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    • 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。
    • 3. 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。
    • 5. 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。
    • 6. 发明申请
    • PROCESS FOR THE PREPARATION OF FORMYLVALERIC ACID AND ADIPIC ACID
    • 制备异戊酸和丙二酸的方法
    • WO2014111446A1
    • 2014-07-24
    • PCT/EP2014/050764
    • 2014-01-16
    • DSM IP ASSETS B.V.
    • PARTON, Rudy Francois Maria JozefJANSSEN, Michèle Catherine ChristianneENGENDAHL, BarthelVRIES, DE, Johannes Gerardus
    • C07C51/14C07C51/373C07C51/42C07C51/44C07C51/48C07C57/03C07C59/147C07C51/09C07D307/32
    • C07C51/373C07C51/09C07C51/12C07C51/14C07C51/42C07C51/44C07C51/48C07D307/32C07C59/147C07C55/14C07C57/03
    • The invention relates to a process for the production of 5-formylvaleric acid and adipic acid or esters thereof from an isomeric mixture of pentenoic acid or esters thereof said mixture comprising at least 4-pentenoic acid or esters thereof, and further comprising 3-pentenoic acid and/or 2-pentenoic acid or esters thereof, theprocess comprising: (a) subjecting the isomeric mixture of pentenoic acid to a hydroformylation reaction comprising a hydroformylation catalyst which is non-isomerizing towards the pentenoic acid or esters thereof to obtain a mixture comprising 5-formylvaleric acid or esters thereof and further comprising 3-pentenoic acid and/or 2-pentenoic acid, or esters thereof; (b) separating the 3-pentenoic acid and/or 2-pentenoic acid, or esters thereof from the 5-formylvaleric acid or esters thereof; (c) subjecting the separated pentenoic acids or esters thereof to a carbonylation reaction comprising an isomerizing carbonylation catalyst to obtain adipic acid or esters thereof; (d) optionally isolating the adipic acid or ester thereof; and (e) optionally isolating the separated 5-formylvaleric acid or esters thereof. The process allows for efficient production of two different intermediates for producing polyamide using a single process, with good selectivity, little waste, in an economically efficient fashion. The process is very suitable to use an isomeric pentenoic acid mixture obtained from valerolactone, and can be used to produce renewable polyamide intermediates using a single process.
    • 本发明涉及一种由戊烯酸或其酯的异构体混合物生产5-甲酰戊酸和己二酸或其酯的方法,所述混合物包含至少4-戊烯酸或其酯,并且还包含3-戊烯酸 和/或2-戊烯酸或其酯,所述方法包括:(a)使戊烯酸的异构体混合物进行加氢甲酰基化反应,所述加氢甲酰化反应包含对戊烯酸或其酯异构化的加氢甲酰化催化剂,以获得包含5 - 甲酰基戊酸或其酯,并且还包含3-戊烯酸和/或2-戊烯酸或其酯; (b)从5-甲酰戊酸或其酯分离3-戊烯酸和/或2-戊烯酸或其酯; (c)使分离的戊烯酸或其酯进行包含异构化羰基化催化剂的羰基化反应以获得己二酸或其酯; (d)任选分离己二酸或其酯; 和(e)任选分离分离的5-甲酰基戊酸或其酯。 该方法允许以经济有效的方式有效地生产用于使用单一工艺生产聚酰胺的两种不同中间体,具有良好的选择性,少量的废料。 该方法非常适合于使用由戊内酯获得的异戊烯酸混合物,并可用于使用单一工艺生产可再生聚酰胺中间体。
    • 7. 发明申请
    • PROCESS FOR THE ISOLATION OF LEVULINIC ACID
    • 分离胆酸的方法
    • WO2014087013A1
    • 2014-06-12
    • PCT/EP2013/075959
    • 2013-12-09
    • DSM IP ASSETS B.V.
    • RIJKE, DE, ArieHANGX, Gerardus Wilhelmus AdrianusPARTON, Rudy Francois Maria JozefENGENDAHL, Barthel
    • C07D307/58B01D3/00C07C51/09
    • C07D307/58B01D3/009C07C51/09C07C51/44C07C51/487Y02P20/127C07C59/185
    • The invention provides a process for the isolation of levulinic acid from a composition comprising levulinic acid and optionally a compound having a boiling temperature of less than 245°C said process comprising: subjecting said composition to distillation and recovering a distillation residue comprising at least 1 wt% angelica lactone; subjecting said distillation residue to a hydration reaction under conditions of temperature and time and in the presence of water and optionally an acid catalyst to produce levulinic acid or to increase the amount of levulinic acid in said distillation residue; and optionally recovering said levulinic acid. The process is suitable for isolating preparing levulinic acid from compositions made by acid hydrolysis of a Iignocellulosic biomass, and also from compositions be made by acid hydrolysis of sugar such as glucose and fructose. The invention also provides the use of reactive distillation for the isolation of levulinic acid from a composition comprising levulinic acid and optionally a compound having a boiling temperature of less than 245°C.
    • 本发明提供了从包含乙酰丙酸和任选的沸点低于245℃的化合物的组合物中分离乙酰丙酸的方法,所述方法包括:使所述组合物蒸馏并回收包含至少1重量% 当归内酯; 在温度和时间的条件下,在水和任选的酸催化剂的存在下,使所述蒸馏残余物进行水合反应以产生乙酰丙酸或增加所述蒸馏残余物中的乙酰丙酸的量; 并任选地回收所述乙酰丙酸。 该方法适用于从通过酸性水解纤维素生物质制备的组合物中分离制备乙酰丙酸,并且还可以通过糖如葡萄糖和果糖的酸水解制备组合物。 本发明还提供反应蒸馏用于从包含乙酰丙酸和任选的沸点温度低于245℃的化合物的组合物中分离乙酰丙酸的用途。
    • 10. 发明申请
    • PROCESS FOR THE ISOLATION OF LEVULINIC ACID AND FORMIC ACID
    • 分离酸性和酸性的方法
    • WO2014087015A1
    • 2014-06-12
    • PCT/EP2013/075961
    • 2013-12-09
    • DSM IP ASSETS B.V.
    • PARTON, Rudy Francois Maria Jozef
    • C07C51/42C07C51/44C07C51/47C07C51/48C07C59/185C07C53/02
    • C07C51/47B01D3/40C07C51/42C07C51/44C07C51/48C07C59/185C07C53/02
    • The invention provides a process for the isolation of levulinic acid and formic acid from a composition comprising formic acid and levulinic acid, said process comprising a solid-liquid separation step, a vapor removal step, and a solvent-solvent extraction step, wherein a vapor condensate vapor and/or an aqueous phase from the solvent extraction is used to wash the solid fraction. Washing with vapor condensate results in higher levulinic acid yields (higher levulinic acid recovery) as compared to washing with normal water. Washing with aqueous phase results in a less compressible filter cake. Washing first with aqueous phase and subsequently with condensate results in even higher levulinic acid yields. The process is suitable for isolating levulinic acid and formic acid from compositions made by acid hydrolysis of a lignocellulosic biomass, and also from compositions made by acid hydrolysis of sugars such as glucose and fructose.
    • 本发明提供从包含甲酸和乙酰丙酸的组合物中分离乙酰丙酸和甲酸的方法,所述方法包括固液分离步骤,蒸气去除步骤和溶剂 - 溶剂萃取步骤,其中蒸气 冷凝物蒸气和/或来自溶剂萃取的水相用于洗涤固体部分。 与正常水洗涤相比,用蒸气冷凝物洗涤导致更高的乙酰丙酸产量(更高的乙酰丙酸回收率)。 用水相洗涤导致较不压缩的滤饼。 首先用水相洗涤,随后用冷凝液洗脱得到甚至更高的乙酰丙酸产率。 该方法适合于通过木质纤维素生物质的酸水解制备的组合物以及由糖如葡萄糖和果糖的酸水解制备的组合物分离乙酰丙酸和甲酸。