AU2001287622A1 - Method for producing acrylic acid by the heterogeneously catalysed gas-phase oxidation of propane - Google Patents

Method for producing acrylic acid by the heterogeneously catalysed gas-phase oxidation of propane

Info

Publication number
AU2001287622A1
AU2001287622A1 AU2001287622A AU8762201A AU2001287622A1 AU 2001287622 A1 AU2001287622 A1 AU 2001287622A1 AU 2001287622 A AU2001287622 A AU 2001287622A AU 8762201 A AU8762201 A AU 8762201A AU 2001287622 A1 AU2001287622 A1 AU 2001287622A1
Authority
AU
Australia
Prior art keywords
propane
acrylic acid
phase oxidation
producing acrylic
heterogeneously catalysed
Prior art date
Legal status (The legal status 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 status listed.)
Abandoned
Application number
AU2001287622A
Inventor
Frieder Borgmeier
Gerhard Cox
Hartmut Hibst
Klaus Joachim Muller-Engel
Andreas Tenten
Signe Unverricht
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
Original Assignee
BASF SE
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
Priority claimed from DE2000134825 external-priority patent/DE10034825A1/en
Priority claimed from DE2000146672 external-priority patent/DE10046672A1/en
Priority claimed from DE10118814A external-priority patent/DE10118814A1/en
Priority claimed from DE2001119933 external-priority patent/DE10119933A1/en
Application filed by BASF SE filed Critical BASF SE
Publication of AU2001287622A1 publication Critical patent/AU2001287622A1/en
Abandoned legal-status Critical Current

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
    • 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
    • B01J23/16—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
    • B01J23/28—Molybdenum
    • 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
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/02—Sulfur, selenium or tellurium; Compounds thereof
    • B01J27/057—Selenium or tellurium; Compounds thereof
    • B01J27/0576—Tellurium; Compounds thereof
    • 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
    • B01J37/0232—Coating by pulverisation
    • 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
    • C07C51/215—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of saturated hydrocarbyl groups
    • 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

The invention relates to a method for producing acrylic acid by the heterogeneously catalysed gas-phase oxidation of propane on a multi-metal oxide mass, said mass containing the elements Mo, V, Te and/or Sb and having a specific X-ray diffractogram.
AU2001287622A 2000-07-18 2001-07-16 Method for producing acrylic acid by the heterogeneously catalysed gas-phase oxidation of propane Abandoned AU2001287622A1 (en)

Applications Claiming Priority (9)

Application Number Priority Date Filing Date Title
DE10034825 2000-07-18
DE2000134825 DE10034825A1 (en) 2000-07-18 2000-07-18 Production of acrolein or acrylic acid involves absorption of propane and propene from a gas mixture followed by desorption and oxidation, with no catalytic dehydrogenation of propane and no added oxygen
DE2000146672 DE10046672A1 (en) 2000-09-20 2000-09-20 Production of acrolein or acrylic acid involves absorption of propane and propene from a gas mixture followed by desorption and oxidation, with no catalytic dehydrogenation of propane and no added oxygen
DE10046672 2000-09-20
DE10118814A DE10118814A1 (en) 2001-04-17 2001-04-17 Production of acrolein or acrylic acid involves absorption of propane and propene from a gas mixture followed by desorption and oxidation, with no catalytic dehydrogenation of propane and no added oxygen
DE10118814 2001-04-17
DE2001119933 DE10119933A1 (en) 2001-04-23 2001-04-23 Production of acrolein or acrylic acid involves absorption of propane and propene from a gas mixture followed by desorption and oxidation, with no catalytic dehydrogenation of propane and no added oxygen
DE10119933 2001-04-23
PCT/EP2001/008178 WO2002006199A2 (en) 2000-07-18 2001-07-16 Method for producing acrylic acid by the heterogeneously catalysed gas-phase oxidation of propane

Publications (1)

Publication Number Publication Date
AU2001287622A1 true AU2001287622A1 (en) 2002-01-30

Family

ID=27437842

Family Applications (1)

Application Number Title Priority Date Filing Date
AU2001287622A Abandoned AU2001287622A1 (en) 2000-07-18 2001-07-16 Method for producing acrylic acid by the heterogeneously catalysed gas-phase oxidation of propane

Country Status (10)

Country Link
US (1) US6867328B2 (en)
EP (1) EP1301457B1 (en)
JP (1) JP2004504288A (en)
CN (1) CN1323998C (en)
AT (1) ATE390401T1 (en)
AU (1) AU2001287622A1 (en)
BR (1) BR0112557B1 (en)
CZ (1) CZ301370B6 (en)
DE (1) DE50113787D1 (en)
WO (1) WO2002006199A2 (en)

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DE10118814A1 (en) * 2001-04-17 2002-10-24 Basf Ag Production of acrolein or acrylic acid involves absorption of propane and propene from a gas mixture followed by desorption and oxidation, with no catalytic dehydrogenation of propane and no added oxygen
DE10051419A1 (en) * 2000-10-17 2002-04-18 Basf Ag Production of acrolein or acrylic acid involves absorption of propane and propene from a gas mixture followed by desorption and oxidation, with no catalytic dehydrogenation of propane and no added oxygen
JP4452011B2 (en) * 2002-02-26 2010-04-21 出光興産株式会社 Hydrocarbon reaction catalyst and reaction method using the same
DE10232482A1 (en) 2002-07-17 2004-01-29 Basf Ag Process for the safe operation of a continuous heterogeneously catalyzed gas phase partial oxidation of at least one organic compound
AU2003278286A1 (en) * 2002-09-10 2004-04-30 Arkema Method for producing acrylic acid from propane, in the presence of molecular oxygen
AU2003278285A1 (en) * 2002-09-10 2004-04-30 Arkema Method for producing acrylic acid from propane
DE10248584A1 (en) * 2002-10-17 2004-04-29 Basf Ag Heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid, used to produce polymers for adhesives, involves using active multimetal oxide material containing e.g. molybdenum and vanadium
US7238827B2 (en) * 2002-09-27 2007-07-03 Basf Aktiengesellschaft Preparation of at least one partial oxidation and/or ammoxidation product of propylene
US7038080B2 (en) * 2002-09-27 2006-05-02 Basf Aktiengesellschaft Heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid
US7038082B2 (en) * 2002-10-17 2006-05-02 Basf Aktiengesellschaft Preparation of a multimetal oxide material
JP4253176B2 (en) * 2002-11-12 2009-04-08 株式会社日本触媒 Catalyst for producing acrylic acid and method for producing 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
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DE10321398A1 (en) * 2003-05-12 2004-05-27 Basf Ag Multi-metal oxides, useful as catalysts for gas phase oxidation or ammoxidation, contain molybdenum and vanadium along with other elements and have an i-phase structure
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FR2880346B1 (en) * 2004-12-30 2007-02-23 Arkema Sa PROCESS FOR THE PREPARATION OF ACRYLIC ACID FROM PROPANE IN ABSENCE OF WATER VAPOR
FR2881136B1 (en) * 2005-01-21 2007-03-23 Arkema Sa PROCESS FOR THE PREPARATION OF ACRYLIC ACID COMPRISING A PARTIAL OXIDATION OF PROPANE PROPYLENE
KR101278795B1 (en) * 2005-11-03 2013-06-25 바스프 에스이 Method for carrying out in a stable manner a process for continuously producing acrolein or acrylic acid or the mixture thereof from propane
DE102006000996A1 (en) 2006-01-05 2007-07-12 Basf Ag Heterogeneously catalyzed gas phase partial oxidation of organic compound in fixed catalyst bed involves recovering quality of catalyst bed by replacing its portion, with a catalyst having activity lower than that of the replaced catalyst
EP1734030A1 (en) * 2006-01-18 2006-12-20 BASF Aktiengesellschaft Method for long term operation of a heterogeneously catalysed gas phase partial oxidation of an organic educt
US7538059B2 (en) * 2006-01-31 2009-05-26 Rohm And Haas Company Regeneration of mixed metal oxide catalysts
EP2913104B1 (en) 2006-03-20 2021-08-11 Asahi Kasei Kabushiki Kaisha Catalyst for oxidation or ammoxidation, and process for producing the same
US20080103326A1 (en) * 2006-10-31 2008-05-01 Bruce Irwin Rosen Lithium containing mixed metal oxide catalysts for ammoxidation of propane and isobutane
US20080103325A1 (en) * 2006-10-31 2008-05-01 Claus Lugmair Mixed metal oxide catalysts for the ammoxidation of propane and isobutane
WO2008058918A1 (en) * 2006-11-15 2008-05-22 Basf Se Process for conducting an exothermic heterogeneously catalyzed partial gas phase oxidation of an organic starting compound to an organic target compound
DE102007004961A1 (en) 2007-01-26 2008-07-31 Basf Se Preparing a catalyst molded body, useful e.g. to prepare catalyst for gas phase partial oxidation of an organic compound, comprises molding a precursor mixture to a desired geometry, using graphite, and thermally treating the molded body
US20080248947A1 (en) * 2007-04-03 2008-10-09 Zajac Gerry W Mixed metal oxide catalysts and catalytic processes for conversions of lower alkane hydrocarbons
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DE102008040093A1 (en) 2008-07-02 2008-12-18 Basf Se Producing a ring like oxidic mold, useful e.g. in partial gas phase oxidation of e.g. an organic compound, comprising mechanical packing of a powdery material which is brought into the fill space of a die made of a metal compound
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Also Published As

Publication number Publication date
US6867328B2 (en) 2005-03-15
US20030187298A1 (en) 2003-10-02
CN1323998C (en) 2007-07-04
CN1443151A (en) 2003-09-17
EP1301457B1 (en) 2008-03-26
WO2002006199A2 (en) 2002-01-24
JP2004504288A (en) 2004-02-12
BR0112557A (en) 2003-07-22
BR0112557B1 (en) 2012-01-24
CZ2003139A3 (en) 2003-06-18
DE50113787D1 (en) 2008-05-08
EP1301457A2 (en) 2003-04-16
CZ301370B6 (en) 2010-02-03
ATE390401T1 (en) 2008-04-15
WO2002006199A3 (en) 2002-05-23

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