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    • 96. 发明授权
    • VERFAHREN ZUR HERSTELLUNG VON 1,6-HEXANDIOL IN EINER REINHEIT VON ÜBER 99,5%
    • PROCESS超过99.5%的的纯度的制备1,6-己二醇
    • EP1765751B1
    • 2007-10-31
    • EP05759413.7
    • 2005-07-07
    • BASF Aktiengesellschaft
    • HAUNERT, AndreaPINKOS, RolfKRUG, ThomasSIRCH, TilmanKOCH, MichaelTEBBEN, Gerd-Dieter
    • C07C29/145C07C29/149C07C31/20
    • C07C29/145C07C29/149C07C2601/14C07C31/20C07C35/08
    • The invention relates to a method for the production of 1,6-hexanediol by hydrogenation of ester mixtures of dialkyl adipates and alkyl 6-hydroxycaproates, containing 1,4-cyclohexanedione and 4-hydroxycyclohexan-1-one as impurities, by a) removing excess alcohol and low-boilers from the obtained ester mixture in a first distillation stage (alcohol removal) b) separation of the sump product into an ester fraction essentially free of 1,4-cyclohexanediols and a fraction containing at least the greater part of the 1,4-cyclohexanediols in a second distillation stage, c) catalytic hydrogenation of the ester fraction essentially free of 1,4-cyclohexanediols (ester hydrogenation) and d) isolation of 1,6-hexanediol from the hydrogenation product in a known manner by a simple distillation step, characterised in that, before step a) and/or before step b), the ester mixture is selectively hydrogenated (purification hydrogenation).
    • 本发明提供了一种通过氢化己二酸二烷基酯制备1,6-己二醇的方法,烷基-6- hydroxycaproates,1,4-环己二酮和4-羟基-1-酮作为酯的混合物,其包括杂质,由一个)释放的酯化混合物所得 过量的醇,并在第一蒸馏步骤(除去醇)低沸物,b)进行的底部产物在第二蒸馏阶段的分离成酯馏分基本上不含1,4-环己二醇和一小部分,其至少包括 大部分1,4-环己二醇的,c)中催化氢化酯馏分基本上不含在净化蒸馏阶段1,4-环己二醇(酯氢化)和d),以这样的方式从氢化流出物获得的1,6-己二醇 本身已知的方法,它包括选择性氢化阶段之前一个该酯的混合物)和/或步骤b)之前(净化氢化)。
    • 98. 发明公开
    • VERFAHREN ZUR HERSTELLUNG VON DEFINIERTEN GEMISCHEN AUS THF, BDO UND GBL DURCH GASPHASENHYDRIERUNG
    • 一种用于通过汽相氢化制备THF,BDO和GBL的定义混合物的过程
    • EP1694662A2
    • 2006-08-30
    • EP04803523.2
    • 2004-12-04
    • BASF Aktiengesellschaft
    • RÖSCH, MarkusPINKOS, RolfHESSE, MichaelSCHLITTER, StephanJUNICKE, HenrikSCHUBERT, OlgaWECK, AlexanderWINDECKER, Gunther
    • C07D307/08C07D307/32
    • C07D307/33C07D307/08
    • The invention relates to a method for variable production of mixtures of optionally alkyl-substituted BDO, GBL and THF by two-stage hydrogenation in the gaseous phase of C4-dicarboxylic acids and/or the derivatives thereof, characterized in that a) a gas flow of C4-dicarboxylic acids and/or the derivatives thereof is hydrogenated in a first stage in the gaseous phase on a catalyst at a pressure of 2-100 bars and at a temperature of 200 °C to 300 °C in a first reactor in the presence of a catalyst in the form of catalyst moulded bodies with a volume of less than 20 mm3, consisting of 5 - 95 wt. % Cu-oxide and 5 - 95 wt. % of an oxide with acid centres in order to form a flow maintly consisting of optionally aryl-substituted GBL and THF, b) succinic anhydride optionally arising therefrom is separated by partial condensation, c) the products THF, water and GBL which remain predominantly in the gaseous phase during said partial condensation are reacted at the same pressure or at a pressure which is reduced in order to reduce flow losses in the hydrogenation circuit at a temperature of 150 to 240 °C in a second reactor on a catalyst of > 95 wt. % CuO and 5 to 95 wt. % of one or several oxides selected from the group consisting of ZnO, Al2O3, SiO2, TiO2, ZrO2, CeO2, MgO, CaO, SrO, BaO, La2O3, and Mn2O3 in order to form a mixture consisting of a flow containing BDO, GBL and THF, d) the hydrogen is separated from the products and returned to the hydrogenation, e) the products THF, BDO, GBL and Wasser are separated in a distillatory manner, a flow rich in GBL is optionally returned to the second reactor or is optionally removed therefrom and BDO, THF and GBL are processed in a distillatory manner, and the ratio of the products THF, GBL and BDO is adjusted in relation to each other in the region of 10 to 100 wt. % THF, 0 to 90 wt. % GBL and 0 to 90 wt. % BDO exclusively by varying the temperatures in the two hydrogenation areas, in addition to that of the GBL return flow.