Preparation of aromatic or heteroaromatic nitriles
    1.
    发明授权
    Preparation of aromatic or heteroaromatic nitriles 失效
    芳香族或杂芳族腈的制备

    公开(公告)号:US5952262A

    公开(公告)日:1999-09-14

    申请号:US723915

    申请日:1996-09-30

    摘要: Preparation of aromatic or heteroaromatic nitrites of the formula I ##STR1## where X is nitrogen or C-R.sup.6 and all of the R substituents represent hydrogen, alkyl, halogen, nitro, amino or similar groups, provided at least one substituent is a cyano or alkylcyano group. The nitrites I are produced by reacting aromatic or heteroaromatic hydrocarbons of the formula II ##STR2## where X is nitrogen or C-R.sup.6, provided at least one substituent is C.sub.1 -C.sub.8 -alkyl, with ammonia and oxygen at 200 to 600.degree. C. under a pressure of 0.1 to 5 bar in the gas phase over a supported catalyst containing 0.5 to 20% by weight of vanadium oxide. The supported catalyst consists of from 2 to 30 particle fractions whose mean diameters differ by from 10 to 80% and the supporting carrier of the catalyst has a bulk density of 0.6 to 1.2 kg/liter.

    摘要翻译: 制备式I的芳族或杂芳族亚硝酸盐,其中X是氮或C-R6,所有R取代基代表氢,烷基,卤素,硝基,氨基或类似基团,提供至少一个取代基是氰基或烷基氰基。 亚硝酸盐I通过使式II的芳族或杂芳族化合物(其中X是氮或C-R 6)提供,其中至少一个取代基是C 1 -C 8 - 烷基,氨和氧在200-600℃的压力下 在含有0.5至20重量%氧化钒的负载型催化剂的气相中为0.1至5巴。 载体催化剂由2至30个颗粒级分组成,其平均直径为10至80%,催化剂的载体载体的堆积密度为0.6至1.2kg /升。

    Process for preparing nitric acid with a concentration in the range from 50 to 77.8% by weight
    3.
    发明授权
    Process for preparing nitric acid with a concentration in the range from 50 to 77.8% by weight 有权
    制备浓度为50-77.8重量%浓度的硝酸的方法

    公开(公告)号:US08765009B2

    公开(公告)日:2014-07-01

    申请号:US12601534

    申请日:2008-07-08

    IPC分类号: C09K3/00

    CPC分类号: C01B21/40 C01B21/262

    摘要: A process for preparing nitric acid by: catalytically oxidizing ammonia, to obtain a gas mixture containing NO and O2; cooling and condensing the gas mixture, thereby further oxidizing NO with O2, to obtain a gas stream containing NO2/N2O4 and an aqueous solution containing nitric acid; and countercurrently absorbing the NO2/N2O4 from the gas stream in an absorber with process water (H2O), to obtain nitric acid and an NOx-containing absorber offgas, wherein the water content of the nitric acid is regulated to a concentration in the range from 50 to 77.8% by weight and the NOx content of the absorber offgas to a concentration in the range from 20 to 500 ppm, by continuously measuring the water content of the process air supplied to the catalytic gas phase oxidation and, as a function of this, adjusting the amount of process water (Q-H2O) fed to the absorber.

    摘要翻译: 一种通过以下方式制备硝酸的方法:催化氧化氨,得到含NO和O2的气体混合物; 冷却并冷凝气体混合物,从而进一步用O 2氧化NO,得到含有NO 2 / N 2 O 4的气流和含有硝酸的水溶液; 并用工艺用水(H 2 O)从吸收器中的气流中逆流吸收NO 2 / N 2 O 4,得到硝酸和含NO x的吸收剂废气,其中将硝酸的含水量调节至 50至77.8重量%,并且通过连续测量供应到催化气相氧化的工艺空气的水含量,吸收器的NOx含量废气至浓度在20至500ppm的范围内,并且作为其功能 ,调节供给到吸收器的工艺用水(Q-H 2 O)的量。

    Method for producing acid chlorides
    4.
    发明授权
    Method for producing acid chlorides 有权
    生产酰氯的方法

    公开(公告)号:US06770783B1

    公开(公告)日:2004-08-03

    申请号:US10070864

    申请日:2002-03-12

    IPC分类号: C07C5158

    CPC分类号: C07C51/64 C07C51/60

    摘要: The invention relates to a method for producing acid chlorides by converting carboxylic acids with carbon oxychlorides or thionyl chloride in the presence of a catalyst adduct of an N,N-disubstituted formamide of general formula (I) and carbon oxychloride or thionyl chloride. In the formula, R1 and R2, independently from one another, mean C1- to C4-alkyl or R1 and R2 together mean a C4- or C5-alkylene chain. According to the inventive method, hydrogen chloride is added during and/or after the conversion.

    摘要翻译: 本发明涉及在通式(I)的N,N-二取代甲酰胺与碳酰氯或亚硫酰氯的催化剂加合物存在下,用碳氧氯化物或亚硫酰氯转化羧酸制备酰氯的方法。 在该式中,R 1和R 2彼此独立地表示C 1至C 4 - 烷基或R 1和R 2一起表示C 4 - 或C 5-亚烷基链。 根据本发明的方法,在转化期间和/或之后加入氯化氢。

    Method for producing o-chloromethyl benzenecarbonyl chlorides
    6.
    发明授权
    Method for producing o-chloromethyl benzenecarbonyl chlorides 失效
    邻苯甲酰氯的制备方法

    公开(公告)号:US06734322B1

    公开(公告)日:2004-05-11

    申请号:US10130826

    申请日:2002-05-23

    IPC分类号: C07C5158

    CPC分类号: C07C51/09 C07C63/04

    摘要: The invention relates to a method for producing o-choromethyl benzenecarbonyl chlorides of formula (I), wherein R1-R4 can be the same or different and stand for hydrogen, C1-C4-alkyl, halogen or trifluoromnethyl, by converting benzocondensed lactones of formula (II), wherein R1-R4 have the aforementioned meaning, with gaseous or liquid phosgene and the dimers or trimers thereof. The inventive method is characterized in that the conversion is carried out in the presence of catalytical amounts of a Lewis acid and catalytical amounts of a phosgenation catalyst

    摘要翻译: 本发明涉及一种制备式(I)的邻氯甲基苯甲酰氯的方法,其中R 1 -R 4可以相同或不同,代表氢,C 1 -C 4 - 烷基,卤素或三氟甲基, 通过用气态或液体光气及其二聚体或三聚体转化其中R 1 -R 4具有上述含义的式(II)的苯并二化内酯。 本发明的方法的特征在于转化在催化量的路易斯酸和催化量的光气化催化剂

    Removal of halides from halide-containing nitrile mixtures
    8.
    发明授权
    Removal of halides from halide-containing nitrile mixtures 失效
    从含卤素腈混合物中除去卤化物

    公开(公告)号:US6153784A

    公开(公告)日:2000-11-28

    申请号:US24457

    申请日:1998-02-17

    摘要: Halides are removed from halide-containing nitrile mixtures by(a) thermally treating the halide-containing nitrile mixture,(b) subsequently adding a base to the thermally treated nitrile mixture and(c) subsequently separating off the base from the nitrile mixture.Amines are prepared by(A) reacting alkyl halides with metal cyanides in an at least two-phase reaction medium in the presence of halide-containing phase-transfer catalysts to give alkanenitriles,(B) separating off the resulting halide-containing alkanenitrile mixture phase and(C) further treating the halide-containing alkanenitrile mixture phase, as described in the stages(a)-(c) removing halides from halide-containing nitrile mixtures and(d) hydrogenating nitrites obtained in stage (c) to give amines, in the presence of suspended or fixed-bed catalysts.

    摘要翻译: 通过(a)热处理含卤素腈混合物,(b)随后向经热处理的腈混合物中加入碱,和(c)随后将腈与腈混合物分离,从卤化物腈混合物中除去卤化物。 胺通过(A)在卤化物相转移催化剂存在下在至少两相反应介质中将烷基卤与金属氰化物反应得到烷腈,(B)将所得的含卤素的烷腈混合物相分离 (C)进一步处理含卤化物的腈腈混合物相,如步骤(a) - (c)所述从卤化物腈混合物中除去卤化物,和(d)氢化阶段(c)中得到的亚硝酸盐,得到胺, 在悬浮或固定床催化剂存在下。