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    Process for obtaining maleic anhydride by distillation
    3.
    发明授权
    Process for obtaining maleic anhydride by distillation 有权
    通过蒸馏获得马来酸酐的方法

    公开(公告)号：US08461356B2

    公开(公告)日：2013-06-11

    申请号：US12532660

    申请日：2008-03-19

    申请人： Gunther Windecker ,  Gerd Kaibel ,  Michael Steiniger ,  Thilo Buntrock ,  Jens Weiguny ,  Dany Vanden Hautte ,  Thierry Lurquin

    发明人： Gunther Windecker ,  Gerd Kaibel ,  Michael Steiniger ,  Thilo Buntrock ,  Jens Weiguny ,  Dany Vanden Hautte ,  Thierry Lurquin

    IPC分类号： C07D307/36

    CPC分类号： B01D3/14 ,  B01D3/141 ,  C07C51/573 ,  C07C57/145

    摘要： What is described is a process for obtaining maleic anhydride by distillation from a solution of maleic anhydride in a high-boiling absorbent which has been obtained by gas phase oxidation of a hydrocarbon and at least partial absorption of the oxidation products into the absorbent, by i) introducing the solution into the side of a feed column with a rectifying section disposed above the feed point and a stripping section disposed below the feed point, ii) providing an upper combining column which communicates with the upper end of the rectifying section and a lower combining column which communicates with the lower end of the stripping section, iii) providing a draw column which communicates with the upper combining column and the lower combining column, iv) drawing maleic anhydride off as a side draw from the draw column, and drawing off compounds having a lower boiling point than maleic anhydride at the top of the upper combining column and the high-boiling absorbent at the bottom of the lower combining column. The maleic anhydride obtained as a side draw has a low content of acrylic acid and acetic acid.

    摘要翻译： 所描述的是通过蒸馏从马来酸酐在高沸点吸收剂中的溶液获得马来酸酐的方法，其通过烃的气相氧化和至少部分吸收氧化产物进入吸收剂中获得， 将溶液引入进料塔的侧面，其中设置在进料点上方的精馏部分和设置在进料点下方的汽提部分，ii）提供与精馏部分的上端连通的上部混合塔和下部 组合柱与汽提部分的下端连通，iii）提供与上部混合塔和下部混合塔连通的牵引柱，iv）将拉伸马来酸酐作为拉伸塔的牵引拉出，拉出 在上部混合塔的顶部具有比马来酸酐低的沸点的化合物和在底部o的高沸点吸收剂 f下组合列。 作为侧馏分获得的马来酸酐具有低含量的丙烯酸和乙酸。

    PROCESS FOR OBTAINING MALEIC ANHYDRIDE BY DISTILLATION
    4.
    发明申请
    PROCESS FOR OBTAINING MALEIC ANHYDRIDE BY DISTILLATION 有权
    通过蒸馏获得马来酸酐的方法

    公开(公告)号：US20100113805A1

    公开(公告)日：2010-05-06

    申请号：US12532660

    申请日：2008-03-19

    申请人： Gunther Windecker ,  Gerd Kaibel ,  Michael Steiniger ,  Thilo Buntrock ,  Jens Weiguny ,  Dany Vanden Hautte ,  Thierry Lurquin

    发明人： Gunther Windecker ,  Gerd Kaibel ,  Michael Steiniger ,  Thilo Buntrock ,  Jens Weiguny ,  Dany Vanden Hautte ,  Thierry Lurquin

    IPC分类号： C07D307/60

    CPC分类号： B01D3/14 ,  B01D3/141 ,  C07C51/573 ,  C07C57/145

    摘要： What is described is a process for obtaining maleic anhydride by distillation from a solution of maleic anhydride in a high-boiling absorbent which has been obtained by gas phase oxidation of a hydrocarbon and at least partial absorption of the oxidation products into the absorbent, by i) introducing the solution into the side of a feed column with a rectifying section disposed above the feed point and a stripping section disposed below the feed point, ii) providing an upper combining column which communicates with the upper end of the rectifying section and a lower combining column which communicates with the lower end of the stripping section, iii) providing a draw column which communicates with the upper combining column and the lower combining column, iv) drawing maleic anhydride off as a side draw from the draw column, and drawing off compounds having a lower boiling point than maleic anhydride at the top of the upper combining column and the high-boiling absorbent at the bottom of the lower combining column. The maleic anhydride obtained as a side draw has a low content of acrylic acid and acetic acid.

    摘要翻译： 所描述的是通过蒸馏从马来酸酐在高沸点吸收剂中的溶液获得马来酸酐的方法，其通过烃的气相氧化和至少部分吸收氧化产物进入吸收剂中获得， 将溶液引入进料塔的侧面，其中设置在进料点上方的精馏部分和设置在进料点下方的汽提部分，ii）提供与精馏部分的上端连通的上部混合塔和下部 组合柱与汽提部分的下端连通，iii）提供与上部混合塔和下部混合塔连通的牵引柱，iv）将拉伸马来酸酐作为拉伸塔的牵引拉出，拉出 在上部混合塔的顶部具有比马来酸酐低的沸点的化合物和在底部o的高沸点吸收剂 f下组合列。 作为侧馏分获得的马来酸酐具有低含量的丙烯酸和乙酸。

    Two-stage method for producing butane diol with intermediated separation of succinic anhydride
    9.
    发明申请
    Two-stage method for producing butane diol with intermediated separation of succinic anhydride 失效
    制备丁二酸酐中间分离丁二醇的两阶段方法

    公开(公告)号：US20060167323A1

    公开(公告)日：2006-07-27

    申请号：US10516922

    申请日：2003-06-11

    申请人： Michael Hesse ,  Stephan Schlitter ,  Holger Borchert ,  Markus Schubert ,  Markus Rosch ,  Nils Bottke ,  Rolf-Hartmuth Fischer ,  Alexander Weck ,  Gunther Windecker ,  Gunnar Heydrich

    发明人： Michael Hesse ,  Stephan Schlitter ,  Holger Borchert ,  Markus Schubert ,  Markus Rosch ,  Nils Bottke ,  Rolf-Hartmuth Fischer ,  Alexander Weck ,  Gunther Windecker ,  Gunnar Heydrich

    IPC分类号： C07C31/18

    CPC分类号： C07C29/149 ,  C07C31/207

    摘要： The present invention relates to a process for preparing optionally alkyl-substituted 1,4-butanediol by two-stage catalytic hydrogenation in the gas phase of C4-dicarboxylic acids and/or of derivatives thereof having the following steps: a) introducing a gas stream of a C4-dicarboxylic acid or of a derivative thereof at from 200 to 300° C. and from 2 to 60 bar into a first reactor and catalytically hydrogenating it in the gas phase to a product which contains mainly optionally alkyl-substituted γ-butyrolactone; b) removing succinic anhydride from the product obtained in step a), preferably to a residual level of from

    摘要翻译： 本发明涉及通过在具有下列物质的C 4 - 二羧酸和/或其衍生物的气相中通过两阶段催化氢化制备任选的烷基取代的1,4-丁二醇的方法 步骤：a）将200-300℃和2-60巴的C 4-14二羧酸或其衍生物的气流引入第一反应器，并将其催化氢化为 气相至主要含有烷基取代的γ-丁内酯的产物; b）从步骤a）中获得的产物中除去琥珀酸酐，优选残留量为约0.3至0.2重量％; c）将步骤b）中获得的产物流在150℃至240℃的温度和15至100巴的压力下引入第二反应器，并将其在气相中催化氢化为任选的烷基 - 取代的1,4-丁二醇; d）从中间体，副产物和任何未转化的反应物中除去所需的产物; e）任选地将未转化的中间体再循环到一个或两个氢化步骤中，所述氢化步骤各自使用催化剂，所述催化剂包含95重量％，优选5至95重量％，特别是10至80重量％的CuO ，和> = 5重量％，优选5至95重量％，特别是20至90重量％的氧化载体，并且所述第二反应器具有比所述第一反应器更高的压力。

    PROCESS FOR SEPARATING OFF FUMARIC ACID AND OTHER MINOR COMPONENTS DURING THE PRODUCTION OF MALEIC ANHYDRIDE
    10.
    发明申请
    PROCESS FOR SEPARATING OFF FUMARIC ACID AND OTHER MINOR COMPONENTS DURING THE PRODUCTION OF MALEIC ANHYDRIDE 有权
    在生产无水异味时分离灭酸和其他微量元素的方法

    公开(公告)号：US20110021789A1

    公开(公告)日：2011-01-27

    申请号：US12935894

    申请日：2009-03-23

    申请人： Gunther Windecker ,  Jens Weiguny ,  Alexander Weck ,  Ellen Dahlhoff ,  Wolf-Steffen Weissker ,  Jörg Heilek ,  Thomas Krug ,  Ralf Freyberger

    发明人： Gunther Windecker ,  Jens Weiguny ,  Alexander Weck ,  Ellen Dahlhoff ,  Wolf-Steffen Weissker ,  Jörg Heilek ,  Thomas Krug ,  Ralf Freyberger

    IPC分类号： C07D307/60

    CPC分类号： C07C51/573 ,  C07C57/145

    摘要： A process for decreasing fumaric acid deposits in the preparation of maleic anhydride by heterogeneously catalyzed oxidation of a hydrocarbon with molecular oxygen, in which the maleic anhydride is absorbed from the crude product mixture in an absorbent in an absorption column and desorbed again in a desorption column, the entirety or a portion of the absorbent depleted in maleic anhydride, for controlled precipitation of fumaric acid, being cooled and/or concentrated by evaporating a portion of the absorbent to such an extent that the difference between the concentration of fumaric acid in the recycle stream at the outlet of the desorption column under the conditions existing there and the equilibrium concentration of fumaric acid according to the solubility curve after the cooling and/or evaporation of a portion of the absorbent is greater than or equal to 250 ppm by weight, and the fumaric acid precipitated as a solid is removed completely or partly from the absorbent recycling system and the fumaric acid-depleted absorbent is recycled completely or partly to the absorption column.

    摘要翻译： 一种通过用分子氧异构催化氧化烃来减少马来酸酐制备中的富马酸沉积物的方法，其中马来酸酐在吸收塔中的吸收剂中从粗产物混合物中吸收并在解吸塔中再解吸 ，通过将一部分吸收剂蒸发而使富马酸的受控沉淀的全部或一部分吸收剂消耗马来酸酐，从而将富马酸的控制沉淀冷却和/或浓缩至使回收物中的富马酸浓度之间的差异 在存在的条件下在解吸塔的出口处的流，并且在一部分吸收剂的冷却和/或蒸发之后，根据溶解度曲线的富马酸的平衡浓度大于或等于250重量ppm， 作为固体沉淀的富马酸被完全或部分地从吸收剂循环系统中除去 em和富马酸贫乏的吸收剂被完全或部分地再循环到吸收塔。