公开(公告)号：WO2011138355A3

公开(公告)日：2012-01-12

申请号：PCT/EP2011057098

申请日：2011-05-04

Applicant: BASF SE ,  PROCHAZKA ROMAN ,  BITTERLICH STEFAN ,  DEUERLEIN STEPHAN ,  MACHHAMMER OTTO ,  KLINGLER DIRK ,  PANTOUFLAS EMMANOUIL

Inventor： PROCHAZKA ROMAN ,  BITTERLICH STEFAN ,  DEUERLEIN STEPHAN ,  MACHHAMMER OTTO ,  KLINGLER DIRK ,  PANTOUFLAS EMMANOUIL

IPC: D21C3/02 ,  C10G1/00 ,  C10G1/02 ,  C10G1/06

CPC classification number: D21C3/02 ,  C10G1/02 ,  C10G2300/1014 ,  C10G2300/4081 ,  D21C11/0007 ,  D21C11/125 ,  Y02P30/20

Abstract: The present invention relates to an integrated method for producing pulp and at least one organic liquid or liquefiable valuable material, in which a) a lignocellulosic starting material is prepared and subjected to disruption with an aqueous-alkaline treatment medium, b) from the disrupted material a cellulose-enriched fraction and a cellulose-depleted black liquor are isolated, c) the black liquor is subjected to a treatment with at least one organic liquid or liquefiable valuable material and at least one exhaust gas stream being obtained, d) at least one of the exhaust gas streams of step c) is recirculated to the method for producing pulp and utilized.

Abstract translation: 本发明涉及一种用于生产纸浆和至少一种有机液体或可液化的可回收材料制成的集成方法，其中a）一个木素纤维素，其包括起始材料并进行消化用含水碱性处理介质，b）从所述消化的纤维素材料富集 馏分和纤维素贫化的黑液分离，c）将黑液的处理，以获得至少一种有机液体或的值可液化材料，和至少一个废气流，D）从步骤c的方法中的废气流）用于生产纸浆的至少一个引回和利用 ，

公开(公告)号：WO2013004398A3

公开(公告)日：2013-04-11

申请号：PCT/EP2012002877

申请日：2012-07-05

Applicant: LINDE AG ,  MAABETA HANS-JUERGEN ,  GOEKE VOLKER ,  MACHHAMMER OTTO ,  GUZMANN MARCUS ,  SCHNEIDER CHRISTIAN ,  HORMUTH WOLFGANG ,  BODE ANDREAS ,  KLINGLER DIRK ,  KERN MATTHIAS ,  KOLIOS GRIGORIOS ,  BASF SE

Inventor： MAABETA HANS-JUERGEN ,  GOEKE VOLKER ,  MACHHAMMER OTTO ,  GUZMANN MARCUS ,  SCHNEIDER CHRISTIAN ,  HORMUTH WOLFGANG ,  BODE ANDREAS ,  KLINGLER DIRK ,  KERN MATTHIAS ,  KOLIOS GRIGORIOS

IPC: C01B3/28 ,  C01B3/30 ,  C01B31/02

CPC classification number: C01B3/24 ,  C01B3/28 ,  C01B3/30 ,  C01B32/05 ,  C01B2203/0272 ,  C01B2203/04 ,  C01B2203/0425 ,  C01B2203/0485 ,  C01B2203/049 ,  C01B2203/06 ,  C01B2203/0805 ,  C01B2203/0811 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/0866 ,  C01B2203/1235 ,  C01B2203/1258 ,  C10B57/005 ,  Y02P20/128

Abstract: The invention relates to a method for the parallel production of hydrogen (3) and of one or a plurality of carbon-containing products (8). In the method, hydrocarbons (2) are introduced into a reaction chamber (R) and are thermally decomposed into carbon and hydrogen in the presence of a carbon-rich granulated material (W). The invention is characterised in that at least a portion of the thermal energy necessary for the decomposition of the hydrocarbons is introduced into the reaction chamber (R) via a gaseous heat transfer medium.

Abstract translation: 一种用于同时生产氢气和含碳的产物的本发明的方法涉及一种方法，用于同时产生氢气的（3）和一个或更多个含碳产品富碳（8），其中，所述烃在反应空间（R）被引入，并在存在（2） 颗粒（W）被热分解成碳和氢。 本发明是通过一种气态传热介质到反应空间（R）被引入，其特征在于在所要求的用于烃的热能的分解的至少一个部分。

公开(公告)号：WO2009027433A3

公开(公告)日：2009-05-14

申请号：PCT/EP2008061221

申请日：2008-08-27

Applicant: BASF SE ,  SEEBER ALEXANDRA ,  SCHINDLER GOETZ-PETER ,  FREITAG KATRIN ,  KLEINE JAEGER FRANK ,  KLINGLER DIRK ,  BORGMEIER FRIEDER

Inventor： SEEBER ALEXANDRA ,  SCHINDLER GOETZ-PETER ,  FREITAG KATRIN ,  KLEINE JAEGER FRANK ,  KLINGLER DIRK ,  BORGMEIER FRIEDER

IPC: B01J35/00 ,  B01D53/86 ,  B01J19/26 ,  B01J37/34 ,  C01G23/07

CPC classification number: B01J35/004 ,  B01J2/003 ,  B01J2/04 ,  B01J19/24 ,  B01J19/26 ,  B01J21/08 ,  B01J35/0013 ,  B01J37/349 ,  B01J2219/00123 ,  B01J2219/00157 ,  B01J2219/00166 ,  B82Y30/00 ,  C01G23/07 ,  C01P2002/85 ,  C01P2004/04 ,  C01P2004/64 ,  C01P2004/84 ,  C01P2004/86 ,  C09C1/3661 ,  C09C1/3684 ,  Y10T428/2991 ,  Y10T428/2993

Abstract: The invention relates to a method for producing coated nanoparticles which comprise a core holding at least one first substance and at least one envelope from at least one additional substance that at least partially surrounds the core, in a fluid system. The invention also relates to nanoparticles obtainable by said method, to nanoparticles comprising a non-porous core that holds at least one first substance, and at least one envelope from at least one additional substance that at least partially surrounds the core, the nanoparticles having a narrow particle-size distribution. The invention finally relates to the use of the nanoparticles in photocatalysis and to a device for carrying out the method.

Abstract translation: 本发明涉及一种方法，其包括一个芯涂覆的纳米颗粒的制剂，其包含至少一个第一材料和至少一个芯，其可以在流动的系统来制备至少一种另外的物质的至少部分地包围鞘，根据该方法的纳米颗粒，所述纳米颗粒包含非 多孔芯，其包括至少一种第一材料和至少一个芯至少部分地围绕至少一种其它物质的多孔壳，其中，所述纳米颗粒具有较窄的粒度分布，使用这些Nanopartikelin光催化，以及用于执行该方法的装置。

公开(公告)号：WO2013004398A2

公开(公告)日：2013-01-10

申请号：PCT/EP2012002877

申请日：2012-07-05

Applicant: LINDE AG ,  MAAS HANS-JUERGEN ,  GOEKE VOLKER ,  MACHHAMMER OTTO ,  GUZMANN MARCUS ,  SCHNEIDER CHRISTIAN ,  HORMUTH WOLFGANG ,  BODE ANDREAS ,  KLINGLER DIRK ,  KERN MATTHIAS ,  KOLIOS GRIGORIOS ,  BASF SE

Inventor： MAAS HANS-JUERGEN ,  GOEKE VOLKER ,  MACHHAMMER OTTO ,  GUZMANN MARCUS ,  SCHNEIDER CHRISTIAN ,  HORMUTH WOLFGANG ,  BODE ANDREAS ,  KLINGLER DIRK ,  KERN MATTHIAS ,  KOLIOS GRIGORIOS

CPC classification number: C01B3/24 ,  C01B3/28 ,  C01B3/30 ,  C01B32/05 ,  C01B2203/0272 ,  C01B2203/04 ,  C01B2203/0425 ,  C01B2203/0485 ,  C01B2203/049 ,  C01B2203/06 ,  C01B2203/0805 ,  C01B2203/0811 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/0866 ,  C01B2203/1235 ,  C01B2203/1258 ,  C10B57/005 ,  Y02P20/128

Abstract: The invention relates to a method for the parallel production of hydrogen and of one or more carbon-containing products. In the method, hydrocarbons are introduced into a reaction chamber (R) and are thermally decomposed into carbon and hydrogen in the presence of a carbon-rich granulated material (W). The invention is characterised in that at least a portion of the thermal energy necessary for the decomposition of the hydrocarbon is introduced into the reaction chamber (R) via a gaseous heat transfer medium.

Abstract translation: 本发明涉及一种用于同时生产氢和一种或多种含碳产品，其中，在一个反应​​空间（R）烃被引入的，并在富碳颗粒（W）的存在下热分解成碳和氢。 本发明是通过一种气态传热介质到反应空间（R）被引入，其特征在于在所要求的用于烃的热能的分解的至少一个部分。

公开(公告)号：WO2011073123A3

公开(公告)日：2011-10-20

申请号：PCT/EP2010069476

申请日：2010-12-13

Applicant: BASF SE ,  GROSSSCHMIDT DIRK ,  YILMAZ BILGE ,  KLINGLER DIRK ,  ZOELS BERND

Inventor： GROSSSCHMIDT DIRK ,  YILMAZ BILGE ,  KLINGLER DIRK ,  ZOELS BERND

IPC: B01J29/76 ,  B01D53/94 ,  B01J29/072 ,  B01J37/02

CPC classification number: B01J37/0238 ,  B01D53/9427 ,  B01D2251/2062 ,  B01D2255/20738 ,  B01D2255/50 ,  B01J29/072 ,  B01J29/76 ,  B01J29/7615 ,  B01J29/763 ,  B01J29/85 ,  B01J35/0073 ,  B01J35/1014 ,  B01J35/1019 ,  B01J35/1057 ,  B01J37/0234 ,  B01J37/086 ,  B01J2229/186 ,  B01J2229/34 ,  B01J2229/40 ,  Y02C20/10

Abstract: The present invention relates to a ferrous zeolite, wherein the number of iron centers, relative to the zeolite, is greater than the number of cation positions of the zeolite. The present invention further relates to a ferrous zeolite that can be produced by gas phase reaction with iron pentacarbonyl, comprising a greater specific surface area than analogous ferrous zeolites produced by ion exchange and/or more hydrothermally stable than analogous ferrous zeolites produced by ion exchange. The present invention further relates to a ferrous zeolite of BETA structure that can be produced by gas phase reaction with iron pentacarbonyl, wherein the number of iron clusters greater than 10 nm is less than 15 wt%, relative to the total amount of iron. The present invention further relates to a method for producing ferrous zeolithic material, characterized in that doping with iron takes place by means of a gas phase reaction using iron pentacarbonyl. The present invention further relates to a method for catalytically reducing nitrogen oxides by adding ammoniac and using catalysts comprising said ferrous zeolithic material.

Abstract translation: 本发明涉及一种含铁沸石，其中铁原子的基于沸石的数量，比沸石的阳离子位置的数目越大。 此外，本发明涉及通过用五羰基铁，其具有比通过离子交换含铁沸石和/或水热比通过离子交换含铁沸石制造的类似的稳定产生模拟较大的比表面积的气相反应产生的含铁Zeoltihen。 此外，本发明betriff结构BETA的含铁沸石，通过用五羰基铁气相反应产生的，与铁簇是大于10纳米，小于15重量％的数量，基于铁的总量是。 此外，本发明涉及一种用于含有铁的沸石材料，其特征在于，所述掺杂经由使用五羰基铁气相反应用铁进行的制备方法。 此外，本发明涉及一种用于在添加氨的催化还原氮氧化物和使用包含所述含铁的沸石材料的催化剂的处理。

公开(公告)号：EP2935098A4

公开(公告)日：2016-10-26

申请号：EP13865384

申请日：2013-12-17

Applicant: BASF SE

Inventor： KERN MATTHIAS ,  GLENK FRIEDRICH ,  KLINGLER DIRK ,  BODE ANDREAS ,  KOLIOS GRIGORIOS ,  SCHUNK STEPHAN ,  WASSERSCHAFF GUIDO ,  BERNNAT JENS ,  ZOELS BERND ,  SCHMIDT SABINE ,  KÖNIG RENE

IPC: C01B3/24 ,  C01B3/38 ,  C01B32/40 ,  C10J3/00 ,  C10K3/02

CPC classification number: C01B3/24 ,  C01B3/38 ,  C01B31/18 ,  C01B32/40 ,  C01B2203/0238 ,  C01B2203/0272 ,  C01B2203/0283 ,  C01B2203/1235 ,  C10J3/06 ,  C10K3/026 ,  Y02P20/129 ,  Y02P20/146

公开(公告)号：ES2655323T3

公开(公告)日：2018-02-19

申请号：ES10787148

申请日：2010-12-13

Applicant: BASF SE

Inventor： GROSSSCHMIDT DIRK ,  YILMAZ BILGE ,  KLINGLER DIRK ,  ZOELS BERND

IPC: B01J29/76

Abstract: Procedimiento para la preparación de un material zeolítico que contiene hierro con las topologías CHA o LEV, caracterizado porque el dopaje con hierro se realiza a través de una reacción en fase gaseosa usando pentacarbonilo de hierro y el dopaje con hierro se realiza en dos etapas parciales (i) carga en fase gaseosa y (ii) descomposición térmica, caracterizado porque en otra etapa parcial (iii) se hace fluir a través del material zeolítico un gas portante con temperaturas de 500 a 1000 ºC a una presión de 10 a 1.000 kPa, en el que se usa como gas portante vapor de agua.

公开(公告)号：ZA201400783B

公开(公告)日：2017-11-29

申请号：ZA201400783

申请日：2014-02-03

Applicant: LINDE AG ,  BASF SE

Inventor： SCHNEIDER CHRISTIAN ,  MACHHAMMER OTTO ,  MAASS HANS-JUERGEN ,  KOLIOS GRIGORIOS ,  KLINGLER DIRK ,  KERN MATTHIAS ,  HORMUTH WOLFGANG ALOIS ,  GUZMANN MARCUS ,  GOEKE VOLKER ,  BODE ANDREAS

Abstract: The invention relates to a process for parallel preparation of hydrogen and one or more carbonaceous products, in which hydrocarbons are introduced into a reaction space (R) and decomposed thermally to carbon and hydrogen in the presence of carbon-rich pellets (W). It is a feature of the invention that at least a portion of the thermal energy required for the hydrocarbon decomposition is introduced into the reaction space (R) by means of a gaseous heat carrier.

公开(公告)号：RU2587078C2

公开(公告)日：2016-06-10

申请号：RU2012130178

申请日：2010-12-13

Applicant: BASF SE

Inventor： GROSSSHMIDT DIRK ,  JILMEZ BILDZH ,  KLINGLER DIRK ,  TSELZ BERND

IPC: B01J29/76 ,  B01D53/94 ,  B01J29/072 ,  B01J37/02

Abstract: Изобретениеотноситсяк способуполученияжелезосодержащегоцеолитногоматериалас топологиямиВЕА, СНА, LEV, ZSM. Способзаключаетсяв том, чтоцеолитныйматериаллегируютжелезомпосредствомреакциив газовойфазес использованиемпентакарбонилажелеза, причемлегированиежелезомпроводятв двестадии: (i) обработкав газовойфазеи (ii) термическоеразложение, инадополнительнойстадии (iii) черезцеолитныйматериалпропускаютпотокгаза-носителяпритемпературеот 500 до 1000°C идавленииот 0,1 до 10 бар, причемв качествегаза-носителяиспользуютводянойпар, воздух, инертныегазыилиихсмеси. Техническийрезультатзаключаетсяв получениижелезосодержащегоцеолитногоматериала, имеющегобольшуюудельнуюповерхностьи высокуюгидротермическуюстабильность. 8 з.п. ф-лы, 2 табл., 4 пр.

公开(公告)号：AU2013357293A1

公开(公告)日：2015-07-23

申请号：AU2013357293

申请日：2013-12-12

Applicant: BASF SE ,  LINDE AG

Inventor： MACHHAMMER OTTO ,  HORMUTH WOLFGANG ALOIS ,  SCHNEIDER CHRISTIAN ,  BODE ANDREAS ,  GOEKE VOLKER ,  MAASS HANS-JUERGEN ,  KERN MATTHIAS ,  KLINGLER DIRK ,  KONIG RENE ,  BRUGGEMANN PHILIPP ,  BERNNAT JENS ,  KOLIOS GRIGORIOS

IPC: B01J19/00 ,  B01J8/00

Abstract: 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.