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    • 5. 发明申请
    • PROCESS FOR PREPARING AMINO HYDROCARBONS BY DIRECT AMINATION OF HYDROCARBONS
    • 通过直接甲烷化来制备氨基烃的方法
    • US20130236801A1
    • 2013-09-12
    • US13781965
    • 2013-03-01
    • BASF SE
    • Bernd Bastian SCHAACKAlexander PanchenkoPhilipp Brueggemann
    • H01M8/06C07C209/02H01M8/10
    • H01M8/0612C07C209/02H01M2008/1095Y02P20/582C07C211/04C07C211/46C07C211/47C07C211/50C07C211/51
    • The present invention relates to a process for direct amination of hydrocarbons to amino hydrocarbons, comprising (a) the reaction of a reactant stream E comprising at least one hydrocarbon and at least one aminating reagent to give a reaction mixture R comprising at least one amino hydrocarbon and hydrogen in a reaction zone RZ, and (b) electrochemical removal of at least a portion of the hydrogen formed in the reaction from the reaction mixture R by means of at least one gas-tight membrane electrode assembly which is in contact with the reaction zone RZ on the retentate side and which has at least one selectively proton-conducting membrane, at least a portion of the hydrogen being oxidized over an anode catalyst to protons on the retentate side of the membrane, and the protons, after passing through the membrane, being partly or fully reacted with an oxidizing agent over a cathode catalyst to give water on the permeate side, and the oxidizing agent originating from a stream O which is contacted with the permeate side of the membrane.
    • 本发明涉及将烃直接胺化成氨基烃的方法,其包括(a)包含至少一种烃和至少一种胺化试剂的反应物流E的反应,得到包含至少一种氨基烃的反应混合物R 和反应区RZ中的氢,和(b)通过与反应接触的至少一个气密膜电极组件电化学去除反应混合物R中形成的氢的至少一部分 并且具有至少一个选择性质子传导膜,所述氢的至少一部分在阳极催化剂上被氧化以在所述膜的滞留侧上的质子和所述质子在通过所述膜之后 ,在阴极催化剂上与氧化剂部分或完全反应以在渗透侧产生水,并且源自流O的氧化剂,其中i s与膜的渗透侧接触。
    • 6. 发明申请
    • PROCESS FOR PREPARING AMINO HYDROCARBONS BY DIRECT AMINATION OF HYDROCARBONS
    • 通过直接甲烷化来制备氨基烃的方法
    • US20130233721A1
    • 2013-09-12
    • US13785980
    • 2013-03-05
    • BASF SE
    • Bernd Bastian SCHAACKAlexander PanchenkoPhilipp Brueggemann
    • C07C209/02C25B3/04
    • C07C209/02C25B3/00C25B3/04Y02P20/582C07C211/46C07C211/47C07C211/50C07C211/51C07C211/04
    • The present invention relates to a process for direct amination of hydrocarbons to amino hydrocarbons, comprising (a) the reaction of a reactant stream E comprising at least one hydrocarbon and at least one aminating reagent to give a reaction mixture R comprising at least one amino hydrocarbon and hydrogen in a reaction zone RZ, and (b) electrochemical removal of at least a portion of the hydrogen formed in the reaction from the reaction mixture R by means of at least one gas-tight membrane electrode assembly which is in contact with the reaction zone RZ on the retentate side and which has at least one selectively proton-conducting membrane, at least a portion of the hydrogen being oxidized over an anode catalyst to protons on the retentate side of the membrane, and the protons, after passing through the membrane, being partly or fully reduced by applying a voltage over a cathode catalyst to give hydrogen on the permeate side.
    • 本发明涉及将烃直接胺化成氨基烃的方法,其包括(a)包含至少一种烃和至少一种胺化试剂的反应物流E的反应,得到包含至少一种氨基烃的反应混合物R 和反应区RZ中的氢,和(b)通过与反应接触的至少一个气密膜电极组件电化学去除反应混合物R中形成的氢的至少一部分 并且具有至少一个选择性质子传导膜,所述氢的至少一部分在阳极催化剂上被氧化以在所述膜的滞留侧上的质子和所述质子在通过所述膜之后 ,通过在阴极催化剂上施加电压以在渗透侧产生氢来部分或完全还原。
    • 7. 发明申请
    • LOW METAL LOADED, CATALYST COMPOSITIONS INCLUDING ACIDIC MIXED METAL OXIDE AS SUPPORT
    • 低金属负载,催化剂组合物,包括酸性混合金属氧化物作为支持
    • US20120238780A1
    • 2012-09-20
    • US13456444
    • 2012-04-26
    • Stephen W. KingStefan K. Mierau
    • Stephen W. KingStefan K. Mierau
    • C07C209/02
    • B01J23/8896B01J21/12B01J35/008B01J35/1014B01J35/1019B01J37/0201C07C209/00
    • The invention provides a method of transaminating a reactant with a catalyst composition comprising support and catalyst portions. The support includes an acidic mixed metal oxide including a transitional alumina and a second metal oxide. The transitional alumina can comprise delta or theta alumina, in combination with other transitional phases, or an alpha or gamma alumina. The second metal oxide has a weight percentage less than the weight percentage of alumina. The catalyst portion is 25 weight percent or less of the catalyst composition and is composed of nickel and rhenium. The catalyst portion includes nickel in an amount in the range of 2 to 20 weight percent, based upon total catalyst composition weight, and there is no boron in the catalyst portion. The method provides high activity and selectivity for reactant transamination to a desired product while minimizing the formation of unwanted cyclic products.
    • 本发明提供了一种用包含载体和催化剂部分的催化剂组合物将反应物转氨的方法。 载体包括含有过渡氧化铝和第二金属氧化物的酸性混合金属氧化物。 过渡氧化铝可以包含与其它过渡相结合的δ或θ氧化铝,或α或γ氧化铝。 第二金属氧化物的重量百分比小于氧化铝的重量百分数。 催化剂部分为催化剂组合物的25重量%以下,由镍和铼构成。 催化剂部分包括基于总催化剂组合物重量的2-20重量%范围内的量的镍,并且在催化剂部分中不存在硼。 该方法提供了对期望产物的反应物转氨酸的高活性和选择性,同时使不期望的环状产物的形成最小化。
    • 8. 发明申请
    • METHOD OF PREPARING NERAMEXANE
    • 制备NERAMEXANE的方法
    • US20120130130A1
    • 2012-05-24
    • US13377954
    • 2010-06-28
    • Herbert KollerMchael PyerinFederico Sbrogio
    • Herbert KollerMchael PyerinFederico Sbrogio
    • C07C211/35C07C209/02
    • C07C209/62C07C211/35
    • The method of producing a salt of 1-amino-1,3,3,5,5-pentamethylcyclohexane comprising steps (i) to (v): (i) converting isophorone to 3,3,5,5-tetramethylcyclohexanone; (ii) converting 3,3,5,5-tetramethylcyclohexanone obtained in step (i) to 1-hydroxy-1,3,3,5,5-pentamethylcyclohexane; (iii) converting 1-hydroxy-1,3,3,5,5-pentamethylcyclohexane obtained in step (ii) to 1-chloroacetamido-1,3,3,5,5-pentamethylcyclohexane; (iv) converting 1-chloroacetamido-1,3,3,5,5-pentamethylcyclohexane obtained in step (iii) to 1-amino-1,3,3,5,5-pentamethylcyclohexane; wherein at least one of 3,3,5,5-tetramethylcyclohexanone, 1-hydroxy-1,3,3,5,5-pentamethylcyclohexane, 1-chloroacetamido-1,3,3,5,5-pentamethylcyclohexane, is not subjected to a purification step.
    • 制备1-氨基-1,3,3,5,5-五甲基环己烷盐的方法,包括步骤(i)至(v):(i)将异佛尔酮转化为3,3,5,5-四甲基环己酮; (ii)将步骤(i)中获得的3,3,5,5-四甲基环己酮转化为1-羟基-1,3,3,5,5-五甲基环己烷; (iii)将步骤(ii)中获得的1-羟基-1,3,3,5,5-五甲基环己烷转化为1-氯乙酰胺基-1,3,3,5,5-五甲基环己烷; (iv)将步骤(iii)中获得的1-氯乙酰氨基-1,3,3,5,5-五甲基环己烷转化为1-氨基-1,3,3,5,5-五甲基环己烷; 其中3,3,5,5-四甲基环己酮,1-羟基-1,3,3,5,5-五甲基环己烷,1-氯乙酰氨基-1,3,3,5,5-五甲基环己烷中的至少一种不经受 纯化步骤。