Oxidation of Hydrocarbons
    42.
    发明申请
    Oxidation of Hydrocarbons 失效
    碳氢化合物的氧化

    公开(公告)号:US20100234589A1

    公开(公告)日:2010-09-16

    申请号:US12601549

    申请日:2008-07-11

    Abstract: 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 an element of Group 4 of the Periodic Table; Y is O or OH; k is 0, 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 formula (I) and the effluent is treated with an aqueous solution of a base to produce an aqueous phase comprising at least part of the unreacted imide catalyst of formula (I) and an organic phase comprising oxidized hydrocarbon product. The organic phase can then be recovered.

    Abstract translation: 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,或者从原子H,F,Cl,Br和I 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为O或OH; k为0,1或2; 1是0,1或2; m为1至3,R3可为R1列出的任何实体。 接触产生包含氧化烃产物和式(I)的未反应酰亚胺催化剂的流出物,流出物用碱的水溶液处理以产生包含至少部分式(I)的未反应的酰亚胺催化剂的水相, 和包含氧化烃产物的有机相。 然后可以回收有机相。

    Catalytic Deamination for Caprolactam Production
    44.
    发明申请
    Catalytic Deamination for Caprolactam Production 有权
    己内酰胺生产催化脱氨

    公开(公告)号:US20100145003A1

    公开(公告)日:2010-06-10

    申请号:US12527848

    申请日:2008-02-20

    Applicant: John W. Frost

    Inventor: John W. Frost

    CPC classification number: C07D201/00 C07D201/02 C07D201/08 Y02P20/52

    Abstract: Catalytic processes for preparing caprolactam, pipecolinic acid, and their derivatives, from lysine or alpha-amino-epsilon-caprolactam starting materials, and products produced thereby. A process for preparing caprolactam or a derivative thereof, the process comprising contacting a reactant comprising lysine or alpha aminocaprolactam with a catalyst and a gas comprising hydrogen gas, in the presence of a solvent. The catalyst may be provided on a support material, such as a transition metal.

    Abstract translation: 从赖氨酸或α-氨基-ε-己内酰胺起始原料制备己内酰胺,哌可啶酸及其衍生物的催化方法,以及由此产生的产物。 一种制备己内酰胺或其衍生物的方法,该方法包括在溶剂存在下使包含赖氨酸或α-氨基己内酰胺的反应物与催化剂和包含氢气的气体接触。 催化剂可以设置在载体材料如过渡金属上。

    Method for making caprolactam from impure 6-amiocapronitrile
    46.
    发明申请
    Method for making caprolactam from impure 6-amiocapronitrile 失效
    从不纯的6-Amiocap腈制备己内酰胺的方法

    公开(公告)号:US20060211859A1

    公开(公告)日:2006-09-21

    申请号:US11083715

    申请日:2005-03-18

    CPC classification number: C07D223/10

    Abstract: The invention relates to the field of production of lactams from aminonitriles, and in particular to the production of ε-caprolactam by the vapor phase hydrolytic cyclization of 6-aminocapronitrile. A crude liquid caprolactam comprising ε-caprolactarn (CL), 6-aminocapronitrile (ACN) and water obtained from a vapor phase cyclization reaction of ACN is contacted with hydrogen in the presence of a hydrogenation catalyst to convert the ACN in the crude liquid caprolactam to a product comprising hexamethylenediamine (HMD) and hexamethyleneimine (HMI). Tetrahydroazepine (THA) in the crude liquid caprolactam is converted to HMI during this hydrogenation. The HMD and HMI have lower boiling points compared to ACN and thus they are more easily separated from CL in the subsequent distillation operations. Thus a process to make CL from ACN with fewer distillation stages, and with lower pressure drop and lower base temperature, is accomplished.

    Abstract translation: 本发明涉及由氨基腈生产内酰胺的领域,特别涉及通过6-氨基己腈的气相水解环化生产ε-己内酰胺。 包含ε-己内酯(CL),6-氨基己腈(ACN)和由ACN的气相环化反应获得的水的粗液体己内酰胺在氢化催化剂存在下与氢气接触,将粗液体己内酰胺中的ACN转化为 包含六亚甲基二胺(HMD)和六亚甲基亚胺(HMI)的产品。 粗制液体己内酰胺中的四氢吖庚因(THA)在该氢化期间转化为HMI。 与ACN相比,HMD和HMI具有较低的沸点,因此在随后的蒸馏操作中它们更容易与CL分离。 因此,实现了具有较少蒸馏阶段以及较低压降和较低基础温度的来自ACN的CL的方法。

    Method for producing a polymer, using caprolactam
    48.
    发明申请
    Method for producing a polymer, using caprolactam 失效
    使用己内酰胺制造聚合物的方法

    公开(公告)号:US20030135019A1

    公开(公告)日:2003-07-17

    申请号:US10257876

    申请日:2002-10-17

    Abstract: A process for preparing a polymer, which comprises a) reacting a mixture (I) containing 6-aminocapronitrile and water in the presence of a catalyst to obtain a mixture (II) containing caprolactam, ammonia, water, high boilers and low boilers, then b) removing ammonia from mixture (II) to obtain a mixture (III) containing caprolactam, water, high boilers and low boilers, then c) removing all or some of the water from mixture (III) to obtain a mixture (IV) containing caprolactam, high boilers and low boilers and then d) feeding mixture (IV) to a polymerization reaction,and also the polymer obtainable by this process, the use of the polymer for producing fibers, sheetlike structures and moldings, and also fibers, sheetlike structures and moldings obtainable using such a polymer.

    Abstract translation: 一种制备聚合物的方法,其包括a)在催化剂存在下使含有6-氨基己腈和水的混合物(I)反应,得到含有己内酰胺,氨,水,高锅炉和低锅炉的混合物(II) b)从混合物(II)中除去氨以得到含有己内酰胺,水,高锅炉和低锅炉的混合物(III),然后c)从混合物(III)中除去全部或部分水,得到含有 己内酰胺,高锅炉和低锅炉,然后d)将混合物(IV)加入到聚合反应中,以及可通过该方法获得的聚合物,使用聚合物生产纤维,片状结构和模制品,以及纤维,片状结构 以及使用这种聚合物可获得的模制品。

    Method for producing caprolactam from 6-aminocapronitrile
    49.
    发明申请
    Method for producing caprolactam from 6-aminocapronitrile 有权
    从6-氨基己腈生产己内酰胺的方法

    公开(公告)号:US20030125546A1

    公开(公告)日:2003-07-03

    申请号:US10258942

    申请日:2002-10-29

    CPC classification number: C07D201/08 C07D201/16

    Abstract: A process for the preparation of caprolactam is provided, wherein a) a mixture (I) containing 6-aminocapronitrile and water is reacted in the liquid phase, in the presence of a catalyst, to give a mixture (II) containing caprolactam, ammonia, water, high-boiling components and low-boiling components, b) ammonia is then removed from the mixture (II) to give a mixture (III) containing caprolactam, water, high-boiling components and low-boiling components, c) water is then removed from the mixture (III) to give a mixture (IV) containing caprolactam, high-boiling components and low-boiling components, and d) a solid (V) containing caprolactam is then obtained from the mixture (IV) by crystallization, the proportion by weight of caprolactam in the solid (V) being greater than in the mixture (IV).

    Abstract translation: 提供了制备己内酰胺的方法,其中a)含有6-氨基己腈和水的混合物(I)在液相中在催化剂存在下反应,得到含有己内酰胺,氨, 水,高沸点组分和低沸点组分,b)然后从混合物(II)中除去氨,得到含有己内酰胺,水,高沸点组分和低沸点组分的混合物(III),c)水是 然后从混合物(III)中取出,得到含己内酰胺,高沸点成分和低沸点组分的混合物(Ⅳ),然后通过结晶从混合物(Ⅳ)中获得含有己内酰胺的固体(Ⅴ) 固体(V)中己内酰胺的重量比例大于混合物(IV)中的比例。

    Process for the preparation of a mixture of .epsilon.-caprolactam,
6-aminocaproic acid and 6-aminocaproic amide
    50.
    发明授权
    Process for the preparation of a mixture of .epsilon.-caprolactam, 6-aminocaproic acid and 6-aminocaproic amide 失效
    制备ε-己内酰胺,6-氨基己酸和6-氨基己酰胺的混合物的方法

    公开(公告)号:US6011153A

    公开(公告)日:2000-01-04

    申请号:US140896

    申请日:1998-08-21

    CPC classification number: C07D201/12

    Abstract: Process for the preparation of a mixture of .epsilon.-caprolactam, 6-aminocaproic acid and 6-aminocaproic amide by heating an aqueous mixture containing ammonia and oligomers of 6-aminocaproic acid and/or of 6-aminocaproic amide, the aqueous mixture containing 0.5-7 wt. % of equivalent ammonia (calculated as NH.sub.3) and the temperature lying between 280.degree. C. and 330.degree. C., in which by "equivalent ammonia" is meant free ammonia and ammonia present in the form of a terminal amide group of one of the compounds present in the aqueous mixture.

    Abstract translation: 通过加热含有氨和6-氨基己酸和/或6-氨基己酸酰胺的低聚物的含水混合物制备ε-己内酰胺,6-氨基己酸和6-氨基己酰胺的混合物的方法,含0.5- 7重量% 相当于氨的百分比(以NH 3计算)和温度在280℃至330℃之间,其中“等效氨”是指游离氨和氨以其中之一的末端酰胺基团的形式存在 存在于含水混合物中的化合物。

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