FIXED-BED REACTOR AND PROCESS FOR PRODUCING ACRYLIC ACID USING THE REACTOR
    1.
    发明申请
    FIXED-BED REACTOR AND PROCESS FOR PRODUCING ACRYLIC ACID USING THE REACTOR 有权
    固定床反应器和使用反应器生产丙烯酸的方法

    公开(公告)号:US20110178334A1

    公开(公告)日:2011-07-21

    申请号:US13056416

    申请日:2009-09-09

    IPC分类号: C07C57/18 B01J8/00 C22C38/00

    摘要: The fixed-bed reactor of the present invention which solves the above problems is a fixed-bed reactor comprising: a first catalyst layer filled with a first catalyst for producing acrolein from propylene; a second catalyst layer filled with a second catalyst for producing acrylic acid from acrolein; and an inert substance layer provided between the first catalyst layer and the second catalyst layer, and filled with an inert substance of a cylindrical shape having a surrounding wall in which an opening is formed. The process for producing acrylic acid of the present invention is a process for producing acrylic acid comprising the step of producing acrylic acid from propylene by using the fixed-bed reactor of the present invention. According to the present invention, since the inert substance of a cylindrical shape having a surrounding wall in which an opening is formed is used as an inert substance, increase of a pressure loss can be drastically suppressed, degradation of the catalyst due to by-produced high-boiling substances and the like can be suppressed, and further the yield of acrylic acid can be enhanced, as compared with the case of using conventional inert substances. Accordingly, it is possible to produce acrylic acid at a high yield stably for a long period.

    摘要翻译: 解决上述问题的本发明的固定床反应器是一种固定床反应器,包括:填充有由丙烯制备丙烯醛的第一催化剂的第一催化剂层; 填充有由丙烯醛制备丙烯酸的第二催化剂的第二催化剂层; 以及设置在第一催化剂层和第二催化剂层之间的惰性物质层,并且填充有具有形成有开口的周围壁的圆筒形状的惰性物质。 本发明的丙烯酸的制造方法是使用本发明的固定床反应器,由丙烯制造丙烯酸的工序,是丙烯酸的制造方法。 根据本发明,由于使用形成有开口的周围壁的圆筒状的惰性物质作为惰性物质,因此可以显着地抑制压力损失的增加,由于副产物引起的催化剂的劣化 可以抑制高沸点物质等,与使用常规惰性物质的情况相比,可以提高丙烯酸的收率。 因此,可以长期稳定地高产率制备丙烯酸。

    Method for gas-phase catalytic oxidation using a fixed bed reactor
    2.
    发明授权
    Method for gas-phase catalytic oxidation using a fixed bed reactor 有权
    使用固定床反应器进行气相催化氧化的方法

    公开(公告)号:US07884235B2

    公开(公告)日:2011-02-08

    申请号:US11826629

    申请日:2007-07-17

    IPC分类号: C07C53/00

    摘要: The invention provides a method of gas-phase catalytic oxidation, in particular, a production method of (meth)acrylic acid, which enables stable continuous operation of gas-phase catalytic oxidation over a long term, maintaining high yield and suppressing increase in pressure loss. In the method a fixed bed reactor is used, in which a treating agent for removing organic substance and/or carbides, preferably a treating agent having an adsorption capacity of at least 0.05% by mass, as measured by crotonaldehyde as an indicator of organic substance, is disposed on the upstream side of the gas-phase oxidation catalyst layer in respect of the direction of the gas flow. It is desirable that at least a part of the treating agent is exchanged at a frequency of at least once a year.

    摘要翻译: 本发明提供了一种气相催化氧化方法,特别是(甲基)丙烯酸的制备方法,其能够长期保持气相催化氧化的稳定连续运行,保持高产率并抑制压力损失增加 。 在该方法中,使用固定床反应器,其中除去有机物和/或碳化物的处理剂,优选具有至少0.05质量%的吸附能力的处理剂,通过巴豆醛作为有机物质的指示剂 相对于气流方向配置在气相氧化催化剂层的上游侧。 理想的是,至少一部分处理剂以每年至少一次的频率进行交换。

    Process for producing acrolein and acrylic acid
    3.
    发明申请
    Process for producing acrolein and acrylic acid 失效
    制备丙烯醛和丙烯酸的方法

    公开(公告)号:US20100249455A1

    公开(公告)日:2010-09-30

    申请号:US12662123

    申请日:2010-03-31

    IPC分类号: C07C51/25 C07C45/35

    摘要: The invention offers an improvement in a process for start-up in the occasion of producing acrolein and acrylic acid by catalytically oxidizing propylene at vapor phase under high load conditions, the start-up meaning the step of increasing the propylene supply rate (loading) from the non-reacting condition to the prescribed reaction conditions. This process is characterized in that the propylene supply rate is increased in the start-up stage of the reaction until the prescribed composition of starting reactant gas and the flow rate of the starting reactant gas are obtained, while adjusting at least one of the reaction temperature, the composition of the starting reactant gas and flow rate of the starting reactant gas, so as to maintain the propylene conversion at not lower than 90 mol %, the maximum peak temperature of the catalyst layer in each reaction zone at no higher than 450° C., and the sum of each ΔT (maximum peak temperature of a catalyst layer—reaction temperature) at the catalyst layer in each of the reaction zones to be no more than 180° C., respectively. According to this process, the reaction speedily reaches the steady state (standard operating conditions) and a high acrolein and acrylic acid yield is stably achieved from the start of the reaction.

    摘要翻译: 本发明提供了在高负载条件下通过在气相下催化氧化丙烯来生产丙烯醛和丙烯酸的情况下的启动方法的改进,启动意味着将丙烯供应速率(负载)从 对规定的反应条件的非反应条件。 该方法的特征在于,在反应的启动阶段,丙烯供给速率增加,直到获得规定的起始反应气体组成和起始反应气体的流量,同时调节至少一个反应温度 ,起始反应物气体的组成和起始反应气体的流速,以保持丙烯转化率不低于90mol%,各反应区中催化剂层的最高峰值温度不高于450° C,以及每个反应区域中的催化剂层的每个&Dgr; T(催化剂层 - 反应温度的最大峰值温度)的总和分别不超过180℃。 根据该方法,反应快速达到稳定状态(标准操作条件),从反应开始就可以稳定地获得高丙烯醛和丙烯酸的收率。

    Process for producing acrylic acid
    4.
    发明申请
    Process for producing acrylic acid 有权
    丙烯酸生产工艺

    公开(公告)号:US20100249454A1

    公开(公告)日:2010-09-30

    申请号:US12659994

    申请日:2010-03-26

    IPC分类号: C07C51/235

    CPC分类号: C07C51/252 C07C57/04

    摘要: The invention offers an improvement in a process for start-up in the occasion of producing acrylic acid by catalytically oxidizing acrolein at vapor phase under high load conditions, the start-up meaning the step of increasing the acrolein supply rate (loading) from the non-reacting condition to the prescribed reaction conditions. This process is characterized in that the acrolein supply rate is increased in the start-up stage of the reaction until the prescribed composition of starting reactant gas and the flow rate of the starting reactant gas are obtained, while adjusting at least one of the reaction temperature, the composition of the starting reactant gas and the flow rate of the starting reactant gas, so as to maintain the acrolein conversion at not lower than 90 mol %, the maximum peak temperature of the catalyst layer in each reaction zone at no higher than 400° C., and the sum of each ΔT (maximum peak temperature of a catalyst layer-reaction temperature) at the catalyst layer in each of the reaction zones to be no more than 150° C., respectively. According to this process, the reaction speedily reaches the steady state (standard operating conditions) and a high acrylic acid yield is stably achieved from the start of the reaction.

    摘要翻译: 本发明提供了在高负载条件下通过在气相下催化氧化丙烯醛来生产丙烯酸的情况下的启动方法的改进,启动意味着提高丙烯醛供应速率(负载) 反应条件达到规定的反应条件。 该方法的特征在于,在反应开始阶段丙烯醛供应速率增加,直到获得规定的起始反应气体组成和起始反应气体的流量,同时调节至少一个反应温度 ,起始反应气体的组成和起始反应气体的流量,以使丙烯醛的转化率保持在不低于90mol%,催化剂层在每个反应区中的最大峰值温度不高于400℃ ℃,以及每个反应区域中的催化剂层的每个&Dgr; T(催化剂层 - 反应温度的最大峰值温度)的总和分别不超过150℃。 根据该方法,反应快速达到稳定状态(标准操作条件),从反应开始就稳定地得到高丙烯酸收率。

    Composite-oxide catalyst and process for production of acrylic acid using said catalyst
    5.
    发明授权
    Composite-oxide catalyst and process for production of acrylic acid using said catalyst 失效
    复合氧化物催化剂和使用所述催化剂生产丙烯酸的方法

    公开(公告)号:US07429678B2

    公开(公告)日:2008-09-30

    申请号:US10764852

    申请日:2004-01-26

    IPC分类号: C07C51/16 C07C51/235

    摘要: There are disclosed a catalyst and a process for production of acrylic acid using this catalyst, wherein, even under conditions where hot spots are formed, the catalyst is excellent in activity, selectivity, and catalyst life time and displays stable performances for a long time. The catalyst is shown by the following formula (1): MoaVbWcCudAeBfCgOx  (1) (wherein: A is at least one species selected from among cobalt, nickel, iron, lead, and bismuth; B is at least one species selected from among antimony, niobium, and tin; and C is at least one species selected from among silicon, aluminum, titanium, and zirconium; and further, a, b, c, d, e, f, g, and x are atomic ratios of Mo, V, W, Cu, A, B, C, and O respectively; and, in the case of a=12, the following inequalities are satisfied: 2≦b≦15; 0

    摘要翻译: 公开了使用该催化剂的催化剂和丙烯酸的制造方法,其中即使在形成热点的条件下,催化剂的活性,选择性和催化剂寿命也优异,长时间显示出稳定的性能。 催化剂由下式(1)表示:<?in-line-formula description =“In-line Formulas”end =“lead”?> Mo a >>>>> e e O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O (1)<?in-line-formula description =“In-line Formulas”end =“tail”?>(其中:A是选自钴,镍,铁,铅中的至少一种 和铋; B是选自锑,铌和锡中的至少一种; C是选自硅,铝,钛和锆中的至少一种;此外,a,b,c,d, e,f,g和x分别是Mo,V,W,Cu,A,B,C和O的原子比;并且在a = 12的情况下,满足以下不等式:2 <= b <= 15; 0

    Production process for acrylic acid under controlled temperature conditions
    9.
    发明授权
    Production process for acrylic acid under controlled temperature conditions 有权
    在控制温度条件下丙烯酸的生产工艺

    公开(公告)号:US06462232B1

    公开(公告)日:2002-10-08

    申请号:US09365845

    申请日:1999-08-03

    IPC分类号: C07C51235

    CPC分类号: C07C51/252 C07C57/04

    摘要: Provided is a process for producing acrylic acid stably at a high yield over a long period of time by subjecting acrolein or acrolein-containing gas to catalytic vapor phase oxidation. The above process is characterized by controlling the reaction so that the following equations (1) and (2) are satisfied: 1° C.≦T0−T1≦15° C.  (1) T1

    摘要翻译: 本发明提供通过使丙烯醛或含丙烯醛的气体进行催化气相氧化而长时间稳定地制备丙烯酸的方法。 上述方法的特征在于控制反应,使得满足以下等式(1)和(2):其中T0表示催化剂层入口中的丙烯醛或含丙烯醛的气体的温度; T1表示催化剂层的入口部的温度; T2表示催化剂层的出口部的温度。