Catalyst system for producing aromatic amines

US2022161237A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2022161237-A1
Application numberUS-202017602887-A
CountryUS
Kind codeA1
Filing dateApr 1, 2020
Priority dateApr 12, 2019
Publication dateMay 26, 2022
Grant date

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

Official abstract text for this publication.

The invention relates to a catalyst system suitable for hydrogenating aromatic nitro compounds (I) to form the corresponding aromatic amines (II), the catalyst system containing, as essential constituents: a component A selected from the group consisting of silicon carbide, corundum (alpha-Al2O3) and slightly porous to non-porous zirconium oxide (ZrO2); and a component B, containing B1—a carrier substance selected from the group consisting of silicon dioxide, gamma-, delta- or theta-aluminum oxide Al2O3, titanium dioxide, zirconium dioxide and graphite, B2—a metal or a plurality of metals selected from the group consisting of copper, nickel, palladium, platinum and cobalt, and optionally B3—an additional metal selected from the group consisting of at least one metal selected from main group I, main group II, main group IV and sub-groups II, V, VI and VIII of the periodic table of the elements, the proportion of component A being in the range of 5 to 60 wt %, in relation to the total weight of the catalyst system, and the aromatic nitro compounds (I) being those of the general formula R—(NO2)n, (I), and the aromatic amines (II) being those of the general formula R—(NH2)n, (II), and the moieties R and indices n in formulas (I) and (II) having the following meaning: R is a substituted or unsubstituted aromatic C6-C10 moiety and n is an integer from 1 to 5.

First claim

Opening claim text (preview).

1 .- 14 . (canceled) 15 . A catalyst system suitable for the hydrogenation of aromatic nitro compounds (I) to the corresponding aromatic amines (II), comprising as essential constituents a component A selected from the group consisting of silicon carbide, corundum (alpha-Al 2 O 3 ) and low-porosity to non-porous zirconium oxide (ZrO 2 ) and a component B comprising B1 a support material selected from the group consisting of silica, gamma-, delta- or theta-alumina Al 2 O 3 , titanium dioxide, zirconium dioxide, and graphite and B2 one or more metals selected from the group consisting of copper, nickel, palladium, platinum, and cobalt, and optionally B3 a further metal selected from the group consisting of at least one metal selected from main group I, main group II, main group IV, and subgroups II, V, VI, and VIII of the periodic table of the elements, wherein the proportion of component A is within a range from 5% to 60% by weight based on the total weight of the catalyst system and where the aromatic nitro compounds (I) are those of the general formula R—(NO 2 ) n (I), the aromatic amines (II) are those of the general formula R—(NH 2 ) n (II), and the radicals R and indices n in formulas (I) and (II) are defined as follows: R is a substituted or unsubstituted aromatic C 6 to C 10 radical and n is an integer from 1 to 5. 16 . The catalyst system according to claim 15 , wherein component A is a constituent of component B1. 17 . The catalyst system according to claim 15 , wherein component A comprises silicon carbide. 18 . The catalyst system according to claim 15 , wherein component A comprises exclusively silicon carbide. 19 . The catalyst system according to claim 15 , wherein component B2 comprises copper. 20 . The catalyst system according to claim 15 , wherein component B2 comprises exclusively copper. 21 . The catalyst system according to claim 15 , wherein component A comprises exclusively silicon carbide and component B2 comprises exclusively copper. 22 . The catalyst system according to claim 15 , wherein component A is a constituent of component B1, component A comprises exclusively silicon carbide, and component B2 comprises exclusively copper. 23 . A process for producing a catalyst system as defined in claim 15 , by i) producing a support material B1 comprising a component selected from the group consisting of silica, gamma-, delta- or theta-alumina Al 2 O 3 , titanium dioxide, zirconium dioxide, and graphite and contacting this support material with one or more metals B2 selected from the group consisting of copper, nickel, palladium, platinum, and cobalt, and optionally with B3 selected from the group consisting of at least one metal selected from main group I, main group II, main group IV, and subgroups II, V, VI, and VIII of the periodic table of the elements and combining this with a component A selected from the group consisting of silicon carbide, corundum (alpha-Al 2 O 3 ) and low-porosity to non-porous zirconium oxide (ZrO 2 ) or ii) producing a support material B1 comprising iia) a component selected from the group consisting of silica, gamma-, delta- or theta-alumina Al 2 O 3 , titanium dioxide, zirconium dioxide, and graphite and component A selected from the group consisting of silicon carbide, corundum (alpha-Al 2 O 3 ) and low-porosity to non-porous zirconium oxide (ZrO 2 ) and contacting this support material with one or more metals B2 selected from the group consisting of copper, nickel, palladium, platinum, and cobalt, and optionally with B3 selected from the group consisting of at least one metal selected from main group I, main group II, main group IV and subgroups II, V, VI, and VIII of the periodic table of the elements. 24 . The catalyst system obtainable by the process according to claim 23 . 25 . A method comprising utilizing the catalyst system as defined in claim 15 for producing aromatic amines (II) through hydrogenation of aromatic nitro compounds (I). 26 . A process for producing aromatic amines (II) through catalytic hydrogenation of the corresponding aromatic nitro compound (II), wherein a catalyst system as defined in claim 15 is used. 27 . The process according to claim 26 , wherein the process is executed in the fluidized bed. 28 . The process according to claim 26 , wherein the aromatic amine compound (II) is aniline and the corresponding aromatic nitro compound (I) is nitrobenzene.

Assignees

Inventors

Classifications

  • Aniline · CPC title

  • Pretreatment of the support · CPC title

  • by reduction of nitro groups bound to carbon atoms of six-membered aromatic rings {in presence of hydrogen-containing gases and a catalyst} · CPC title

  • Treating with free oxygen-containing gas · CPC title

  • B01J23/72Primary

    Copper · CPC title

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What does patent US2022161237A1 cover?
The invention relates to a catalyst system suitable for hydrogenating aromatic nitro compounds (I) to form the corresponding aromatic amines (II), the catalyst system containing, as essential constituents: a component A selected from the group consisting of silicon carbide, corundum (alpha-Al2O3) and slightly porous to non-porous zirconium oxide (ZrO2); and a component B, containing B1—a carrie…
Who is the assignee on this patent?
Basf Se
What technology area does this patent fall under?
Primary CPC classification B01J23/72. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Thu May 26 2022 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).