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公开(公告)号:US20220161237A1
公开(公告)日:2022-05-26
申请号:US17602887
申请日:2020-04-01
Applicant: BASF SE
Inventor: Veronika WLOKA , Dominik GARELLA , Michael REISER , Thomas HEIDEMANN , Hendrik DE WINNE
IPC: B01J23/72 , B01J27/224 , B01J37/02 , B01J37/08 , B01J8/24 , C07C209/36
Abstract: 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.
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公开(公告)号:US20180222830A1
公开(公告)日:2018-08-09
申请号:US15747809
申请日:2016-07-26
Applicant: BASF SE
Inventor: Alexander DUEFERT , Rolf PINKOS , Michael REISER , Philipp BRUEGGEMANN , Gerhard THEIS
IPC: C07C29/149
CPC classification number: C07C29/149 , B01J21/02 , B01J23/72 , C07C29/90 , C07C31/202 , C07C67/08 , C07C31/20
Abstract: Process for preparing monoethylene glycol (MEG) by metal-catalyzed reaction of a dialkyl oxalate of the formula I where R1 and R2 are each, independently of one another, methyl, ethyl, n-propyl or isopropyl, with hydrogen (H2), wherein the dialkyl oxalate (I) is used as melt or as a solution in a solvent, dialkyl oxalate (I) and H2 are used in a molar ratio of H2: dialkyl oxalate (I) in the range from 4.0 to 30 and the reaction is carried out continuously in a reactor at a cross-sectional loading of 10 m/s, a temperature in the range from 150 to 270° C., a pressure in the range from 150 to 390 bar and in the presence of a chromium-free heterogeneous catalyst comprising copper.
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公开(公告)号:US20210379565A1
公开(公告)日:2021-12-09
申请号:US17282710
申请日:2019-09-26
Applicant: BASF SE
Inventor: Carlos LIZANDARA PUEYO , Lukas WENGELER , Sabine HUBER , Stephan A. SCHUNK , Jaroslaw Michael MORMUL , Dominique MOULIN , Stephan Josef ASCHAUER , Chiara BOSCAGLI , Marcel SCHMITT , Matthias Georg SCHWAB , Michael REISER
Abstract: The present invention relates to a process for carrying out a chemical reaction in a chemical reactor, in which at least one starting material, which is an organic chemical compound comprising 1 to 80 carbon atoms, is converted into at least one reaction product in a fluid phase in the presence of a film comprising solid catalyst particles, which catalyze said chemical reaction, and comprising an organic polymer in fibrillated form, wherein the mass fraction of the sum of the starting material and of the reaction product based on the total mass of the fluid phase is in the range from 0.01 to 1.
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公开(公告)号:US20140107378A1
公开(公告)日:2014-04-17
申请号:US14045940
申请日:2013-10-04
Applicant: BASF SE
Inventor: Koenraad VANDEWALLE , Karen VERCRUYSSE , Leo DENISSEN , Filip DEBERDT , Hendrik DE WINNE , Bart VAN DE VOORDE , Michael REISER , Samuel NETO
IPC: C07C209/36
CPC classification number: C07C209/36 , C07C209/84 , C07C211/46
Abstract: A process for obtaining pure aniline contains catalytically hydrogenating nitrobenzene, to obtain a reaction mixture, separating the reaction mixture into a gas phase containing hydrogen and a liquid phase, liquid/liquid phase separating the liquid phase to obtain an aqueous phase and also crude aniline containing water as an organic phase, distillatively pre-purifying the crude aniline by removing the water via an overhead stream of a first distillation column to obtain a first bottom stream, feeding the first bottom stream as a feed stream to a pure column from which a pure aniline stream is taken off at the top and a second bottom stream containing high boilers is taken off, and passing the second bottom stream to incineration, by pumping the second bottom stream through heated pipelines and by adding methanol, ethanol, propanol, and/or acetone to the second bottom stream.
Abstract translation: 获得纯苯胺的方法含有催化氢化硝基苯,得到反应混合物,将反应混合物分离成含有氢和液相的气相,液/液相分离液相,得到含水相和粗苯胺 水作为有机相,通过经由第一蒸馏塔的塔顶物流除去水来蒸馏预纯化粗苯胺,以获得第一底部料流,将第一底部料流作为进料流进料至纯的塔,纯纯 将苯胺流从顶部取出,取出含有高锅炉的第二塔底物流,并将第二塔底物流通过加热的管道,并通过加入甲醇,乙醇,丙醇和/或 丙酮到第二底部流。
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