de reação, com uma carga de acroleína de <242> 150 NI/I.h, é alimentada por um catalisador de leito fixo que é acomodado em duas zonas de reação A, B dispostas em uma maneira espacialmente sucessiva, por meio da qual a temperatura da zona de reação B é mantida em uma temperatura mais elevada do que aquela da zona de reação A.
BRPI0008825-0A 1999-03-10 2000-02-28 processo para a oxidação catalìtica em fase gasosa de acroleìna para ácido acrìlico. BR0008825B1 (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19910508A DE19910508A1 (de) 1999-03-10 1999-03-10 Verfahren der katalytischen Gasphasenoxidation von Acrolein zu Acrylsäure
PCT/EP2000/001633 WO2000053559A1 (de) 1999-03-10 2000-02-28 Verfahren der katalytischen gasphasenoxidation von acrolein zu acrylsäure

Publications (2)

Publication Number Publication Date
BR0008825A true BR0008825A (pt) 2002-03-26
BR0008825B1 BR0008825B1 (pt) 2010-11-16

Family

ID=7900365

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0008825-0A BR0008825B1 (pt) 1999-03-10 2000-02-28 processo para a oxidação catalìtica em fase gasosa de acroleìna para ácido acrìlico.

Country Status (8)

Country Link
US (1) US6403829B1 (pt)
EP (1) EP1159246B1 (pt)
JP (2) JP5348814B2 (pt)
CN (1) CN1238325C (pt)
BR (1) BR0008825B1 (pt)
DE (2) DE19910508A1 (pt)
ES (1) ES2209832T3 (pt)
WO (1) WO2000053559A1 (pt)

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MY119958A (en) 1999-03-10 2005-08-30 Basf Ag Catalytic gas-phase oxidation of propene to acrylic acid
DE19910508A1 (de) * 1999-03-10 2000-09-21 Basf Ag Verfahren der katalytischen Gasphasenoxidation von Acrolein zu Acrylsäure
US6620968B1 (en) 1999-11-23 2003-09-16 Rohm And Haas Company High hydrocarbon space velocity process for preparing unsaturated aldehydes and acids
DE50111556D1 (de) 2000-06-14 2007-01-11 Basf Ag Verfahren zur herstellung von acrolein und/oder acrylsäure
DE10046957A1 (de) * 2000-09-21 2002-04-11 Basf Ag Verfahren zur Herstellung eines Multimetalloxid-Katalysators, Verfahren zur Herstellung ungesättigter Aldehyde und/oder Carbonsäuren und Bandcalziniervorrichtung
JP5134745B2 (ja) * 2001-09-19 2013-01-30 株式会社日本触媒 アクリル酸の製造方法
US7115776B2 (en) 2002-07-18 2006-10-03 Basf Aktiengesellschaft Heterogeneously catalyzed gas-phase partial oxidation of at least one organic compound
US7038080B2 (en) * 2002-09-27 2006-05-02 Basf Aktiengesellschaft Heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid
US6958414B2 (en) 2002-12-16 2005-10-25 Basf Aktiengesellschaft Preparation of at least one organic compound by heterogeneously catalyzed partial gas-phase oxidation
WO2004085365A2 (de) 2003-03-25 2004-10-07 Basf Aktiengesellschaft Verfahren der heterogen katalysierten partiellen gasphasenoxidation von acrolein zu acrylsäure
DE10313214A1 (de) 2003-03-25 2004-10-07 Basf Ag Verfahren der heterogen katalysierten partiellen Gasphasenoxidation von Acrolein zu Acrylsäure
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EP1611079B1 (de) * 2003-03-25 2007-05-23 BASF Aktiengesellschaft Verfahren der heterogen katalysierten partiellen gasphasenoxidation von acrolein zu acryls ure
US7294734B2 (en) * 2003-05-02 2007-11-13 Velocys, Inc. Process for converting a hydrocarbon to an oxygenate or a nitrile
US7220390B2 (en) 2003-05-16 2007-05-22 Velocys, Inc. Microchannel with internal fin support for catalyst or sorption medium
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TWI302147B (en) * 2003-09-01 2008-10-21 Lg Chemical Ltd Method of producing unsaturated aldehyde and unsaturated acid in fixed-bed catalytic partial oxidation reactor with enhanced heat control system
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JP5006507B2 (ja) * 2004-01-30 2012-08-22 株式会社日本触媒 アクリル酸の製造方法
JP2005329362A (ja) * 2004-05-21 2005-12-02 Mitsubishi Chemicals Corp 不飽和カルボン酸の製造用触媒の製造方法
US8431743B2 (en) * 2004-07-01 2013-04-30 Basf Aktiengesellschaft Preparation of acrylic acid by heterogeneously catalyzed partial gas phase oxidation of propylene
FR2884818B1 (fr) * 2005-04-25 2007-07-13 Arkema Sa Procede de preparation d'acide acrylique a partir de glycerol
DE102006000996A1 (de) 2006-01-05 2007-07-12 Basf Ag Verfahren der heterogen katalysierten Gasphasen-Partialoxidation wenigstens einer organischen Ausgangsverbindung
EP1734030A1 (de) * 2006-01-18 2006-12-20 BASF Aktiengesellschaft Verfahren zum Langzeitbetrieb einer heterogen katalysierten partiellen Gasphasenoxidation einer organischen Ausgangsverbindung
WO2008058918A1 (de) * 2006-11-15 2008-05-22 Basf Se Verfahren zum betreiben einer exothermen heterogen katalysierten partiellen gasphasenoxidation einer organischen ausgangsverbindung zu einer organischen zielverbindung
DE102007010422A1 (de) 2007-03-01 2008-09-04 Basf Se Verfahren zur Herstellung eines Katalysators bestehend aus einem Trägerkörper und einer auf der Oberfläche des Trägerkörpers aufgebrachten katalytisch aktiven Masse
JP2010083899A (ja) * 2009-12-29 2010-04-15 Nippon Shokubai Co Ltd アクリル酸の製造方法
DE102010048405A1 (de) 2010-10-15 2011-05-19 Basf Se Verfahren zum Langzeitbetrieb einer heterogen katalysierten partiellen Gasphasenoxidation von Proben zu Acrolein
DE102011076931A1 (de) 2011-06-03 2012-12-06 Basf Se Wässrige Lösung, enthaltend Acrylsäure und deren konjugierte Base
DE102012207811A1 (de) 2012-05-10 2012-07-12 Basf Se Verfahren der heterogen katalysierten Gasphasenpartialoxidation von (Meth)acrolein zu (Meth)acrylsäure
CN103071514B (zh) * 2013-01-29 2015-09-30 新兴能源科技有限公司 一种用于丙烯一步催化氧化制备丙烯酸催化剂的制备方法
DE102013202048A1 (de) 2013-02-07 2013-04-18 Basf Se Verfahren zur Herstellung einer katalytisch aktiven Masse, die ein Gemisch aus einem die Elemente Mo und V enthaltenden Multielementoxid und wenigstens einem Oxid des Molybdäns ist
WO2017184496A1 (en) * 2016-04-21 2017-10-26 Rohm And Haas Company Methods for using macroporous inert materials in monomer production
CN109305903A (zh) * 2017-07-28 2019-02-05 中国石油化工股份有限公司 用于生产丙烯酸的方法
CN109305910A (zh) * 2017-07-28 2019-02-05 中国石油化工股份有限公司 丙烯醛制丙烯酸的方法
CN110590536A (zh) * 2018-06-12 2019-12-20 中国石油化工股份有限公司 丙烯酸的合成方法
CN110590539A (zh) * 2018-06-12 2019-12-20 中国石油化工股份有限公司 丙烯酸生产方法
CN110642709A (zh) * 2018-06-27 2020-01-03 中国石油化工股份有限公司 丙烯醛氧化制备丙烯酸的方法
CN110639505A (zh) * 2018-06-27 2020-01-03 中国石油化工股份有限公司 丙烯酸的生产方法
CN110639537A (zh) * 2018-06-27 2020-01-03 中国石油化工股份有限公司 丙烯醛氧化合成丙烯酸的方法
CN110642710A (zh) * 2018-06-27 2020-01-03 中国石油化工股份有限公司 丙烯醛氧化合成丙烯酸催化剂
CN111068702A (zh) * 2018-10-18 2020-04-28 中国石油化工股份有限公司 用于制备丙烯酸的催化剂及其应用
CN111068700A (zh) * 2018-10-18 2020-04-28 中国石油化工股份有限公司 丙烯醛氧化合成丙烯酸的负载型催化剂及其应用
CN111068701A (zh) * 2018-10-18 2020-04-28 中国石油化工股份有限公司 用于生产丙烯酸的催化剂及其应用
CN110280257A (zh) * 2019-07-10 2019-09-27 兰州科润化工技术有限公司 一种丙烯酸催化剂及其制备方法
EP3770145A1 (en) 2019-07-24 2021-01-27 Basf Se A process for the continuous production of either acrolein or acrylic acid as the target product from propene
CN112547082B (zh) * 2019-09-25 2023-08-29 中国石油化工股份有限公司 用于丙烯醛氧化制丙烯酸的催化剂及其制备方法和应用
CN112705215B (zh) * 2019-10-25 2023-08-29 中国石油化工股份有限公司 核壳型催化剂及其制备方法与应用
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CN116490275A (zh) 2020-10-29 2023-07-25 巴斯夫欧洲公司 制备核壳催化剂的方法

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Also Published As

Publication number Publication date
DE50004069D1 (de) 2003-11-20
ES2209832T3 (es) 2004-07-01
EP1159246A1 (de) 2001-12-05
JP2011074083A (ja) 2011-04-14
CN1238325C (zh) 2006-01-25
DE19910508A1 (de) 2000-09-21
JP2002539103A (ja) 2002-11-19
EP1159246B1 (de) 2003-10-15
JP5348814B2 (ja) 2013-11-20
WO2000053559A1 (de) 2000-09-14
BR0008825B1 (pt) 2010-11-16
CN1343192A (zh) 2002-04-03
US6403829B1 (en) 2002-06-11

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Legal Events

Date Code Title Description
B07A Application suspended after technical examination (opinion) [chapter 7.1 patent gazette]
B09A Decision: intention to grant [chapter 9.1 patent gazette]
B16A Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]

Free format text: PRAZO DE VALIDADE: 10 (DEZ) ANOS CONTADOS A PARTIR DE 16/11/2010, OBSERVADAS AS CONDICOES LEGAIS.

B25D Requested change of name of applicant approved

Owner name: BASF SE (DE)

B21A Patent or certificate of addition expired [chapter 21.1 patent gazette]

Free format text: PATENTE EXTINTA EM 16.11.2020