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    • 13. 发明授权
    • Process for preparing polyether alcohols
    • 制备聚醚醇的方法
    • US09120731B2
    • 2015-09-01
    • US13813300
    • 2011-08-08
    • Achim LoefflerMichael StoesserWolfgang LothRalf BoehlingSirus Zarbakhsh
    • Achim LoefflerMichael StoesserWolfgang LothRalf BoehlingSirus Zarbakhsh
    • C07C41/02C08G65/26
    • C07C41/02C08G65/2696
    • What is proposed is a process for preparing polyether alcohols by conversion of the following reactants: a) one or more alkylene oxides and optionally carbon dioxide and b) one or more H-functional starter substances, in the presence of a catalyst, to form a liquid reaction mixture, in a reaction unit (1), which is characterized in that the reaction unit (1) has internals (2) which form a multitude of microstructured flow channels which bring about multiple splitting of the liquid reaction mixture into component flow paths and recombination thereof in altered arrangement, the multiple splitting and recombination being repeated several times and the microstructured flow channels having a characteristic dimension which is defined as the greatest possible distance of any particle in the liquid reaction mixture from the wall of a flow channel closest to the particle, in the range from 20 to 10 000 μm, the result being that the flow profile of the liquid reaction mixture approximates to ideal plug flow as a result of the microstructured flow channels.
    • 提出的是通过以下反应物的转化来制备聚醚醇的方法:a)一种或多种环氧烷烃和任选的二氧化碳,和b)一种或多种H官能起始物质,在催化剂存在下,形成 液体反应混合物,在反应单元(1)中,其特征在于反应单元(1)具有形成多个微结构流动通道的内部(2),其导致液体反应混合物多次分离成组分流动路径 并且其重组在改变的布置中,多次分裂和重组被重复几次,并且微结构流动通道具有被定义为液体反应混合物中任何颗粒与流动通道的壁最接近的最大可能距离的特征尺寸 颗粒在20至1000000范围内,其结果是液体反应混合物的流动分布近似于id 作为微结构化流动通道的结果,流动的流动。
    • 14. 发明申请
    • PROCESS FOR PREPARING POLYETHER ALCOHOLS
    • 制备聚醚醇的方法
    • US20130131389A1
    • 2013-05-23
    • US13813300
    • 2011-08-08
    • Achim LoefflerMichael StoesserWolfgang LothRalf BoehlingSirus Zarbakhsh
    • Achim LoefflerMichael StoesserWolfgang LothRalf BoehlingSirus Zarbakhsh
    • C07C41/02
    • C07C41/02C08G65/2696
    • What is proposed is a process for preparing polyether alcohols by conversion of the following reactants: a) one or more alkylene oxides and optionally carbon dioxide and b) one or more H-functional starter substances, in the presence of a catalyst, to form a liquid reaction mixture, in a reaction unit (1), which is characterized in that the reaction unit (1) has internals (2) which form a multitude of microstructured flow channels which bring about multiple splitting of the liquid reaction mixture into component flow paths and recombination thereof in altered arrangement, the multiple splitting and recombination being repeated several times and the microstructured flow channels having a characteristic dimension which is defined as the greatest possible distance of any particle in the liquid reaction mixture from the wall of a flow channel closest to the particle, in the range from 20 to 10 000 μm, the result being that the flow profile of the liquid reaction mixture approximates to ideal plug flow as a result of the microstructured flow channels.
    • 提出的是通过以下反应物的转化来制备聚醚醇的方法:a)一种或多种环氧烷烃和任选的二氧化碳,和b)一种或多种H官能起始物质,在催化剂存在下,形成 液体反应混合物,在反应单元(1)中,其特征在于反应单元(1)具有形成多个微结构流动通道的内部(2),其导致液体反应混合物多次分离成组分流动路径 并且其重组在改变的布置中,多次分裂和重组被重复几次,并且微结构流动通道具有被定义为液体反应混合物中任何颗粒与流动通道的壁最接近的最大可能距离的特征尺寸 该颗粒在20至1000000m范围内,结果是液体反应混合物的流动分布近似于id 作为微结构化流动通道的结果,流动的流动。
    • 16. 发明授权
    • Process for preparing isopropanol and 2-butanol from the corresponding alkanes
    • 从相应的烷烃制备异丙醇和2-丁醇的方法
    • US07750194B2
    • 2010-07-06
    • US12374351
    • 2007-07-16
    • Georg DegenSven CroneRalf BoehlingAnsgar Gereon AltenhoffWolfgang RohdeJochen BuerkleGoetz-Peter SchindlerThomas HoltmannMarkus Schmitt
    • Georg DegenSven CroneRalf BoehlingAnsgar Gereon AltenhoffWolfgang RohdeJochen BuerkleGoetz-Peter SchindlerThomas HoltmannMarkus Schmitt
    • C07C29/09
    • C07C67/04C07C29/095Y02P20/127C07C31/10C07C31/12C07C69/06C07C69/14
    • A process for preparing alkanols (I) selected from the group consisting of isopropanol and 2-butanol from the corresponding alkanes (II) selected from the group consisting of propane and n-butane, comprising the steps of: A) providing a starting gas stream a comprising the alkane (II); B) feeding the starting gas stream a comprising the alkane (II) into a dehydrogenation zone and subjecting the alkane (II) to a dehydrogenation to the alkene (III) to obtain a product gas stream b comprising the alkene (III) and unconverted alkane (II), with or without high boilers, steam, hydrogen and low boilers; C) at least compressing product gas stream b, optionally separating product gas stream b into an aqueous phase c1, a phase c2 comprising the alkene (III) and the alkane (II), with or without high boilers, and a gas phase c3 comprising hydrogen and low boilers; D) reacting product gas stream b or the phase c2 comprising alkene (III) and alkane (II) with an organic acid (IV) in an esterification zone to obtain a product mixture d comprising the corresponding alkyl ester (V) of the organic acid and the unconverted alkane (II); E) removing from product mixture d a gas stream e1 which comprises an alkane (II) and is recycled into the dehydrogenation zone if appropriate, and a product mixture e2 comprising the alkyl ester; F) reacting the product mixture e2 comprising the alkyl ester with water in an ester hydrolysis zone to give a product mixture f comprising the alkanol (I) and the organic acid (IV); G) removing the alkanol (I) and the organic acid (IV) from product mixture f and, if appropriate, recycling the organic acid into the esterification zone.
    • 从选自丙烷和正丁烷的相应的烷烃(II)制备选自异丙醇和2-丁醇的链烷醇(I)的方法,包括以下步骤:A)提供起始气流 a包含烷烃(II); B)将包含烷烃(II)的起始气体流(a)进料到脱氢区中并使烷烃(II)脱氢至烯烃(III),得到包含烯烃(III)和未转化烷烃的产物气流b (II),有或没有高锅炉,蒸汽,氢气和低锅炉; C)至少压缩产物气流b,任选地将产物气流b分离成水相c1,包含烯烃(III)和烷烃(II)的阶段c2,具有或不具有高锅炉,以及气相c3,其包含 氢和低锅炉; D)使产物气流b或包含烯烃(III)和烷烃(II)的相c与酯化区中的有机酸(IV)反应,得到包含相应的有机酸烷基酯(V)的产物混合物d 和未转化的烷烃(II); E)从产物混合物d除去包含烷烃(II)的气流e1,并且如果合适的话再循环到脱氢区中,以及包含烷基酯的产物混合物e2; F)在酯水解区中使包含烷基酯的产物混合物e2与水反应,得到包含链烷醇(I)和有机酸(IV)的产物混合物f; G)从产物混合物f中除去链烷醇(I)和有机酸(IV),如果合适,将有机酸再循环到酯化区。