Reactor for producing a nitrile compound and method for operating the reactor
    3.
    发明申请
    Reactor for producing a nitrile compound and method for operating the reactor 审中-公开
    用于生产腈化合物的反应器和操作反应器的方法

    公开(公告)号:US20040005254A1

    公开(公告)日:2004-01-08

    申请号:US10326056

    申请日:2002-12-23

    摘要: A reactor for producing a nitrile compound from a carbon ring or heterocyclic compound having organic substituents by a gas phase reaction using a fluidized catalyst bed with ammonia and a gas containing oxygen. In a cylindrical fluidized catalyst bed having a diameter of 2.0 meters or greater, partial vaporization-type cooling tubes (the cooling medium is partially vaporized in the tubes) and complete vaporization-type cooling tubes (the cooling medium is completely vaporized in the cooling tubes) are disposed in a specific arrangement. Water containing ionic SiO2 in 0.1 ppm or smaller and having an electric conductivity of 5 nullS/cm or smaller is used as the cooling medium for the complete vaporization-type cooling tubes. The temperature of the reaction is easily stabilized and uniform distribution of temperature is obtained in the fluidized catalyst bed. Stable continuous operation is achieved for a long time in a commercial scale apparatus.

    摘要翻译: 一种反应器,其由具有有机取代基的碳环或杂环化合物通过气相反应使用流化催化剂床与氨和含氧气体制备。 在直径为2.0米或更大的圆柱形流化催化剂床中,部分气化型冷却管(冷却介质在管中部分蒸发)和完全蒸发式冷却管(冷却介质在冷却管中完全汽化 )以特定的布置处理。 使用0.1ppm以下的导电率为5μS/ cm以下的离子性SiO 2的水作为完全蒸发式冷却管的冷却介质。 反应的温度容易稳定,在流化催化剂床中得到均匀的温度分布。 在商业规模的设备中长期实现稳定的连续操作。

    Process for producing a polynitrile compound
    4.
    发明申请
    Process for producing a polynitrile compound 有权
    腈化合物的制备方法

    公开(公告)号:US20030114701A1

    公开(公告)日:2003-06-19

    申请号:US10313022

    申请日:2002-12-06

    IPC分类号: C07C253/28 C07D213/70

    CPC分类号: C07C253/28 C07C255/51

    摘要: In a process for producing a polynitrile compound comprising introducing a polysubstituted organic compound (POC) which is a carbon ring or heterocyclic compounds having a plurality of organic substituents into a reactor with ammonia and a gas containing oxygen and ammoxidizing POC in the presence of a catalyst, at least a portion of the unreacted POC and a mononitrile compound of an intermediate product in the reaction gas discharged from the reactor is separated, recovered and recycled to the reactor so that the flow rate of the mononitrile compound at the outlet of the reactor is 2 to 16% by mole of the total flow rate of POC and the mononitrile compound supplied to the reactor. Burning reaction of the side reaction is suppressed and the loss of POC can be decreased without adverse effects on productivity and the polynitrile compound can be obtained at a high yield.

    摘要翻译: 在制备多腈化合物的方法中,包括在催化剂存在下,将具有多个有机取代基的多取代有机化合物(POC)或具有多个有机取代基的杂环化合物引入反应器中,所述反应器具有氨和含氧气和氨氧化POC的气体 ,将从反应器排出的反应气体中的至少一部分未反应的POC和中间产物的单腈化合物分离,回收并再循环至反应器,使得反应器出口处的单腈化合物的流速为 相对于供给到反应器的POC和单腈化合物的总流量为2〜16摩尔%。 抑制副反应的燃烧反应,可以降低POC的损失,而不会对生产率产生不利影响,并且可以以高产率获得腈化合物。

    Method of purifying isophthalonitrile
    5.
    发明申请
    Method of purifying isophthalonitrile 有权
    间苯二腈的纯化方法

    公开(公告)号:US20020035287A1

    公开(公告)日:2002-03-21

    申请号:US09953409

    申请日:2001-09-17

    IPC分类号: C07C253/28 B01D001/00

    CPC分类号: C07C253/34 C07C255/51

    摘要: In a method for separating isophthalonitrile from a gas produced by causing m-xylene to react with ammonia and oxygen-containing gas in the presence of a catalyst, the gas is brought into contact with an organic solvent having a boiling point lower than that of isophthalonitrile; a liquid in which isophthalonitrile is trapped in a trapping step is distilled, to thereby recover isophthalonitrile and the organic solvent from the top of the column and separate at the bottom of the column impurities having boiling points higher than that of isophthalonitrile; and the organic solvent is recovered from the top of the rectification column and liquefied isophthalonitrile of high purity is recovered at the bottom of the column. Thus, loss of isophthalonitrile and plugging of a vacuum-evacuation system caused by isophthalonitrile migrating from a condensation system during distillation under reduced pressure can be prevented, and high-purity isophthalonitrile can be produced at high yield constantly for a long period of time.

    摘要翻译: 在由催化剂存在下使间二甲苯与氨和含氧气体反应而产生的气体的分离方法中,使气体与沸点低于间苯二甲腈的有机溶剂接触 ; 将捕获步骤中间苯二腈的液体蒸馏,从柱顶部回收间苯二腈和有机溶剂,并在柱的底部分离具有高于间苯二腈的沸点的杂质; 从精馏塔顶部回收有机溶剂,在塔底回收高纯度的液体间苯二腈。 因此,可以防止间苯二腈的损失和由减压蒸馏期间由缩合体系迁移的间苯二甲腈引起的真空排气系统的堵塞,能够长时间高产率地高产率地产生高纯度间苯二腈。

    Catalyst for catalytic oxidation use
    6.
    发明授权
    Catalyst for catalytic oxidation use 有权
    用于催化氧化的催化剂

    公开(公告)号:US6133184A

    公开(公告)日:2000-10-17

    申请号:US165134

    申请日:1998-10-02

    摘要: A carrier containing silicon carbide, inorganic bonding component, and at least one oxide selected from the group consisting of a niobium oxide, an antimony oxide, and a tungsten oxide carries at least one oxide selected from the group consisting of a vanadium oxide and a molybdenum oxide as catalytically active component. An inexpensive catalyst for catalytic oxidation use can be thus offered that does not change its properties over a period of time, that boasts stable catalytic activity over a period of time, and that is suitable for, e.g., manufacture of an acid anhydride and a nitrile compound by conducting a catalytic gas-phase oxidation reaction (partial oxidation reaction) on a hydrocarbon.

    摘要翻译: 含有碳化硅,无机结合成分和选自氧化铌,氧化锑和氧化钨中的至少一种氧化物的载体含有至少一种选自氧化钒和钼的氧化物 氧化物作为催化活性成分。 因此可提供廉价的用于催化氧化的催化剂,其在一段时间内不改变其性质,其在一段时间内具有稳定的催化活性,并且适于例如制备酸酐和腈 化合物通过在烃上进行催化气相氧化反应(部分氧化反应)。

    Preparation of aromatic or heteroaromatic nitriles
    7.
    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。

    METHOD FOR PRODUCING PURIFIED PHTHALONITRILE AND METHOD FOR PURIFYING PHTHALONITRILE

    公开(公告)号:US20230111802A1

    公开(公告)日:2023-04-13

    申请号:US17904855

    申请日:2021-02-26

    发明人: Kuniaki MUNEYASU

    IPC分类号: C07C253/28 C07C253/34

    摘要: A method for producing a purified phthalonitrile is described. The method involves reacting ammonia, oxygen, and xylene in the presence of a catalyst to obtain a product gas containing a phthalonitrile and a cyanobenzamide and then contacting the reaction product gas with an organic solvent to obtain a collection liquid. The collection liquid is distilled by a high boiling point fraction-separating column to obtain a gas that contains the phthalonitrile and the organic solvent from the column top, and to obtain a bottom liquid that contains a cyanobenzamide from the column bottom. The bottom liquid has a phthalonitrile content of 90% by mass or less. The bottom liquid is subjected to combustion, while being kept in a liquid state, and the purified phthalonitrile is obtained by removing the organic solvent from the gas that has been obtained from the column top.