PROCESS FOR SIMULTANEOUSLY PREPARING 6-AMINOCAPRONITRILE AND HEXAMETHYLENE DIAMINE
    2.
    发明申请
    PROCESS FOR SIMULTANEOUSLY PREPARING 6-AMINOCAPRONITRILE AND HEXAMETHYLENE DIAMINE 审中-公开
    操作法,6-氨基己腈和己二胺同时生产

    公开(公告)号:WO1998011051A1

    公开(公告)日:1998-03-19

    申请号:PCT/EP1997004542

    申请日:1997-08-21

    CPC classification number: C07C209/48 C07C253/30

    Abstract: The invention concerns a process for simultaneously preparing 6-aminocapronitrile and hexamethylene diamine proceeding from a mixture which contains a phosphorated compound and substantially adipodinitrile and is obtained by reacting butadiene with hydrocyanic acid in the presence of a catalyst containing a phosphorated compound. The process is characterized in that: (1) the portion by weight of a phosphorated compound, calculated as phosphorus, in the mixture is reduced; (2) the resultant mixture is partially hydrogenated in the presence of a catalyst in order to form an alpha-, omega aminonitrile; and (3) 6-aminocapronitrile and hexamethylene diamine are separated from the mixture.

    Abstract translation: 为6-氨基己腈和六亚甲基二胺的同时制备从混合物含有含磷化合物和基本上己二腈,并通过与氢氰酸在含含磷化合物的催化剂的存在下,其特征在于,一个丁二烯的反应而得到的起始(1的方法 )将得到的混合物氢化,在催化剂的存在下,以形成从所述混合物中分离(重量)的含磷化合物,如磷计算的比例的α,ω-二氨基腈部分和(3)6-氨基己腈和六亚甲基二胺,在混合物中降低,并且(2)。

    PROCESS FOR PRODUCING AMINES AND AMINO NITRILES
    4.
    发明申请
    PROCESS FOR PRODUCING AMINES AND AMINO NITRILES 审中-公开
    用于生产胺和氨基腈

    公开(公告)号:WO1998004515A1

    公开(公告)日:1998-02-05

    申请号:PCT/EP1997004100

    申请日:1997-07-29

    CPC classification number: C07C209/48 C07C209/52 C07C211/12 C07C211/35

    Abstract: Herstellung von NH2-Gruppen enthaltenden Verbindungen durch Hydrierung von Verbindungen, die mindestens eine ungesättigte Kohlenstoff-Stickstoff-Bindung enthalten, mit Wasserstoff in Gegenwart eines Katalysators bei Temperaturen von nicht unterhalb Raumtemperatur und erhöhtem Wasserstoff-Partialdruck gewünschtenfalls in Gegenwart eines Lösungsmittels, indem man (a) als Katalysator einen Cobalt- und/oder Eisen-haltigen Katalysator einsetzt, und (b) nach Absinken des Umsatzes, bezogen auf die zu hydrierende Verbindung, und/oder der Selektivität, bezogen auf das gewünschte Produkt, unter einen definierten Wert oder nach Ansteigen der Menge eines unerwünschten Nebenproduktes über einen definierten Wert, die Hydrierung unterbricht, indem man die Zufuhr der zu hydrierenden Verbindungen sowie gewünschtenfalls vorhandenem Lösungsmittel stoppt, (c) den Katalysator bei einer Temperatur im Bereich von 150 bis 400 DEG C mit Wasserstoff behandelt, wobei man dem Wasserstoffdruck im Bereich von 0,1 bis 30 MPa und die Behandlungszeit im Bereich von 2 bis 48 h wählt, und (d) anschliessend die Hydrierung der mindestens eine ungesättigte Kohlenstoff-Stickstoff-Bindung enthaltenden Verbindungen fortsetzt, sowie Regenerierung von Cobalt- und/oder Eisen-haltigen Katalysatoren.

    Abstract translation: 本发明涉及生产由氢化含有与氢的至少一个不饱和碳 - 氮键的化合物在催化剂的温度不低于室温,并在增加氢分压的存在下含NH 2基团的化合物,优选在存在 溶剂中,在其中一个:(a)使用钴和/或含铁催化剂,和(b),所述化合物的转换后待氢化和/或产品的选择性期望低于限定值滴,或后 氢在不期望的副产物超过限定值的数量增加,一个通过停止化合物的供给折断氢化待氢化,并且如果需要清除,任何存在的溶剂中,(c)一种治疗与催化剂 在150之间,以400℃和(d)0.1之间的氢气压力至30MPa,并且选择的2〜48小时的处理时间,和温度一个随后继续被至少一个C的氢化 ompound碳 - 氮键,以及钴和/或含铁催化剂的再生包含不饱和。

    CATALYSTS SUITABLE FOR PREPARING ALIPHATIC ALPHA-, OMEGA-AMINONITRILES BY PARTIAL HYDROGENATION OF ALIPHATIC DINITRILES
    5.
    发明申请
    CATALYSTS SUITABLE FOR PREPARING ALIPHATIC ALPHA-, OMEGA-AMINONITRILES BY PARTIAL HYDROGENATION OF ALIPHATIC DINITRILES 审中-公开
    脂肪族α,ω-二氨基腈由脂族二腈合适的催化剂的部分氢化的制造

    公开(公告)号:WO1998011058A1

    公开(公告)日:1998-03-19

    申请号:PCT/EP1997004547

    申请日:1997-08-21

    CPC classification number: C07C253/30

    Abstract: The invention concerns catalysts suitable for preparing aliphatic alpha-, omega-aminonitriles by partial hydrogenation of aliphatic dinitriles, containing: (a) metallic cobalt, a cobalt compound or their mixtures, the metallic cobalt portion being between 20 and 100 wt % relative to (a); (b) between 10 and 70 wt %, relative to (a), of metallic iron, iron oxide, a further iron compound or their mixtures, the iron oxide portion being between 20 and 100 wt % relative to (b); and (c) between 0 and 1 wt %, relative to (a), of a compound based on an alkali metal, alkaline earth metal or zinc.

    Abstract translation: 对于由脂肪族二腈合适的催化剂的部分氢化制备的脂族α,ω-氨基腈的包括(a)金属钴,钴化合物或它们的混合物,其特征在于,金属钴的基于(a)20至100重量的比例。 - %(重量),(b)10至70重量%,基于金属(a)中铁,铁氧化物,进一步铁化合物或它们的混合物,其中氧化铁基于(b)中20到100重量比例.-% 按重量计,(C)基于(a)的基础上的碱金属,碱土金属或锌的化合物为0〜1重量%。

    PROCESS FOR PRODUCING 2-CYANO-3,3-DIARY ACRYLIC ACID ESTERS
    7.
    发明申请
    PROCESS FOR PRODUCING 2-CYANO-3,3-DIARY ACRYLIC ACID ESTERS 审中-公开
    用于生产2青色-3,3-DIARYLACRYLSÄUREESTERN

    公开(公告)号:WO1996038409A1

    公开(公告)日:1996-12-05

    申请号:PCT/EP1996002238

    申请日:1996-05-24

    CPC classification number: C07C253/30

    Abstract: A process for producing 2-cyano-3,3-diary acrylic acid esters of general formula (I) in which R and R are hydrogen, C1-C12 alkoxy groups or di-(C1-C4 alkyl) amino groups and R is a C4-C18 alkyl group which may be interrupted by oxygen atoms in the ether function, by the reaction of benzophenonimine of general formula (II) with a cyanic acid ester of general formula (III), in which the reaction is conducted at 20 to 60 DEG C and the ammonia released is continuously removed from the reaction mixture with the aid of a stream of gas or by reducing the pressure to 900 to 100mbar.

    Abstract translation: 一种通式(I)中R <2>为氢,C1-C12烷基,C1-C12烷氧基或二 - (C 1 -C <1>和R的2-氰基-3,3-diarylacrylsäureestern的制备方法 氨基-C 4 - 烷基)和R <3>是其可通过在醚功能个氧原子间断的C4-C18烷基,由通式(II)的二苯甲酮亚胺与通式(III)的氰基酯反应,其特征在于 如果反应是在这种情况下,在20下进行到60℃,并且所释放的氨持续地与气体流的帮助下或通过减少从反应混合物中的压力,以900〜100毫巴除去。

    2-CYANOACRYLIC ACID ESTERS
    8.
    发明申请
    2-CYANOACRYLIC ACID ESTERS 审中-公开
    2-氰基丙烯酸酯

    公开(公告)号:WO1996015102A2

    公开(公告)日:1996-05-23

    申请号:PCT/EP1995004312

    申请日:1995-11-03

    Abstract: Described are 2-cyanoacrylic acid esters (I) in which the groups are defined as follows: R and R are hydrogen or a group with an isocyclic or heterocyclic ring system having at least one iso-aromatic or hetero-aromatic nucleus, whereby one of the groups R and R must be different from hydrogen, n is from 2 to 10, X in the case when n = 2 is a group of the formula (II) in which m is from 2 to 8, X in the case when n > 2 is an n-hydric aliphatic or cycloaliphatic polyol group with 3 to 20 C-atoms, whereby the cycloaliphatic polyol group may include 1 to 2 hetero-atoms and the aliphatic polyol group may include up to 8 non-adjacent oxygen atoms, sulphur atoms, imino groups or C1-C4 alkylimino groups in the carbon chain. Compounds of the formula (I) are suitable for use as light-protection agents.

    Abstract translation: 新2-氰基酯(I),其中,所述基团具有以下含义:R t <1>和R <2>是氢或基团具有至少一个异 - 或杂芳族核,R的其中一个<一个异 - 或杂环体系 1>或R <2>必须是不同于氢,N = 2〜10,X为下式基团(II),其中m是对于n = 2 = 2〜8的,X对于n> 2是基团的n的 具有含羟脂族或脂环族多元醇3-20个C原子,其中一个脂环族基团也可以包含由多达8个不相邻的氧原子,硫原子,亚氨基或C 1 -C 4烷基亚氨基可以被中断取代的1至2个杂原子和脂族基团。 化合物(I)被用作光稳定剂。

    IMPROVED METHOD FOR PRODUCING HEXAMETHYLENE DIAMINE
    9.
    发明申请
    IMPROVED METHOD FOR PRODUCING HEXAMETHYLENE DIAMINE 审中-公开
    改进工艺用于生产己二胺

    公开(公告)号:WO2000003972A1

    公开(公告)日:2000-01-27

    申请号:PCT/EP1999004582

    申请日:1999-07-02

    CPC classification number: C07C209/48 C07C211/12

    Abstract: A method for catalytic hydrogenation of adipodinitrile into hexamethylene diamine at a high temperature and high pressure in the presence of catalysts based on elementary iron as a catalytically active constituent and ammonia as a solvent. The invention is characterized in that a) adipodinitrile is hydrogenated at temperatures ranging from 70 to 220 °C and at pressures of 100-400 bars in the presence of catalysts based on elementary iron and ammonia as a solvent to obtain a mixture containing adipodinitrile, 6-aminocapronitrile, hexamethylene diamine and high boilers until the sum of the 6-aminocapronitrile and adipodinitrile concentrations amount to 1-50 wt. % in relation to the ammonia-free hydrogenation mixture; b) ammonia is separated from the hydrogenation product; c) hexamethylene diamine is separated from the remaining mixture; d) 6-aminocapronitrile and adipodinitrile are separated individually or jointly from high boilers and e) 6-aminocapronitrile, adipodinitrile or the mixtures thereof are returned to step a).

    Abstract translation: 一种用于己二腈的催化加氢过程中在升高的温度和升高的压力下在催化剂的存在下根据元素铁作为催化活性组分和氨作为溶剂,其特征在于:a)己二腈在70℃至220℃六亚甲基二胺 氢化和基于元素铁作为催化活性组分和氨作为溶剂的混合物,其包含己二腈,6-氨基己腈,六亚甲基二胺和高沸点直到6-氨基己腈的总和至400巴在催化剂的存在下的100的压力 和的1的己二腈的浓度至50重量%,基于该无氨氢化混合物; b)从该氢化产物氨分离; c)从剩余的混合物中分离六亚甲基二胺; D)6-氨基己腈和己二腈从高沸点单独或一起被分离; 和e)6-氨基己腈,己二腈或它们的混合物到步骤a)引回。

    METHOD FOR PRODUCING POLYALCOHOLS
    10.
    发明申请
    METHOD FOR PRODUCING POLYALCOHOLS 审中-公开
    用于生产多元醇

    公开(公告)号:WO1998028253A1

    公开(公告)日:1998-07-02

    申请号:PCT/EP1997006776

    申请日:1997-12-04

    Abstract: The invention relates to a method for producing polymethylol compounds of formula (I), in which R represents a further methylol group or an alkyl group with between 1 and 22 C atoms or an aryl or alkyl aryl group with between 6 and 22 C atoms, by condensating aldehydes with between 2 and 24 C atoms with formaldehyde, using tertiary amines as catalysts, with a view to obtaining compounds of formula (II), in which R has the meaning assigned to it above. The invention further relates to a process for hydrogenating polymethylol compounds by condensation in stages. For this, a) in a first (reaction) stage, the aldehydes with 2 or more C atoms are reacted with 2 to 8 times the molar quantity of formaldehyde in the presence of a tertiary amine as catalyst; b) in a second (separation) stage, either the reaction mixture is separated into a distillation residue containing primarily the compounds of formula (II) and a destillation flow containing primarily the compounds of unreacted or partly reacted starting materials which is fed back to the first stage, or the reaction mixture of the first stage is separated into an aqueous and an organic phase by means of a phase separation device and the organic phase fed back to the first stage, and c) in a third (post-reaction distillation) stage, the distillation residue of the second stage or the aqueous phase obtained by phase separation during the second stage is subjected to a catalytic and/or heat treatment, the compound of formula (III) which has not been fully methylolized is transformed into the corresponding compound of formula (II) and into the corresponding methylene compound of formula (IV), in which R' represents hydrogen or has the meaning assigned above to R, the reaction mixture obtained in this way is distilled, and the distillation overhead product, which contains a compound of formula (IV) and unreacted formaldehyde, is fed back to the first stage. Thereafter, the still bottom of this distillation process, which essentially contains the compound of formula (II), is hydrogenated in the known manner so as to obtain the corresponding end product of formula (I).

    Abstract translation: 一种用于制备式(I),其中R是一个进一步羟甲基或具有1至22个碳原子或具有碳原子数为6〜22的芳基或芳基的烷基,由具有2〜24的醛的缩合的多羟甲基化合物的方法 通过使用叔胺作为催化剂与甲醛个碳原子,以形成式(II),其中R具有上述含义,并且通过进行冷凝阶段它们的氢化,其中a)在第一(反应)步骤的化合物 具有2个或更多个碳原子的醛与甲醛的2-至8-倍摩尔量的叔胺作为催化剂的存在下,b)反应或者在式I的主要的化合物的反应混合物(在第二(分离)阶段 含II)和贮槽主要由未反应的或部分反应的起始原料,馏出物流被分离,将其再循环到第一级,或 反应混合物从第一级由分离装置成水和有机相,并回收有机相到第一级,以及c)在第三(反应后蒸馏)级的第二级的底部的相位的装置或在第二级分离 通过催化和/或热处理的相分离水相得到的进行,除了通式(III)为式(II)的相应化合物的不完全羟甲基化的化合物和成式(IV)的相应的亚甲基化合物,其中R“是氢 或如上对R所定义,已转让,蒸馏由此获得的反应混合物,并回收该蒸馏的塔顶产物,其含有式(IV)和在所述第一步骤和以已知的方式基本上与未反应的甲醛的化合物 含有式(II)的该底部产物Destilla的化合物 和灰氢化,式(I)的相应的最终产物。

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