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1. 发明申请

US20130090496A1 PROCESS FOR PREPARING FORMIC ACID BY REACTING CARBON DIOXIDE WITH HYDROGEN 审中-公开
标题翻译：通过用氢气反应二氧化碳制备形式酸的方法
公开(公告)号：US20130090496A1
公开(公告)日：2013-04-11
申请号：US13646161
申请日：2012-10-05
申请人： Thomas Schaub , Oliver Bey , Anton Meier , Donata Maria Fries , Randolf Hugo
发明人： Thomas Schaub , Oliver Bey , Anton Meier , Donata Maria Fries , Randolf Hugo
IPC分类号： C07C51/15
CPC分类号： C07C51/02 , C07C51/41 , C07C53/06 , C07C53/02
摘要： The invention relates to a process for preparing formic acid by reacting carbon dioxide with hydrogen in a hydrogenation reactor in the presence of a catalyst comprising an element of group 8, 9 or 10 of the Periodic Table, a tertiary amine and a polar solvent to form formic acid-amine adducts which are subsequently dissociated thermally into formic acid and tertiary amine.
摘要翻译：本发明涉及在含有元素周期表第8,9或10族元素，叔胺和极性溶剂的催化剂存在下，在氢化反应器中使二氧化碳与氢反应制备甲酸的方法，以形成随后将甲酸 - 胺加合物热分解成甲酸和叔胺。

2. 发明授权

US08952156B2 Process for working up reaction outputs from the hydrogenation of EDDN or EDMN 有权
标题翻译：处理EDDN或EDMN的氢化反应产物的方法
公开(公告)号：US08952156B2
公开(公告)日：2015-02-10
申请号：US13598691
申请日：2012-08-30
申请人： Hermann Luyken , Sebastian Ahrens , Gordon Brasche , Jens Baldamus , Robert Baumann , Randolf Hugo , Stephanie Jaegli , Johann-Peter Melder , Jörg Pastre , Boris Buschhaus
发明人： Hermann Luyken , Sebastian Ahrens , Gordon Brasche , Jens Baldamus , Robert Baumann , Randolf Hugo , Stephanie Jaegli , Johann-Peter Melder , Jörg Pastre , Boris Buschhaus
IPC分类号： C07C213/02 , B01D3/36 , C07C209/48 , C07C209/86 , C07C253/00 , B01D3/14 , C08G59/50
CPC分类号： B01D3/36 , B01D3/143 , C07C209/48 , C07C209/86 , C07C253/00 , C08G59/502 , C07C211/14 , C07C255/09 , C07C255/25
摘要： A process is disclosed for separating the output from the reaction of EDDN or EDMN with hydrogen in the presence of THF, a catalyst, TETA or DETA, water, and optionally organic compounds having higher and lower boiling points than TETA or DETA. Hydrogen is removed, and the output is supplied to a distillation column DK1 in which an azeotrope, optionally comprising organic compounds with a boiling point lower than TETA or DETA, is removed from the top. A product comprising TETA or DETA is removed from the bottom and passed into a distillation column DK2, removing THF. A stream comprising TETA or DETA passes from the bottom of DK2. The DK1 azeotrope is condensed. Phase separation is induced by the addition of an organic solvent essentially immiscible with water, and the mixture is separated. The organic phase is recycled into DK1 and the water phase is discharged.
摘要翻译：公开了一种在THF，催化剂，TETA或DETA，水和具有比TETA或DETA具有更高和更低沸点的任何有机化合物存在下将EDDN或EDMN与氢气反应的输出分离出来的方法。除去氢气，并将输出物供给到蒸馏塔DK1，在该蒸馏塔DK1中，从顶部除去任选包含沸点低于TETA或DETA的有机化合物的共沸物。将包含TETA或DETA的产物从底部除去并进入蒸馏塔DK2中，除去THF。包含TETA或DETA的流从DK2的底部通过。 DK1共沸物浓缩。通过加入基本上与水不混溶的有机溶剂诱导相分离，并分离混合物。有机相再循环到DK1中，水相排出。

3. 发明授权

US08642828B2 Process for purifying a recycle stream from a 1,3-butadiene processing plant 有权
标题翻译：从1,3-丁二烯加工厂净化循环物流的方法
公开(公告)号：US08642828B2
公开(公告)日：2014-02-04
申请号：US13732668
申请日：2013-01-02
申请人： Bernd Heida , Randolf Hugo
发明人： Bernd Heida , Randolf Hugo
IPC分类号： C07C7/08
CPC分类号： C07C7/11 , C07C7/04 , C07C7/08 , Y02P20/124 , C07C11/167
摘要： Secondary streams in 1,3-butadiene processing plants still contain high amounts of valuable 1,3-butadiene. An energy-efficient process for purifying a recycle stream from a 1,3-butadiene processing plant is provided. The recycle stream is divided into two substreams: the first substream for prepurifying pure 1,3-butadiene feedstream by removing high boilers relative to 1,3-butadiene in a stripping column and the second substream in an extractive distillation plant.
摘要翻译： 1,3-丁二烯加工厂中的二次流仍含有大量有价值的1,3-丁二烯。提供了一种用于纯化来自1,3-丁二烯加工设备的再循环物流的节能方法。再循环流分为两个子流：第一子流，用于通过在汽提塔中除去高沸点相对于1,3-丁二烯和萃取蒸馏装置中的第二子流来纯化纯1,3-丁二烯进料流。

4. 发明申请

US20130197292A1 PROCESS FOR PURIFYING A RECYCLE STREAM FROM A 1,3-BUTADIENE PROCESSING PLANT 有权
标题翻译：从1,3-丁二烯加工厂净化回收液流程
公开(公告)号：US20130197292A1
公开(公告)日：2013-08-01
申请号：US13732668
申请日：2013-01-02
申请人： Bernd Heida , Randolf Hugo
发明人： Bernd Heida , Randolf Hugo
IPC分类号： C07C7/11 , C07C7/08
CPC分类号： C07C7/11 , C07C7/04 , C07C7/08 , Y02P20/124 , C07C11/167
摘要： Secondary streams in 1,3-butadiene processing plants still contain high amounts of valuable 1,3-butadiene. An energy-efficient process for purifying a recycle stream from a 1,3-butadiene processing plant is provided. The recycle stream is divided into two substreams: the first substream for prepurifying pure 1,3-butadiene feedstream by removing high boilers relative to 1,3-butadiene in a stripping column and the second substream in an extractive distillation plant.
摘要翻译： 1,3-丁二烯加工厂中的二次流仍含有大量有价值的1,3-丁二烯。提供了一种用于纯化来自1,3-丁二烯加工设备的再循环物流的节能方法。再循环流分为两个子流：第一子流，用于通过在汽提塔中除去高沸点相对于1,3-丁二烯和萃取蒸馏装置中的第二子流来纯化纯1,3-丁二烯进料流。

5. 发明申请

US20130085286A1 Unknown 审中-公开
标题翻译：未知
公开(公告)号：US20130085286A1
公开(公告)日：2013-04-04
申请号：US13600877
申请日：2012-08-31
申请人： Hermann Luyken , Sebastian Ahrens , Gordon Brasche , Jens Baldamus , Robert Baumann , Randolf Hugo , Stephanie Jaegli , Johann-Peter Melder , Jõrg Pastre , Boris Buschhaus
发明人： Hermann Luyken , Sebastian Ahrens , Gordon Brasche , Jens Baldamus , Robert Baumann , Randolf Hugo , Stephanie Jaegli , Johann-Peter Melder , Jõrg Pastre , Boris Buschhaus
IPC分类号： C07C209/48
CPC分类号： C07C209/48 , C07C211/14
摘要： A process for preparing amines of the formula (II) R1—NH—CH2—CH2—NH2 (II) in which R1 is hydrogen or radicals of the formula x is integers from zero to two, by reacting nitriles of the formula (I) R2—NH—CH2—CN (I) in which R2 is hydrogen or radicals of the formula and R3 is the NC— or H2N—CH2- radicals and x is integers from zero to two, with hydrogen in the presence of a catalyst in suspension mode or in a fixed bed, wherein the space velocity on the catalyst, based on the catalyst surface area, is 10−6 to 10−4 kg of nitrile of the formula (I) per m2 of catalyst surface area and hour, the catalyst surface area being determined by the BET method.
摘要翻译：通过使式（I）的腈反应，制备其中R1是氢的式（Ⅱ）的R1-NH-CH2-CH2-NH2（Ⅱ）或式x的基团为0至2的整数的方法， R2-NH-CH2-CN（Ⅰ），其中R2是氢或R3和R3的基团是NC-或H2N-CH2-基，x是从0到2的整数，在催化剂存在下用氢气悬浮模式或固定床，其中催化剂上的空速基于催化剂表面积为每平方米催化剂表面积和小时为10-6至10-4kg式（I）的腈，催化剂表面积由BET法测定。

6. 发明申请

US20130060002A1 PROCESS FOR WORKING UP REACTION OUTPUTS FROM THE HYDROGENATION OF EDDN OR EDMN 有权
标题翻译：从EDDN或EDMN加氢处理反应产物的过程
公开(公告)号：US20130060002A1
公开(公告)日：2013-03-07
申请号：US13598691
申请日：2012-08-30
申请人： Hermann Luyken , Sebastian Ahrens , Gordon Brasche , Jens Baldamus , Robert Baumann , Randolf Hugo , Stephanie Jaegli , Johann-Peter Melder , Jörg Pastre , Boris Buschhaus
发明人： Hermann Luyken , Sebastian Ahrens , Gordon Brasche , Jens Baldamus , Robert Baumann , Randolf Hugo , Stephanie Jaegli , Johann-Peter Melder , Jörg Pastre , Boris Buschhaus
IPC分类号： B01D3/36 , C08G69/00 , C08G59/02 , C07C209/48 , C07C231/00
CPC分类号： B01D3/36 , B01D3/143 , C07C209/48 , C07C209/86 , C07C253/00 , C08G59/502 , C07C211/14 , C07C255/09 , C07C255/25
摘要： A process is disclosed for separating the output from the reaction of EDDN or EDMN with hydrogen in the presence of THF, a catalyst, TETA or DETA, water, and optionally organic compounds having higher and lower boiling points than TETA or DETA. Hydrogen is removed, and the output is supplied to a distillation column DK1 in which an azeotrope, optionally comprising organic compounds with a boiling point lower than TETA or DETA, is removed from the top. A product comprising TETA or DETA is removed from the bottom and passed cinto a distillation column DK2, removing THF. A stream comprising TETA or DETA passes from the bottom of DK2. The DK1 azeotrope is condensed. Phase separation is induced by the addition of an organic solvent essentially immiscible with water, and the mixture is separated. The organic phase is recycled into DK1 and the water phase is discharged.
摘要翻译：公开了一种在THF，催化剂，TETA或DETA，水和具有比TETA或DETA具有更高和更低沸点的任何有机化合物的存在下将EDDN或EDMN与氢反应的输出分离出来的方法。除去氢气，并将输出物供给到蒸馏塔DK1，在该蒸馏塔DK1中，从顶部除去任选包含沸点低于TETA或DETA的有机化合物的共沸物。包含TETA或DETA的产品从底部除去并通过蒸馏塔DK2，除去THF。包含TETA或DETA的流从DK2的底部通过。 DK1共沸物浓缩。通过加入基本上与水不混溶的有机溶剂诱导相分离，并分离混合物。有机相再循环到DK1中，水相排出。

7. 发明申请

US20130053597A1 PROCESS FOR PREPARING EDDN, EDMN, TETA AND DETA 审中-公开
标题翻译：制备EDDN，EDMN，TETA和DETA的方法
公开(公告)号：US20130053597A1
公开(公告)日：2013-02-28
申请号：US13598698
申请日：2012-08-30
申请人： Hermann Luyken , Sebastian Ahrens , Gordon Brasche , Jens Baldamus , Robert Baumann , Randolf Hugo , Stephanie Jaegli , Johann-Peter Melder , Jörg Pastre , Boris Buschhaus
发明人： Hermann Luyken , Sebastian Ahrens , Gordon Brasche , Jens Baldamus , Robert Baumann , Randolf Hugo , Stephanie Jaegli , Johann-Peter Melder , Jörg Pastre , Boris Buschhaus
IPC分类号： C07C253/00 , C07C209/48
CPC分类号： C07C209/48 , C07C253/00 , C07C255/25 , C07C211/14
摘要： A process for preparing ethylenediaminediacetonitrile (EDDN) and/or ethylenediamine-monoacetonitrile (EDMN) by conversion of formaldehyde (FA), hydrogen cyanide (HCN) and ethylenediamine (EDA), which comprises using stabilizer-free HCN, or HCN which has been stabilized with an organic acid, in the process.
摘要翻译：通过甲醛（FA），氰化氢（HCN）和乙二胺（EDA）的转化制备乙二胺二乙腈（EDDN）和/或乙二胺一乙腈（EDMN）的方法，其包括使用稳定剂的HCN或稳定的HCN 在有机酸的过程中。

8. 发明申请

US20120101303A1 METHYL-SUBSTITUTED TETA COMPOUNDS 失效
标题翻译：甲基取代的四唑化合物
公开(公告)号：US20120101303A1
公开(公告)日：2012-04-26
申请号：US13378091
申请日：2010-06-14
申请人： Randolf Hugo , Johann-Peter Melder , Robert Baumann , Alfred Oftring , Boris Buschhaus , Gordon Brasche , Sebastian Ahrens , Peter Pfab
发明人： Randolf Hugo , Johann-Peter Melder , Robert Baumann , Alfred Oftring , Boris Buschhaus , Gordon Brasche , Sebastian Ahrens , Peter Pfab
IPC分类号： C07C209/62 , C07C209/90
CPC分类号： C07D207/327 , C07C211/14
摘要： The invention relates to a process for preparing triethylenetetramine substituted by at least one methyl group (Me-TETA or methyl-substituted TETA compounds). Me-TETA is prepared by hydrogenating biscyanomethylimidazolidine (BCMI) in the presence of a catalyst. The present invention further relates to methyl-substituted TETA compounds as such. The present invention further relates to the use of methyl-substituted TETA compounds as a reactant or intermediate in the production of, for example, coatings or adhesives.
摘要翻译：本发明涉及一种制备由至少一个甲基（Me-TETA或甲基取代的TETA化合物）取代的三亚乙基四胺的方法。通过在催化剂存在下氢化双氰基甲基咪唑烷（BCMI）制备Me-TETA。本发明还涉及甲基取代的TETA化合物。本发明还涉及甲基取代的TETA化合物在制备例如涂料或粘合剂中作为反应物或中间体的用途。

9. 发明申请

US20090158930A1 REFITTING PLANTS FOR ACID GAS REMOVAL 有权
标题翻译：用于酸性气体去除的植物
公开(公告)号：US20090158930A1
公开(公告)日：2009-06-25
申请号：US12278471
申请日：2007-02-14
申请人： Rupert Wagner , Randolf Hugo
发明人： Rupert Wagner , Randolf Hugo
IPC分类号： B01D53/14
CPC分类号： B01D53/1456 , B01D53/1406 , B01D53/1425 , C10L3/10 , C10L3/102
摘要： A method for removing acid gases from a fluid stream in which the fluid stream, in contact with an absorption medium in the form of an aqueous amine solution in an absorber, is passed through a first absorption zone and through a second absorption zone, the loaded absorption medium is passed into a first regeneration zone, a part of the resultant partially regenerated absorption medium is passed into the first absorption zone, the other part of the partially regenerated absorption medium is passed into a second regeneration zone, and a part of the resultant regenerated absorption medium is passed into the first absorption zone and the other part of the regenerated absorption medium is passed into the second absorption zone. The method can be carried out with few changes to apparatus of a hot pot plant, the energy requirement for the same performance being no higher than in the hot pot process.
摘要翻译：一种从流体物流中除去酸性气体的方法，其中与吸收剂中的胺水溶液形式的吸收介质接触的流体流通过第一吸收区并通过第二吸收区，吸收介质进入第一再生区，部分再生的部分吸收介质的一部分通入第一吸收区，部分再生吸收介质的另一部分通入第二再生区，一部分再生吸收介质通入第一吸收区，再生吸收介质的另一部分进入第二吸收区。该方法可以对火锅厂的设备进行少量改变，相同性能的能量要求不高于火锅过程。

10. 发明授权

US07368610B2 Preparation of xylylenediamine (XDA) 失效
标题翻译：苯二甲胺（XDA）的制备
公开(公告)号：US07368610B2
公开(公告)日：2008-05-06
申请号：US10569985
申请日：2004-09-04
申请人： Randolf Hugo , Sabine Jourdan , Kirsten Wenz , Thomas Preiss , Alexander Weck
发明人： Randolf Hugo , Sabine Jourdan , Kirsten Wenz , Thomas Preiss , Alexander Weck
IPC分类号： C07C209/48
CPC分类号： C07C209/48 , C07C211/27
摘要： A process for preparing xylylenediamine, comprising the steps of ammoxidizing xylene to phthalonitrile and hydrogenating the phthalonitrile, which comprises contacting the vaporous product of the ammoxidation stage directly with a liquid organic solvent or with molten phthalonitrile (quench),partly or fully removing components having a boiling point lower than phthalonitrile (low boilers) from the resulting quench solution or suspension or phthalonitrile melt and, after the low boiler removal and before the hydrogenation, removing products having a boiling point higher than phthalonitrile (high boilers).
摘要翻译：一种制备苯二甲胺的方法，包括以下步骤：将二甲苯与邻苯二甲腈氨化并氢化邻苯二甲腈，其包括将氨氧化阶段的蒸气产物直接与液体有机溶剂或熔融的邻苯二甲腈（骤冷）接触，部分或全部除去具有沸点低于邻苯二甲腈（低锅炉），从所得的淬火溶液或悬浮液或邻苯二甲腈熔体中，并且在低锅炉去除和氢化之前，除去沸点高于邻苯二甲腈（高锅炉）的产物。

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