CA1006178A - Process and apparatus inhibiting post reactions in the catalytic oxidation of propylene and/or acrolein to produce acrolein and/or acrylic acid - Google Patents

Process and apparatus inhibiting post reactions in the catalytic oxidation of propylene and/or acrolein to produce acrolein and/or acrylic acid

Info

Publication number
CA1006178A
CA1006178A CA178,161A CA178161A CA1006178A CA 1006178 A CA1006178 A CA 1006178A CA 178161 A CA178161 A CA 178161A CA 1006178 A CA1006178 A CA 1006178A
Authority
CA
Canada
Prior art keywords
acrolein
propylene
acrylic acid
catalytic oxidation
produce
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.)
Expired
Application number
CA178,161A
Other languages
English (en)
Other versions
CA178161S (en
Inventor
Klaus Gehrmann
Heinz Erpenbach
Winfried Lork
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.)
Hoechst AG
Original Assignee
Hoechst 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 Hoechst AG filed Critical Hoechst AG
Application granted granted Critical
Publication of CA1006178A publication Critical patent/CA1006178A/en
Expired 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
    • B01J8/067—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/27—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
    • C07C45/32—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen
    • C07C45/33—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties
    • C07C45/34—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds
    • C07C45/35—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds in propene or isobutene
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212—Plates; Jackets; Cylinders
CA178,161A 1972-08-07 1973-08-07 Process and apparatus inhibiting post reactions in the catalytic oxidation of propylene and/or acrolein to produce acrolein and/or acrylic acid Expired CA1006178A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2238851A DE2238851B2 (de) 1972-08-07 1972-08-07 Verfahren zur Herstellung von Acrolein und/oder Acrylsäure unter Vermeidung von Nachreaktionen bei der katalytischen Oxidation von Propylen und/oder Acrolein

Publications (1)

Publication Number Publication Date
CA1006178A true CA1006178A (en) 1977-03-01

Family

ID=5852924

Family Applications (1)

Application Number Title Priority Date Filing Date
CA178,161A Expired CA1006178A (en) 1972-08-07 1973-08-07 Process and apparatus inhibiting post reactions in the catalytic oxidation of propylene and/or acrolein to produce acrolein and/or acrylic acid

Country Status (10)

Country Link
US (1) US3876693A (de)
JP (1) JPS49132007A (de)
BE (1) BE803245A (de)
CA (1) CA1006178A (de)
DD (1) DD105200A5 (de)
DE (1) DE2238851B2 (de)
FR (1) FR2195613B1 (de)
GB (1) GB1405040A (de)
IT (1) IT990132B (de)
NL (1) NL7310290A (de)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2436818C3 (de) * 1974-07-31 1985-05-09 Basf Ag, 6700 Ludwigshafen Verfahren zur Herstellung von Acrylsäure durch Oxidation von Propylen mit Sauerstoff enthaltenden Gasen in zwei getrennten Oxidationsstufen
US4029636A (en) * 1974-11-12 1977-06-14 Celanese Corporation Method for reducing molybdenum trioxide content of gases issuing from reactors containing molybdenum-based catalysts
JPS5673041A (en) * 1979-11-19 1981-06-17 Mitsubishi Petrochem Co Ltd Preparation of acrylic acid
US4708853A (en) * 1983-11-03 1987-11-24 Calgon Carbon Corporation Mercury adsorbent carbon molecular sieves and process for removing mercury vapor from gas streams
DE4132684A1 (de) * 1991-10-01 1993-04-08 Basf Ag Verfahren zur katalytischen gasphasenoxidation von methacrolein zu methacrylsaeure
DE4445017A1 (de) * 1994-03-12 1995-09-14 Kupplungstechnik Gmbh Überlastkupplung
SG81982A1 (en) 1998-05-18 2001-07-24 Nippon Catalytic Chem Ind Method for production of acrolein and acrylic acid
JP4553440B2 (ja) * 2000-03-10 2010-09-29 三菱レイヨン株式会社 メタクリル酸の製造方法
ATE309856T1 (de) * 2002-02-27 2005-12-15 Verfahren zur herstellung von phosgen
JP2005298376A (ja) * 2004-04-08 2005-10-27 Mitsubishi Chemicals Corp アクロレイン及びアクリル酸の製造方法
JP4572573B2 (ja) * 2004-05-13 2010-11-04 三菱化学株式会社 （メタ）アクロレイン又は（メタ）アクリル酸の製造方法
JP2007302613A (ja) * 2006-05-12 2007-11-22 Asahi Kasei Chemicals Corp アルデヒドの分解を抑制する方法
WO2009125658A1 (ja) * 2008-04-09 2009-10-15 株式会社日本触媒 アクロレインおよび／またはアクリル酸の製造方法
JP5420556B2 (ja) * 2008-09-30 2014-02-19 株式会社日本触媒 アクロレインおよび／またはアクリル酸製造用の触媒および該触媒を用いたアクロレインおよび／またはアクリル酸の製造方法
EP2347823B1 (de) * 2008-09-30 2016-08-31 Nippon Shokubai Co., Ltd. Katalysator zur acrylsäureherstellung und verfahren zur acrylsäureherstellung mithilfe dieses katalysators
US9440903B2 (en) * 2012-09-24 2016-09-13 Arkema Inc. Shell and tube oxidation reactor with improved resistance to fouling
EP4043424A4 (de) * 2019-09-27 2023-11-15 Sumitomo Chemical Company, Limited Chemisches reaktionsverfahren und chemische reaktionsvorrichtung
EP3889127A1 (de) 2020-04-03 2021-10-06 Röhm GmbH Verbessertes sicheres verfahren zur tandem-c-4-oxidation zu methacrylsäure
EP3892367A1 (de) 2020-04-09 2021-10-13 Röhm GmbH Rohrbündelreaktor und verfahren für die herstellung von methacrylsäure durch die teiloxidierung von methacrolein
EP3945086B1 (de) 2020-07-30 2022-10-26 Röhm GmbH C-4 basiertes verfahren zur herstellung von mma unter rückführung und recyclierung von methacrolein

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3147084A (en) * 1962-03-08 1964-09-01 Shell Oil Co Tubular catalytic reactor with cooler
GB975686A (en) * 1962-05-25 1964-11-18 Distillers Co Yeast Ltd Improvements in or relating to the production of acrolein
DE1792681C3 (de) * 1964-07-18 1974-08-08 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler, 6000 Frankfurt Verfahren zur Herstellung eines Katalysators für die Oxidation von Olefinen. Ausscheidung aus: 1467026
DE1568925C3 (de) * 1966-08-09 1975-10-09 Hoechst Ag, 6000 Frankfurt Verfahren zur Abtrennung von Acrylsäure aus den Reaktionsgasen der Propylen- oder Acrolein-Oxydation
DE1910795A1 (de) * 1969-03-04 1970-09-17 Degussa Verfahren zur Vermeidung von Nachreaktionen bei der katalytischen Oxydation von Propylen oder Acrolein

Also Published As

Publication number Publication date
FR2195613B1 (de) 1978-12-01
DE2238851B2 (de) 1979-08-30
JPS49132007A (de) 1974-12-18
US3876693A (en) 1975-04-08
DE2238851A1 (de) 1974-02-14
BE803245A (fr) 1974-02-06
IT990132B (it) 1975-06-20
DD105200A5 (de) 1974-04-12
FR2195613A1 (de) 1974-03-08
GB1405040A (en) 1975-09-03
NL7310290A (de) 1974-02-11

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