公开(公告)号：US07030052B2

公开(公告)日：2006-04-18

申请号：US10449772

申请日：2003-06-02

Applicant: Guido Stochniol ,  Bernd Jaeger ,  Thomas Haas ,  Norbert Finke ,  Werner Burkhardt ,  Juergen Grunert

Inventor： Guido Stochniol ,  Bernd Jaeger ,  Thomas Haas ,  Norbert Finke ,  Werner Burkhardt ,  Juergen Grunert

IPC: B01J21/18 ,  B01J23/00

CPC classification number: C07C209/72 ,  B01J23/462 ,  B01J35/10 ,  B01J35/108 ,  C07C2601/14 ,  C07C211/36

Abstract: The invention relates to a process for hydrogenating an aromatic amine that has at least one amino group bound to an aromatic nucleus with hydrogen in the presence of a supported catalyst that contains at least ruthenium as active metal. The catalyst support has a BET surface area in the range from greater than 30 m2/g to less than 70 m2/g and more than 50% of the pore volume of the catalyst support is formed by macropores having a pore diameter of greater than 50 nm and less than 50% are mesopores having a pore diameter of 2 to 50 nm.

Abstract translation: 本发明涉及一种在至少含有钌作为活性金属的载体催化剂存在下氢化芳族胺的方法，所述芳族胺具有至少一个与芳族核结合的氨基。 催化剂载体的BET表面积大于30m 2 / g至小于70m 2 / g，超过孔体积的50％ 的催化剂载体由孔径大于50nm且小于50％的大孔形成为具有2至50nm孔径的介孔。

公开(公告)号：US07029230B2

公开(公告)日：2006-04-18

申请号：US10497480

申请日：2002-10-14

Applicant: Bernd Jaeger

Inventor： Bernd Jaeger

IPC: F04D5/00

CPC classification number: F04D29/188

Abstract: An impeller for a delivery pump in which profiled section (14) comprising webs (15) is located on the outer periphery of an impeller (4) for a feed pump (2) that is configured as a side channel pump. The webs (15) are arranged at an ascending incline, viewed in the rotational direction of the impeller (4) from the designated pressure side to the designated intake side. This permits flow losses between the radial external region of the impeller (4) and the housing parts (6, 7) of the feed pump (2) to be maintained at a particularly low level.

Abstract translation: 一种用于输送泵的叶轮，其中包括腹板（15）的成型部分（14）位于用作用于侧通道泵的进料泵（2）的叶轮（4）的外周上。 从叶轮（4）的旋转方向从指定的压力侧到指定的进气侧，腹板（15）布置成上升的倾斜。 这允许叶轮（4）的径向外部区域和进料泵（2）的壳体部件（6,7）之间的流动损失保持在特别低的水平。

公开(公告)号：US06441255B1

公开(公告)日：2002-08-27

申请号：US09406137

申请日：1999-09-27

Applicant: Thomas Haas ,  Bernd Jaeger ,  Jörg Sauer ,  Rudolf Vanheertum

Inventor： Thomas Haas ,  Bernd Jaeger ,  Jörg Sauer ,  Rudolf Vanheertum

IPC: C07C29141

CPC classification number: C07C29/145 ,  C07B2200/07 ,  C07C29/141 ,  C07C31/205 ,  C07C31/10 ,  C07C31/26

Abstract: Carrier-bound ruthenium catalysts are used to produce alcohols by the catalytic hydrogenation of aldehydes and ketones. The problem of deactivation of the catalyst is solved by the use of a ruthenium catalyst on an oxide carrier of the series TiO2, SiO2, ZrO2, MgO, mixed oxides thereof and silicates thereof. In particular, Ru on TiO2 or SiO2 results in a long service life of the catalyst.

Abstract translation: 载体结合的钌催化剂用于通过醛和酮的催化氢化制备醇。 催化剂失活的问题是通过使用钌催化剂在TiO 2，SiO 2，ZrO 2，MgO，其混合氧化物和其硅酸盐的氧化物载体上来解决的。 特别地，在TiO 2或SiO 2上的Ru导致催化剂的使用寿命长。

公开(公告)号：US06180831B2

公开(公告)日：2001-01-30

申请号：US09438376

申请日：1999-11-12

Applicant: Robert Weber ,  Wilhelm Keim ,  Bernd Jaeger ,  Thomas Haas ,  Rudolf Vanheertum

Inventor： Robert Weber ,  Wilhelm Keim ,  Bernd Jaeger ,  Thomas Haas ,  Rudolf Vanheertum

IPC: C07C4549

CPC classification number: C07C45/58 ,  C07C47/19

Abstract: &bgr;-Hydroxyaldehydes are produced by a method in which 1,2-oxiranes are reacted with carbon monoxide and hydrogen in the presence of transitional metal compounds which are modified with phosphorus-oxygen ligands or nitrogen-oxygen ligands and which act as a catalyst.

Abstract translation: 通过在氧磷配体或氮 - 氧配体改性并用作催化剂的过渡金属化合物存在下，使1,2-环氧乙烷与一氧化碳和氢气反应的方法制备β-羟基醛。

公开(公告)号：US20180134676A1

公开(公告)日：2018-05-17

申请号：US15570167

申请日：2016-04-19

Applicant: Robert JAHN ,  Wolfgang WÖLL ,  Bernd JAEGER ,  Matthias PASCALY

Inventor： Robert JAHN ,  Wolfgang WÖLL ,  Bernd JAEGER ,  Matthias PASCALY

IPC: C07D301/12 ,  C07D301/36 ,  C07D303/04 ,  B01J29/89 ,  B01D3/34 ,  B01D3/42 ,  B01D19/04

CPC classification number: C07D301/12 ,  B01D3/34 ,  B01D3/4294 ,  B01D19/0409 ,  B01J29/89 ,  C07D301/36 ,  C07D303/04

Abstract: In a process for the epoxidation of propene, comprising the steps: reacting propene with hydrogen peroxide in the presence of a titanium silicalite catalyst and a methanol solvent; separating non-reacted propene and propene oxide from the resulting reaction mixture to provide a solvent mixture comprising methanol and water in a combined amount of at least 90% by weight; and feeding this solvent mixture as a feed stream to a continuously operated methanol distillation column at a feed point in the middle section of said column to provide an overhead product comprising at least 90% by weight methanol and a bottoms product comprising at least 90% by weight water; the addition of a liquid defoamer, having a solubility in the feed stream of less than 10 mg/kg at 25° C. and a surface tension at the liquid air interface of less than 22 mN/m at 20° C., at or above the feed point in an amount exceeding the solubility of the liquid defoamer in the feed stream suppresses foam formation in the methanol distillation column.

公开(公告)号：US07507862B2

公开(公告)日：2009-03-24

申请号：US11284932

申请日：2005-11-23

Applicant: Guido Stochniol ,  Bernd Jaeger ,  Thomas Haas ,  Norbert Finke ,  Werner Burkhardt ,  Juergen Grunert

Inventor： Guido Stochniol ,  Bernd Jaeger ,  Thomas Haas ,  Norbert Finke ,  Werner Burkhardt ,  Juergen Grunert

IPC: C07C209/00

CPC classification number: C07C209/72 ,  B01J23/462 ,  B01J35/10 ,  B01J35/108 ,  C07C2601/14 ,  C07C211/36

Abstract: The invention relates to a process for hydrogenating an aromatic amine that has at least one amino group bound to an aromatic nucleus with hydrogen in the presence of a supported catalyst that contains at least ruthenium as active metal. The catalyst support has a BET surface area in the range from greater than 30 m2/g to less than 70 m2/g and more than 50% of the pore volume of the catalyst support is formed by macropores having a pore diameter of greater than 50 nm and less than 50% are mesopores having a pore diameter of 2 to 50 nm.

Abstract translation: 本发明涉及一种在至少含有钌作为活性金属的载体催化剂存在下氢化芳族胺的方法，所述芳族胺具有至少一个与芳族核结合的氨基。 催化剂载体的BET表面积在大于30m 2 / g至小于70m 2 / g的范围内，并且催化剂载体的孔体积的大于50％由孔径大于50的大孔形成 nm且小于50％是孔径为2〜50nm的中孔。

公开(公告)号：US07473069B2

公开(公告)日：2009-01-06

申请号：US10935647

申请日：2004-09-07

Applicant: Johannes Deichmann ,  Eberhard Geissel ,  Bernd Jaeger

Inventor： Johannes Deichmann ,  Eberhard Geissel ,  Bernd Jaeger

IPC: F04D5/00

CPC classification number: F04D5/005

Abstract: In a fuel pump (6) designed as a side channel pump, in each case two conveying chambers (20-23) one surrounding the other concentrically are arranged on two impellers (9, 10). The conveying chambers (20, 21) of one impeller (9) are connected to an inlet duct (25), while the conveying chambers (22, 23) of the other impeller (10) are connected to an outlet duct (26). A connection (24) of the conveying chambers (20-23) is arranged in a partition (17) keeping the impellers (9, 10) at a distance from one another. As a result, the fuel pump (6) has an especially high volume flow, along with a very high conveying pressure.

Abstract translation: 在设计为侧通道泵的燃料泵（6）中，在两个叶轮（9,10）中，在每种情况下，两个围绕另一个同心的传送室（20-23）布置。 一个叶轮（9）的输送室（20,21）连接到入口管道（25），而另一个叶轮（10）的输送室（22,23）连接到出口管道（26）。 传送室（20-23）的连接（24）布置在保持叶轮（9,10）彼此距离的隔板（17）中。 结果，燃料泵（6）具有特别高的体积流量以及非常高的输送压力。

公开(公告)号：US07195748B2

公开(公告)日：2007-03-27

申请号：US10476202

申请日：2003-03-04

Applicant: Bernd Jaeger ,  Thomas Haas ,  Jürgen Glenneberg ,  Jürgen Grunert

Inventor： Bernd Jaeger ,  Thomas Haas ,  Jürgen Glenneberg ,  Jürgen Grunert

IPC: C01B15/023

CPC classification number: C01B15/023 ,  B01J23/96 ,  B01J35/023 ,  Y02P20/584

Abstract: The invention relates to a process for the production of hydrogen peroxide by the anthraquinone process, comprising a hydrogenation stage, an oxidation stage and an extraction stage. According to the invention, catalytic hydrogenation of anthraquinone derivatives dissolved in a working solution is carried out in the presence of added molecular oxygen. Per mol hydrogen, 0.1 to 10 mmol oxygen is preferably introduced into the hydrogenation stage with the hydrogenating gas, in mixture with an inert gas and/or dissolved and/or dispersed in the working solution. This increases the residence time of the catalyst.

Abstract translation: 本发明涉及一种通过蒽醌法生产过氧化氢的方法，包括氢化阶段，氧化阶段和萃取阶段。 根据本发明，溶解在工作溶液中的蒽醌衍生物的催化氢化在加入的分子氧的存在下进行。 每摩尔氢气，优选将0.1至10mmol氧气与氢化气体一起引入氢化阶段，与惰性气体混合和/或溶解和/或分散在工作溶液中。 这增加了催化剂的停留时间。

公开(公告)号：US07091384B2

公开(公告)日：2006-08-15

申请号：US10516319

申请日：2003-06-25

Applicant: Bernd Jaeger ,  Thomas Haas ,  Guido Stochniol ,  Christian Lettmann ,  Willi Hofen ,  Klaus Stadtmueller ,  Joerg Lotz

Inventor： Bernd Jaeger ,  Thomas Haas ,  Guido Stochniol ,  Christian Lettmann ,  Willi Hofen ,  Klaus Stadtmueller ,  Joerg Lotz

IPC: C07C209/72

CPC classification number: C07C209/72 ,  C07C211/36

Abstract: The invention relates to a process for increasing the selectivity of the hydrogenation of 4,4′-diaminodiphenylmethane (4,4′-MDA) to diaminodicyclohexylmethane (4,4′-HMDA) by catalytic hydrogenation of a mixture containing 4,4′-MDA as the main component and its mono-N-methyl derivative as a secondary component. According to the invention, the hydrogenation is terminated before a conversion of 4,4′-MDA to 4,4′-HMDA of 99% is achieved. Under these conditions, a substantially smaller proportion of the N-methyl-4,4′-MDA is hydrogenated to N-methyl-4,4-HMDA.

Abstract translation: 本发明涉及通过催化氢化含有4,4'-二氨基二苯基甲烷（4,4'-MDA）的混合物的方法提高4,4'-二氨基二苯基甲烷（4,4'-MDA） MDA为主要成分，其单-N-甲基衍生物为次要成分。 根据本发明，在将4,4'-MDA转化为99％的4,4'-HMDA之前终止氢化。 在这些条件下，将大部分比例的N-甲基-4,4'-MDA氢化成N-甲基-4,4-HMDA。

公开(公告)号：US20060079717A1

公开(公告)日：2006-04-13

申请号：US11284932

申请日：2005-11-23

Applicant: Guido Stochniol ,  Bernd Jaeger ,  Thomas Haas ,  Norbert Finke ,  Werner Burkhardt ,  Juergen Grunert

Inventor： Guido Stochniol ,  Bernd Jaeger ,  Thomas Haas ,  Norbert Finke ,  Werner Burkhardt ,  Juergen Grunert

IPC: C07C209/72

CPC classification number: C07C209/72 ,  B01J23/462 ,  B01J35/10 ,  B01J35/108 ,  C07C2601/14 ,  C07C211/36

Abstract: The invention relates to a process for hydrogenating an aromatic amine that has at least one amino group bound to an aromatic nucleus with hydrogen in the presence of a supported catalyst that contains at least ruthenium as active metal. The catalyst support has a BET surface area in the range from greater than 30 m2/g to less than 70 m2/g and more than 50% of the pore volume of the catalyst support is formed by macropores having a pore diameter of greater than 50 nm and less than 50% are mesopores having a pore diameter of 2 to 50 nm.