Oxidized organic compound manufacturing method
    5.
    发明授权
    Oxidized organic compound manufacturing method 有权
    氧化有机化合物的制造方法

    公开(公告)号:US08962881B2

    公开(公告)日:2015-02-24

    申请号:US13203311

    申请日:2009-03-09

    CPC分类号: C07C51/235

    摘要: The disclosed invention is a method for manufacturing an oxidized organic compound which includes a step of forming an oxidized organic compound, in use of a fixed-bed reactor having a reaction tube packed with an oxide catalyst, by supplying at least one type of organic compound as a reaction feedstock gas and using a molecular oxygen-containing gas to carry out a catalytic gas-phase oxidation reaction; and a step of stopping the catalytic gas-phase oxidation reaction. In the manufacturing method, when stopping the catalytic gas-phase oxidation reaction, the supply of the reaction feedstock gas is stopped, after which an inert gas is supplied to the reactor, then a molecular oxygen-containing gas is supplied, subsequent to which the supply of the molecular oxygen-containing gas to the reactor is stopped.

    摘要翻译: 所公开的发明是一种氧化有机化合物的制造方法,其包括形成氧化有机化合物的步骤,在使用具有填充有氧化物催化剂的反应管的固定床反应器的情况下,通过供给至少一种类型的有机化合物 作为反应原料气体并使用含分子氧的气体进行催化气相氧化反应; 以及停止催化气相氧化反应的步骤。 在制造方法中,停止催化气相氧化反应时,停止供给反应原料气体,之后向反应器供给惰性气体,然后供给含分子氧气体,接着, 停止向反应器供应含分子氧的气体。

    Catalyst and process for production of acrylic acid
    6.
    发明申请
    Catalyst and process for production of acrylic acid 有权
    用于生产丙烯酸的催化剂和方法

    公开(公告)号:US20090043128A1

    公开(公告)日:2009-02-12

    申请号:US12287082

    申请日:2008-10-06

    摘要: An object of the present invention is to provide: a catalyst for production of acrylic acid which is a catalyst usable for production of acrylic acid and is excellent in the catalytic performances such as catalytic activity and in the physical properties such as physical strength of the catalyst itself; and a process for production of acrylic acid using this catalyst. As a means of achieving this object, a catalyst for production of acrylic acid according to the present invention is a catalyst obtained by drying a mixed liquid of starting materials including molybdenum and vanadium as essential components to give a dried material, molding the dried material with a liquid binder, and calcining the resultant molding, with the catalyst being characterized in that an ignition loss ratio of the dried material is from 5 to 40% by mass. A process for production of acrylic acid according to the present invention comprises the step of: subjecting acrolein to a catalytic gas phase oxidation in the presence of a molecular oxygen, with the process being characterized in that the above catalyst for production of acrylic acid according to the present invention is used.

    摘要翻译: 本发明的目的在于提供:丙烯酸的制造用催化剂,其为可用于生产丙烯酸的催化剂,催化性能如催化活性以及催化剂的物理性能如催化剂的物理性能优异 本身; 以及使用该催化剂生产丙烯酸的方法。 作为实现该目的的手段,本发明的丙烯酸的制造用催化剂是通过干燥含有钼和钒的起始材料的混合液作为必要成分而得到的催化剂,得到干燥后的材料, 液体粘合剂,并煅烧所得到的模制品,催化剂的特征在于,干燥材料的灼烧损失率为5〜40质量%。 根据本发明的制备丙烯酸的方法包括以下步骤:在分子氧存在下使丙烯醛进行催化气相氧化,其特征在于上述用于生产丙烯酸的催化剂根据 使用本发明。

    Catalytic gas phase oxidation reaction
    8.
    发明授权
    Catalytic gas phase oxidation reaction 有权
    催化气相氧化反应

    公开(公告)号:US07161044B2

    公开(公告)日:2007-01-09

    申请号:US10958015

    申请日:2004-10-04

    摘要: An object of the present invention is to provide a catalytic gas phase oxidation reaction in which: even under reaction conditions of a higher gas pressure, a higher concentration of the raw material gas and a larger space velocity of a reaction gas, the thermal accumulation at the hot spot portion can be sufficiently suppressed with ease and at low costs, so that the reaction can be continued for a long time while a high yield is maintained. As a means of achieving this object, a catalytic gas phase oxidation reaction according to the present invention is a catalytic gas phase oxidation reaction with molecular oxygen or a molecular-oxygen-containing gas by using a fixed-bed multitubular reactor packed with catalysts; with the catalytic gas phase oxidation reaction being characterized in that: a catalyst-packed layer of each reaction tube of the reactor is divided into at least two reaction zones in a tubular axial direction; and the packing of the catalysts is such that the occupation volumes of the catalysts differ between at least two of the reaction zones and that an inert substance molding is mixed in at least one of the reaction zones.

    摘要翻译: 本发明的目的是提供一种催化气相氧化反应,其中即使在较高气体压力,较高浓度的原料气体和较大的反应气体的空间速度的反应条件下,热累积在 可以容易地且低成本地充分地抑制热点部分,使得反应可以长时间持续,同时保持高产率。 作为实现该目的的手段,本发明的催化气相氧化反应是使用填充有催化剂的固定床多管反应器进行与分子氧或含分子氧气体的催化气相氧化反应, 催化气相氧化反应的特征在于:将反应器的每个反应管的催化剂填充层分成至少两个沿管轴方向的反应区; 并且催化剂的填充使得催化剂的占有体积在至少两个反应区之间不同,并且惰性物质模制品在至少一个反应区中混合。

    Support for gas-phase oxidation catalyst and process for its production, gas-phase oxidation catalyst,and process for producing acrylic acid
    9.
    发明申请
    Support for gas-phase oxidation catalyst and process for its production, gas-phase oxidation catalyst,and process for producing acrylic acid 有权
    支持气相氧化催化剂及其制备方法,气相氧化催化剂及丙烯酸生产工艺

    公开(公告)号:US20060234861A1

    公开(公告)日:2006-10-19

    申请号:US11405588

    申请日:2006-04-18

    IPC分类号: B01J21/00

    摘要: A support for a gas-phase oxidation catalyst, the support including a solid acid, of which acid strength (H0) meets an inequality: −5.6≦H0≦1.5; a gas-phase oxidation catalyst including the above support and a complex oxide containing molybdenum and vanadium as essential components, the complex oxide being supported on the support; a process for producing acrylic acid by gas-phase catalytic oxidation of acrolein with molecular oxygen, the process including carrying out the gas-phase catalytic oxidation in a presence of the above gas-phase oxidation catalyst; and a process for producing the above support, the process including controlling an acid strength (H0) of a solid acid so as to meet an inequality: −5.6≦H0≦1.5 by adjusting a calcination temperature in a preparation of the solid acid contained in the support.

    摘要翻译: 对于气相氧化催化剂的载体,其包含固体酸的载体,其酸强度(H 0 O 3)满足不等式:-5.6 <= H <0 < = 1.5; 包含上述载体的气相氧化催化剂和含有钼和钒作为必要组分的复合氧化物,复合氧化物负载在载体上; 通过气相催化氧化丙烯醛与分子氧生产丙烯酸的方法,该方法包括在上述气相氧化催化剂存在下进行气相催化氧化; 以及制备上述载体的方法,所述方法包括控制固体酸的酸强度(H 2 O 3)以满足不等式:-5.6 <= H <0 通过调节包含在载体中的固体酸的制备中的煅烧温度来确定。

    Catalytic gas phase oxidation process

    公开(公告)号:US07045657B2

    公开(公告)日:2006-05-16

    申请号:US10387244

    申请日:2003-03-12

    IPC分类号: C07C51/235 C07C51/16

    摘要: The object of the present invention is to provide a process in which, when the unsaturated carboxylic acid is produced, or when the unsaturated aldehyde and/or the unsaturated carboxylic acid are produced by carrying out the catalytic gas phase oxidation reaction by using the fixed-bed multitubular reactor which is packed with the molybdenum-containing catalyst, the reaction can be continued for a long time while a high yield is maintained, regardless of where the hot spot portion occurs and also even if the concentration of the raw gas is high. To solve this object, the present invention production process for an unsaturated carboxylic acid is characterized in: a particulate catalysts including, as catalytic components, an oxide and/or a complex oxide including Mo and V, or Mo, Fe and Bi as essential components, and having a hole are used; and a catalyst-packed layer of each reaction tube of the fixed-bed multitubular reactor is divided into at least two reaction zones in a tubular axial direction, wherein the packing of the catalysts is such that the diameters of the holes of the catalysts differ between at least two of the reaction zones.