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    • 11. 发明公开
    • CYCLOHEXANONE PRODUCTION PROCESS WITH MULTIPLE POST-DISTILLATION
    • VERFAHREN ZUR HERSTELLUNG VON CYCLOHEXANON麻省理工学院
    • EP2231577A1
    • 2010-09-29
    • EP08863517.2
    • 2008-12-16
    • DSM IP Assets B.V.
    • DORTMONT, VAN, Godefridus MariaHORSELS, MarleenPARTON, Rudy Francois Maria JozefTINGE, Johan Thomas
    • C07C45/82C07C29/48C07C45/00C07C45/29C07C51/00B01J10/00C08F232/00C07C49/403C07C55/14C07C35/08
    • C07C29/50C07C45/006C07C45/82C07C51/00C07C2601/14C07C49/403C07C55/14C07C35/08
    • The present invention relates to a method for continuously preparing cyclohexanone from phenol making use of a catalyst comprising at least one catalytically active metal selected from platinum and palladium comprising hydrogenating phenol to form a product stream comprising cyclohexanone and unreacted phenol; separating at least part of the product stream, or at least part of the product stream from which one or more components having a lower boiling point than cyclohexanone have been removed, into a first fraction comprising cyclohexanone and a second fraction comprising phenol and cyclohexanol, using distillation; separating the second fraction into a third fraction, rich in cyclohexanol, and a fourth fraction, rich in phenol, using distillation; - subjecting at least part of the fourth fraction to a further distillation step, thereby forming a fifth fraction and a sixth fraction, wherein the fifth fraction is enriched in phenol compared to the sixth fraction, and wherein the sixth fraction comprises side-products having a higher boiling point than phenol, and phenol; and which method is characterized in the additional step of continuously or intermittently separating at least part of the sixth fraction to yet a further distillation step, thereby forming a seventh fraction and an eight fraction, wherein the seventh fraction is enriched in phenol compared to the eight fraction, and wherein the eight fraction comprises side-products having a higher boiling point than phenol.
    • 本发明涉及一种使用包含至少一种选自铂和钯的催化活性金属的催化剂从苯酚连续制备环己酮的方法,其包括氢化苯酚以形成包含环己酮和未反应苯酚的产物流; 将至少部分产物流或至少部分产物流从其中除去一个或多个沸点低于环己酮的组分的产物流转化成包含环己酮的第一馏分和包含苯酚和环己醇的第二馏分,使用 蒸馏; 将第二级分分离成富含环己醇的第三级分,和使用蒸馏富含苯酚的第四级分; - 将第四部分的至少一部分喷射至另一蒸馏步骤,从而形成第五馏分和第六馏分,其中与第六馏分相比,第五馏分富含苯酚,其中第六馏分包含具有 沸点高于苯酚,苯酚; 并且该方法的特征在于将第六馏分的至少一部分连续或间歇地分离成另外的蒸馏步骤的另外步骤,从而形成第七馏分和八馏分,其中第七馏分富含苯酚,与八 馏分,其中八馏分包含沸点高于苯酚的副产物。
    • 12. 发明公开
    • OXIDATION OF HYDROCARBONS
    • 氧化哇哇哇哇哇哇哇哇
    • EP2220039A1
    • 2010-08-25
    • EP08844604.2
    • 2008-10-08
    • ExxonMobil Chemical Patents Inc.
    • DAKKA, Jihad, M.VARTULI, James, C.ZUSHMA, Stephen
    • C07C407/00C07C409/08C07C409/02C07C409/14C07C55/14C07C39/16
    • C07C409/04B01D15/00B01J31/0235C07C29/50C07C37/08C07C37/20C07C45/33C07C45/53C07C407/00C07C407/003C07C409/08C07C409/14C07C2601/14Y02P20/52C07C49/403C07C35/08C07C39/04C07C39/16C07C409/06C07C409/10
    • In a process for oxidizing a hydrocarbon to a corresponding hydroperoxide, alcohol, ketone, carboxylic acid or dicarboxylic acid, the hydrocarbon is contacted with an oxygen- containing gas in the presence of a catalyst comprising a cyclic imide of the general formula (I); wherein each of R1 and R2 is independently selected from hydrocarbyl and substituted hydrocarbyl radicals having 1 to 20 carbon atoms, or from the groups SO3H, NH2, OH and NO2, or from the atoms H, F, Cl, Br and I provided that R1 and R2 can be linked to one another via a covalent bond; each of Q1 and Q2 is independently selected from C, CH, N and CR3; each of X and Z is independently selected from C, S, CH2, N, P and elements of Group 4 of the Periodic Table; Y is O or OH; k is O, 1, or 2; 1 is 0, 1, or 2; m is 1 to 3, and R3 can be any of the entities listed for R1. The contacting produces an effluent comprising an oxidized hydrocarbon product and unreacted imide catalyst of said formula (I) and the effluent is treated with a solid sorbent to remove at least part of the unreacted imide catalyst and produce a treated effluent comprising said oxidized hydrocarbon product. The organic phase can then be recovered.
    • 在将烃氧化成相应的氢过氧化物,醇,酮,羧酸或二羧酸的方法中,烃在含有通式(I)的环状酰亚胺的催化剂存在下与含氧气体接触: 其中R 1和R 2各自独立地选自具有1至20个碳原子的烃基和取代的烃基,或者来自SO 3 H,NH 2,OH和NO 2基团,或者来自原子H,F,Cl,Br和I,条件是R1 并且R 2可以通过共价键彼此连接; Q1和Q2中的每一个独立地选自C,CH,N和CR 3; X和Z各自独立地选自C,S,CH 2,N,P和元素周期表第4族的元素; Y是O或OH; k为0,1或2; l为0,1或2; m为1至3,R3可为R1列出的任何实体。 接触产生包含所述式(I)的氧化烃产物和未反应的酰亚胺催化剂的流出物,并且用固体吸附剂处理流出物以除去至少部分未反应的酰亚胺催化剂并产生包含所述氧化的烃产物的经处理的流出物。 然后可以回收有机相。