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41. 发明授权

EP1485337B1 VERFAHREN DER KONTINUIERLICHEN HETEROGEN KATALYSIERTEN PARTIELLEN DEHYDRIERUNG 有权
标题翻译：法连续多相催化部分脱氢
公开(公告)号：EP1485337B1
公开(公告)日：2015-12-02
申请号：EP03743835.5
申请日：2003-03-04
申请人： BASF SE
发明人： MACHHAMMER, Otto , SCHINDLER, Götz-Peter , HARTH, Klaus , ZEHNER, Peter
IPC分类号： C07C5/333 , C07C45/35 , B01J8/02 , B01J19/26 , B01J23/00 , B01J27/199 , C07C45/33
CPC分类号： B01J19/26 , B01J8/025 , B01J8/0278 , B01J23/002 , B01J27/199 , B01J2523/00 , C07C45/33 , C07C45/35 , Y02P20/582 , C07C47/22 , B01J2523/13 , B01J2523/15 , B01J2523/3706 , B01J2523/41 , B01J2523/43 , B01J2523/48 , B01J2523/828

42. 发明公开

EP2931415A1 VERFAHREN ZUR DURCHFÜHRUNG WÄRMEVERBRAUCHENDER PROZESSE 有权转让
标题翻译：方法实施热耗下降过程
公开(公告)号：EP2931415A1
公开(公告)日：2015-10-21
申请号：EP13814068.6
申请日：2013-12-12
申请人： BASF SE , Linde AG
发明人： MACHHAMMER, Otto , HORMUTH, Wolfgang Alois , SCHNEIDER, Christian , BODE, Andreas , GOEKE, Volker , MAASS, Hans-Juergen , KERN, Matthias , KLINGLER, Dirk , KÖNIG, Rene , BRÜGGEMANN, Philipp , BERNNAT, Jens , KOLIOS, Grigorios
IPC分类号： B01J19/00 , B01J8/00
摘要： The invention relates to a method for performing endothermic process, characterized in that the annual average total energy required for the endothermic process originates from at least two different energy sources. One of the energy sources is an electrical energy source, the power of which varies between 0 and 100% of the required total power, and three different energy modes individually can provide the total required power for the endothermic process: (i) exclusively electrical energy, (ii) a mixture of electrical energy and at least one additional non-energy source, or (iii) exclusively non-electrical energy. The transition time in which the change from one energy mode to another energy mode is completed 30 minutes at most.

43. 发明公开

EP2622300A2 VORRICHTUNG ZUR SPEICHERUNG VON HEISSEN, KORROSIV WIRKENDEN FLÜSSIGKEITEN SOWIE VERWENDUNG DER VORRICHTUNG 审中-公开
标题翻译：设备，用于存储HOT，腐蚀性液体和设备的使用
公开(公告)号：EP2622300A2
公开(公告)日：2013-08-07
申请号：EP11755318.0
申请日：2011-09-08
申请人： BASF SE
发明人： WORTMANN, Jürgen , SEELER, Fabian , MAJOR, Felix , SCHIERLE-ARNDT, Kerstin , MACHHAMMER, Otto , HUBER, Günther , MAURER, Stephan , GEYER, Karolin , LUTZ, Michael , GÄRTNER, Martin
IPC分类号： F28D20/00
CPC分类号： F28D20/0043 , C09K5/12 , F28D20/0039 , F28D2020/0047 , F28D2020/0069 , F28F19/00 , F28F19/04 , F28F2265/14 , F28F2270/00 , Y02E60/142
摘要： The invention relates to a device for receiving hot, corrosive liquids (7), comprising a chamber enclosed by a wall (21) for receiving the liquid (7), wherein the chamber comprises an interior insulation (19). The invention further relates to a use of the device for storing corrosive liquids for storing a heat storage medium comprising sulfur.

44. 发明公开

EP2567173A1 VORRICHTUNG UND VERFAHREN ZUR SPEICHERUNG VON WÄRME 有权
标题翻译：设备和方法储存热量
公开(公告)号：EP2567173A1
公开(公告)日：2013-03-13
申请号：EP11716585.2
申请日：2011-05-02
申请人： BASF SE
发明人： WORTMANN, Jürgen , SCHÄFER, Claus , LUTZ, Michael , SEELER, Fabian , GÄRTNER, Martin , MAJOR, Felix , SCHIERLE-ARNDT, Kerstin , MACHHAMMER, Otto , HUBER, Günther , MAURER, Stephan
IPC分类号： F28D20/00 , F24D11/00 , F24H7/00 , F24J2/34
CPC分类号： F28D20/0034 , F24S60/00 , F28D20/0039 , F28D2020/0091 , F28F2265/14 , Y02E10/40 , Y02E60/142
摘要： The invention relates to a device for storing heat, comprising a heat storage medium, which for storing heat takes up heat and for using the stored heat gives off heat, and a tank for receiving the heat storage medium, wherein the tank is closed by a gas-tight covering, and means for volume equalization are comprised, in order to equalize an increase in volume of the heat storage medium (3) as a result of an increase in temperature and a decrease in volume as a result of a decrease in temperature. The invention also relates to a method for storing heat, in which, for storing heat, heat is transferred to a heat storage medium or, for using heat, heat is removed from the heat storage medium and passed to the heat transfer medium, wherein the heat storage medium is held in a tank, which is closed by a gas-tight covering, wherein an expansion of the volume of the heat storage medium (3) is equalized by an increase in the volume of the tank (1), or by heat storage medium (3) flowing out of the tank (1) into a buffer tank (21; 63, 65), and a decrease in the volume of the heat storage medium (3) is equalized by a reduction in the volume of the tank (1) or by heat storage medium (3) flowing out of the buffer tank (21; 63, 65) into the tank (1).

45. 发明授权

EP1824803B1 VERFAHREN ZUR HERSTELLUNG VON PROPEN AUS PROPAN 有权
标题翻译：用于生产丙烯丙烷
公开(公告)号：EP1824803B1
公开(公告)日：2009-06-10
申请号：EP05817170.3
申请日：2005-12-08
申请人： BASF SE
发明人： CRONE, Sven , MACHHAMMER, Otto , SCHINDLER, Götz-Peter
IPC分类号： C07C5/327 , C07C7/11 , C07C11/06
CPC分类号： C07C5/3337 , C07C7/04 , C07C11/06
摘要： The invention relates to a method for producing propene from propane. Said method comprises the following steps: A) a feed gas flow a containing propane is provided; B) said feed gas flow a containing propane and an oxygen-containing gas flow are delivered into a dehydrogenation zone, and propane is subjected to non-oxidative catalytic, autothermal dehydrogenation so as to obtain propene in a product gas flow b containing propane, propene, methane, ethane, ethene, C4+ hydrocarbons, carbon monoxide, carbon dioxide, steam, and hydrogen; C) the product gas flow b is cooled and steam is separated by precipitation so as to obtain a product gas flow c that is stripped of steam; D) carbon dioxide is separated by gas washing so as to obtain a product gas flow d stripped of carbon dioxide; E) product gas flow d is cooled, and a liquid hydrocarbon flow e containing propane, propene, methane, ethene, and C4+ hydrocarbons is separated by precipitation so as to obtain a remaining gas flow e containing methane, hydrogen, and carbon monoxide; F) the liquid hydrocarbon flow e1 is delivered into a first distillation zone and is divided by distillation into a flow f1 containing propane, propene, and the C4+ hydrocarbons and a flow f2 containing ethane and ethene; G) flow f1 is delivered into a second distillation zone and is divided by distillation into a product flow g1 containing propene and a flow g2 containing propane and the C4+ hydrocarbons.

46. 发明公开

EP3194333A1 VERFAHREN ZUR ERZEUGUNG VON SYNTHESEGAS 有权
公开(公告)号：EP3194333A1
公开(公告)日：2017-07-26
申请号：EP15754117.8
申请日：2015-08-13
申请人： BASF SE
发明人： MAASS, Hans-Jürgen , MACHHAMMER, Otto , BODE, Andreas , KOLIOS, Grigorios
IPC分类号： C01B3/24 , C01B3/28 , C01B32/40 , C10J3/00 , C01B3/34
CPC分类号： C01B3/28 , C01B3/24 , C01B5/00 , C01B31/18 , C01B32/40 , C01B2203/0216 , C01B2203/0222 , C01B2203/0238 , C01B2203/0272 , C01B2203/0838 , C01B2203/1235 , Y02P20/13 , Y02P20/142
摘要： The invention relates to a method for generating syngas (5). Hydrocarbon (2) is thermally decomposed into hydrogen and carbon in a first reaction zone (Z1), and hydrogen produced in the process is conducted from the first reaction zone (Z1) to a second reaction zone (Z2) in order to react the hydrogen with carbon monoxide (4) in the second reaction zone so as to produce water and carbon monoxide. The invention is characterized in that the energy required for the thermal hydrocarbon decomposition in the first reaction zone (Z1) is supplied from the second reaction zone (Z2).
摘要翻译：本发明涉及用于产生合成气（5）的方法。烃（2）在第一反应区（Z1）中热分解成氢和碳，并且在该过程中产生的氢从第一反应区（Z1）传导到第二反应区（Z2）以使氢气与第二反应区中的一氧化碳（4）反应以产生水和一氧化碳。本发明的特征在于，第一反应区（Z1）中热烃分解所需的能量从第二反应区（Z2）供给。

47. 发明公开

EP2334625A1 VERFAHREN ZUR INTEGRIERTEN HERSTELLUNG VON ZELLSTOFF UND NIEDERMOLEKULARER WERTSTOFFE 审中-公开
标题翻译：法纸浆一体化生产和低分子量价值的材料
公开(公告)号：EP2334625A1
公开(公告)日：2011-06-22
申请号：EP09782673.9
申请日：2009-09-07
申请人： BASF SE
发明人： MACHHAMMER, Otto , HENKELMANN, Jochem , ROHDE, Wolfgang , EMMELUTH, Mario , GIESA, Sonja
IPC分类号： C07C37/54 , C07C47/58 , D21C11/00
CPC分类号： C07C37/54 , C07C41/18 , D21C11/0007 , Y02P30/20 , C07C39/04 , C07C39/08 , C07C43/23
摘要： The present invention relates to an integrated method for producing cellulose and at least one low-molecular-weight reusable material, in which a starting material containing lignocellulose is provided and subjected to a decomposition with a processing medium. A fraction enriched with cellulose and a fraction depleted of cellulose is then isolated from the decomposition material, the depleted fraction of cellulose being subjected to a treatment during which at least one low-molecular-weight reusable material is obtained.

48. 发明授权

EP1442000B1 VERFAHREN ZUR DEHYDRIERUNG VON C 2-C 30-ALKANEN 有权
标题翻译： PROCESS FOR脱水的C 2-C 30烷烃
公开(公告)号：EP1442000B1
公开(公告)日：2009-03-25
申请号：EP02801334.0
申请日：2002-10-14
申请人： BASF SE
发明人： WALSDORFF, Christian , SCHINDLER, Götz-Peter , MACHHAMMER, Otto , HARTH, Klaus
IPC分类号： C07C5/48 , C07C5/327
CPC分类号： C07C5/48 , C07C5/327 , C07C5/333 , C07C2521/02 , C07C2521/04 , C07C2521/06 , C07C2521/08 , C07C2521/10 , C07C2523/04 , C07C2523/10 , C07C2523/14 , C07C2523/42 , C07C2523/44 , C07C2523/74 , C07C15/46
摘要： The invention concerns a method for dehydrogenating C2-C30 alkanes, which consist in: (i) in a first process, dehydrogenating ethyl benzene into styrene, generating a hydrogen-containing gas stream, and (ii) in a second process, dehydrogenating one or several C2-C30 alkanes heterogeneously catalyzed in one or several reaction zones into corresponding olefins, a hydrogen-containing gas stream being mixed in at least one reaction zone with the dehydrogenation reaction gas stream. The invention is characterized in that at least part of the hydrogen-containing gaseous effluents derived from ethyl benzene dehydrogenation is added to the alkane dehydrogenation reaction gas mixture.

49. 发明授权

EP1558556B1 FLEXIBLES VERFAHREN ZUR GEMEINSAMEN HERSTELLUNG VON (I) AMEISENSÄURE,(II) EINER CARBONSÄURE MIT MINDESTENS ZWEI KOHLENSTOFFATOMEN UND/ODER DEREN DERIVATEN UND (III) EINES CARBONSÄUREANHYDRIDS 有权
标题翻译：灵活的方法为（I）甲酸，（II）炭酸与至少两个碳原子和/或其衍生物以及（III）的羧酸酐THE PRODUCTION
公开(公告)号：EP1558556B1
公开(公告)日：2009-03-18
申请号：EP03769425.4
申请日：2003-10-21
申请人： BASF SE
发明人： PASTRE, Jörg , EXNER, Kai Michael , STÜER, Wolfram , GEISSLER, Elke , MACHHAMMER, Otto
IPC分类号： C07C51/54 , C07C51/09 , C07C67/10 , C07C51/56 , C07C53/122 , C07C53/124 , C07C63/313 , C07C53/02 , C07C69/14 , C07C53/12
CPC分类号： C07C51/54 , C07C51/09 , C07C51/56 , Y02P20/582 , C07C53/02 , C07C57/04 , C07C53/124 , C07C53/122 , C07C63/313 , C07C53/12
摘要： Disclosed is a method for jointly producing (i) formic acid (III); (ii) a carboxylic acid comprising at least two carbon atoms (II) and/or the derivatives thereof; and (iii) a carboxylic acid anhydride (VII). According to said method, (a) a formic acid ester (I) is transesterified to formic acid (III) and the corresponding carboxylic acid ester (IV) by means of a carboxylic acid comprising at least two carbon atoms (II); (b) at least one portion of the carboxylic acid ester (IV) formed in step (a) is carbonylated in order to obtain the carboxylic acid anhydride (V); and (c) at least one portion of the carboxylic acid anhydride (V) formed in step (b) is further dehydrated by means of a carboxylic acid (VI) so as to form a carboxylic acid anhydride (VII) and the carboxylic acid (II).

50. 发明授权

EP1658258B1 VERFAHREN ZUR HERSTELLUNG VON MALEINS UREANHYDRID 有权
标题翻译：用于生产马来酸酐
公开(公告)号：EP1658258B1
公开(公告)日：2008-05-14
申请号：EP04740696.2
申请日：2004-07-06
申请人： BASF SE
发明人： DUDA, Mark , MACHHAMMER, Otto , WECK, Alexander
IPC分类号： C07C51/215
CPC分类号： C07C51/215 , C07C57/145
摘要： Disclosed is a method for producing maleic anhydride by means of heterogeneous catalytic gas phase oxidation of n-butane with gases containing oxygen on a catalyst comprising vanadium, phosphorus, and oxygen in a reactor unit at a temperature ranging between 350 and 500 °C, whereupon the obtained maleic anhydride is isolated while a gas flow is formed that contains unreacted n-butane and water, and at least some of the unreacted n-butane is recirculated to the reactor unit. According to the inventive method, an input flow having an n-butane concentration of 0.5 to 1.5 percent by volume and an oxygen concentration of 5 to 21 percent by volume is fed to the reactor unit while a pressure of 0.4 to 2 MPa abs is adjusted at the inlet of the reactor unit and 40 to 100 percent of the n-butane from the input flow are reacted per reactor cycle.

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