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    • 1. 发明申请
    • CYCLOHEXANONE PRODUCTION PROCESS WITH MULTIPLE POST-DISTILLATION
    • 具有多次后蒸馏的环辛砜生产工艺
    • WO2009080620A1
    • 2009-07-02
    • PCT/EP2008/067632
    • 2008-12-16
    • DSM IP Assets B.V.DORTMONT, VAN, Godefridus MariaHORSELS, MarleenPARTON, Rudy Francois Maria JozefTINGE, Johan Thomas
    • 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,所述催化活性金属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; 将第二馏分分离成富含环己醇的第三馏分和富含苯酚的第四馏分,使用蒸馏; 将至少部分第四馏分进行进一步的蒸馏步骤,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连续或间歇地将至少部分第六馏分分离成另外的蒸馏步骤,从而形成第七馏分和八馏分的附加步骤,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。
    • 2. 发明申请
    • CYCLOHEXANONE PRODUCTION PROCESS WITH MODIFIED POST-DISTILLATION
    • 具有改性后蒸馏的环辛砜生产工艺
    • WO2009080621A1
    • 2009-07-02
    • PCT/EP2008/067635
    • 2008-12-16
    • DSM IP ASSETS B.V.HORSELS, MarleenPARTON, Rudy Francois Maria JozefTINGE, Johan Thomas
    • HORSELS, MarleenPARTON, Rudy Francois Maria JozefTINGE, Johan Thomas
    • C07C45/82C07C49/403B01J10/00C07C29/48C07C45/00C07C45/29C07C51/00C07C55/14C07C35/08C08F232/00
    • 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 a) hydrogenating phenol to form a product stream comprising cyclohexanone and unreacted phenol; b) 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; c) separating the second fraction into a third fraction, rich in cyclohexanol, and a fourth fraction, rich in phenol and, using distillation; d) 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, wherein step d) is carried out in a vacuum distillation column equipped with trays in the lower part of the column, and wherein in the upper part of the column, i.e. in the part above the feed inlet, packing material is present instead of trays in at least part of said upper part, which packing material has a comparable or improved separating efficiency, and provides a reduction of the pressure drop by at least 30%, preferably more than 50%, as compared to the case with trays in the upper part, under otherwise similar distillation conditions.
    • 本发明涉及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:a)氢化苯酚以形成包含环己酮和未反应苯酚的产物流; b)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; c)将第二级分分离成富含环己醇的第三馏分和富含苯酚的第四级分,并使用蒸馏; d)使至少部分第四馏分进一步蒸馏步骤,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 比苯酚高的沸点和苯酚,其中步骤d)在柱的下部配备有塔板的真空蒸馏塔中进行,并且其中在塔的上部,即在进料的上方的部分 入口,包装材料代替所述上部的至少一部分中的托盘,该填充材料具有相当或改进的分离效率,并且将压降降低至少30%,优选大于50%,如 与上部托盘的情况相比,在相似的蒸馏条件下。
    • 8. 发明申请
    • PROCESS FOR ENZYMATIC HYDROLYSIS OF LIGNOCELLULOSIC MATERIAL AND FERMENTATION OF SUGARS
    • 木质纤维素材料的酶解水解和糖的发酵工艺
    • WO2015165951A1
    • 2015-11-05
    • PCT/EP2015/059316
    • 2015-04-29
    • DSM IP ASSETS B.V.
    • NOORDAM, BertusBEVERS, Loes ElizabethPARTON, Rudy Francois Maria JozefBERKHOUT, Michael Petrus Jozef
    • C12P19/02D21C3/26C12P19/14
    • C12P19/02C12P19/14C12P2203/00C13K1/02C13K13/00C13K13/002D21C3/26Y02E50/16
    • The invention relates to a process for the preparation of a fermentation product from lignocellulosic material, comprising the following steps: • a) optionally, pretreatment of the lignocellulosic material, • b) optionally, washing of the optionally pretreated lignocellulosic material, • c) enzymatic hydrolysis of the optionally washed and/or optionally pretreated lignocellulosic material using an enzyme composition comprising at least two cellulases and whereby the enzyme composition at least comprises LPMO, and optionally purifying the hydrolysed lignocellulosic material, • d) fermentation of the hydrolysed lignocellulosic material to produce a fermentation product, and • e) optionally, recovery of a fermentation product, wherein the amounts of formed hydrolysed oxidation product gluconic acid at the end of the enzymatic hydrolysis by the oxidation by LPMO of the lignocellulosic material containing cellulose and/or cello-oligosaccharides is kept between 3 to 80 g/kg glucan present in the lignocellulosic material by adding a suitable amount of oxygen after the pre-treatment and before and/ or during the enzymatic hydrolysis to the lignocellulosic material, preferably the formed hydrolysed oxidation product is gluconic acid, an aldonic acid and/or geminal diol, more preferably the hydrolysed oxidation product is gluconic acid.
    • 本发明涉及一种用于从木质纤维素材料制备发酵产物的方法,包括以下步骤:a)任选地预处理木质纤维素材料,b)任选地,洗涤任选预处理的木质纤维素材料,c)酶促 使用包含至少两种纤维素酶的酶组合物对任选洗涤和/或任选预处理的木质纤维素材料进行水解,由此该酶组合物至少包含LPMO,并任选地纯化水解的木质纤维素材料; d)水解的木质纤维素材料的发酵以产生 发酵产物,和e)任选地回收发酵产物,其中在酶水解结束时形成的水解氧化产物葡糖酸的量通过LPMO氧化含有纤维素和/或低聚半乳糖的木质纤维素材料 保持在3至80g / kg葡聚糖之间 通过在预处理之后和在酶水解之前和/或期间在木质纤维素材料中加入适量的氧,优选形成的水解氧化产物是葡糖酸,醛糖酸和/或偕二醇,存在于木质纤维素材料中, 更优选地,水解的氧化产物是葡萄糖酸。
    • 10. 发明申请
    • CONTINUOUS PROCESS FOR THE PRODUCTION OF A VALUABLE COMPOUND FROM LIGNOCELLULOSIC BIOMASS
    • 用于生产有效化合物的连续生产过程
    • WO2015007601A1
    • 2015-01-22
    • PCT/EP2014/064795
    • 2014-07-10
    • DSM IP ASSETS B.V.
    • HOVING, Hendrik DerkPARTON, Rudy Francois Maria Jozef
    • C07C51/00C07D307/46C07D307/48C07D307/50C07C53/02C07C59/185
    • C07D307/50C07C51/00C07C51/47C07C51/48C07D307/46C07D307/48C07C59/185C07C53/02
    • The invention relates to continuous process for the production of a valuable compound from a lignocellulosic biomass, said process comprising: subjecting a slurried lignocellulosic biomass to an acid hydrolysis reaction in a reactor having an inlet and an outlet, in the presence of a mineral acid and under conditions of temperature, time, and acid concentration to yield a biomass hydrolysate comprising a valuable compound; subjecting said biomass hydrolysate to a solvent-extraction to yield an organic phase comprising the valuable compound, and an aqueous phase comprising at least part of the mineral acid and separating said phases resulting in an organic stream and an aqueous stream, optionally concentrating said aqueous stream; recycling the optionally concentrated aqueous stream to the acid hydrolysis reaction; and optionally isolating the valuable compound. The process may result in reduced consumption of mineral acid and may give efficient, stable, and robust process.
    • 本发明涉及用于从木质纤维素生物质生产有价值化合物的连续方法,所述方法包括:在无机酸存在下,在具有入口和出口的反应器中使浆状木质纤维素生物质进行酸水解反应,和 在温度,时间和酸浓度的条件下,产生包含有价值化合物的生物质水解产物; 使所述生物质水解产物进行溶剂萃取以产生包含有价值化合物的有机相和包含至少部分无机酸的水相,并分离所述相,得到有机物流和水流,任选地将所述含水物流 ; 将任选浓缩的水流再循环到酸水解反应中; 并任选分离有价值的化合物。 该方法可能导致无机酸的消耗降低,并且可以提供有效,稳定和稳定的过程。