METHOD FOR PRODUCING N-ETHYL-DIISOPROPYLAMINE
    1.
    发明申请
    METHOD FOR PRODUCING N-ETHYL-DIISOPROPYLAMINE 有权
    生产N-乙基 - 二异戊基胺的方法

    公开(公告)号:US20170008831A1

    公开(公告)日:2017-01-12

    申请号:US15119203

    申请日:2015-02-06

    Applicant: BASF SE

    Inventor: Hendrik DE WINNE

    Abstract: A process for preparing N-ethyldiisopropylamine by reacting acetaldehyde with diisopropylamine and hydrogen at elevated temperature and under pressure in the presence of a heterogeneous hydrogenation catalyst, the catalyst being a supported transition metal catalyst comprising Pd and/or Pt as catalytically active metal, wherein the diisopropylamine used has a purity of 58% to 94% by weight and impurities as follows:3% to 20% by weight of water, 3% to 20% by weight of isopropanol, 0% to 2% by weight of others.

    Abstract translation: 3重量%至20重量%的水,3重量%至20重量%的异丙醇,0重量%至2重量%的水。

    PROCESS FOR PRODUCING ANILINE
    2.
    发明公开

    公开(公告)号:US20240317673A1

    公开(公告)日:2024-09-26

    申请号:US18574795

    申请日:2022-06-29

    Applicant: BASF SE

    CPC classification number: C07C209/36

    Abstract: The invention relates to a process for producing aniline by catalytic hydrogenation of nitrobenzene comprising: (a) reacting hydrogen and nitrobenzene in the presence of a catalyst in a hydrogenation reactor, forming a crude reaction product; (b) working up the crude reaction product to obtain pure aniline, wherein the composition of the crude reaction product is analysed continuously or at regular time intervals before starting working-up in (b), for determining the proportion of by-products, wherein, in the event of an increase in the amount of by-products, measures are taken to prevent nitrobenzene from breaking through in the hydrogenation reactor.

    CATALYST SYSTEM FOR PRODUCING AROMATIC AMINES

    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

    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.

    PROCESS FOR OBTAINING PURE ANILINE
    5.
    发明申请
    PROCESS FOR OBTAINING PURE ANILINE 有权
    获得纯麻药的方法

    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

    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。

    PROCESS FOR PREPARATION OF CHLORINE FROM HYDROGEN CHLORIDE

    公开(公告)号:US20240228279A9

    公开(公告)日:2024-07-11

    申请号:US17769400

    申请日:2020-10-16

    Abstract: The invention relates to a process for preparation of chlorine from hydrogen chloride comprising circulating a liquid melt comprising copper ions Cun+ with n being a number in the range from 1 to 2, alkali cations and chloride ions Cl in a reactor system comprising three bubble lift reactors I, II and III, each comprising a reaction zone i, ii and iii respectively, wherein: ⋅(a) in the reaction zone i of the first bubble lift reactor I, a liquid melt comprising copper ions Cun+, alkali cations and chloride ions Cl— is contacted with oxygen at a temperature in the range from 395 to 405° C. so that the molar ratio Cun+:Cu+ in the liquid melt increases, obtaining a liquid melt having an increased molar ratio Cun+:Cu+ ⋅(b) the liquid melt obtained in (a) is circulated to the reaction zone ii in the second bubble lift reactor II, where the liquid melt is contacted with hydrogen chloride at a temperature in the range from 395 to 405° C. so that water is formed, obtaining a liquid melt being enriched in chloride anions (CI-) compared to the liquid melt obtained according to (a); ⋅(c) circulating the liquid melt obtained in (b) to the reaction zone iii in the third bubble lift reactor III, which is operated at a temperature in the range from 420 to 430° C. so that chlorine (Cl2) is formed, wherein Cl2 is removed from the reaction zone iii and the third bubble lift reactor III respectively in gaseous form, leaving a liquid melt depleted of Cl-compared to the liquid melt obtained according to (b). The invention further relates to a reactor system comprising three bubble lift reactors I, II and III.

    PROCESS FOR PREPARATION OF CHLORINE FROM HYDROGEN CHLORIDE

    公开(公告)号:US20240132350A1

    公开(公告)日:2024-04-25

    申请号:US17769400

    申请日:2020-10-15

    Abstract: The invention relates to a process for preparation of chlorine from hydrogen chloride comprising circulating a liquid melt comprising copper ions Cun+ with n being a number in the range from 1 to 2, alkali cations and chloride ions Cl in a reactor system comprising three bubble lift reactors I, II and III, each comprising a reaction zone i, ii and iii respectively, wherein: ⋅(a) in the reaction zone i of the first bubble lift reactor I, a liquid melt comprising copper ions Cun+, alkali cations and chloride ions Cl— is contacted with oxygen at a temperature in the range from 395 to 405° C. so that the molar ratio Cun+:Cu+ in the liquid melt increases, obtaining a liquid melt having an increased molar ratio Cun+:Cu+ ⋅(b) the liquid melt obtained in (a) is circulated to the reaction zone ii in the second bubble lift reactor II, where the liquid melt is contacted with hydrogen chloride at a temperature in the range from 395 to 405° C. so that water is formed, obtaining a liquid melt being enriched in chloride anions (CI-) compared to the liquid melt obtained according to (a); ⋅(c) circulating the liquid melt obtained in (b) to the reaction zone iii in the third bubble lift reactor III, which is operated at a temperature in the range from 420 to 430° C. so that chlorine (Cl2) is formed, wherein Cl2 is removed from the reaction zone iii and the third bubble lift reactor III respectively in gaseous form, leaving a liquid melt depleted of Cl-compared to the liquid melt obtained according to (b). The invention further relates to a reactor system comprising three bubble lift reactors I, II and III.

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