MONITORING OF THE STOICHIOMETRIC RATIO IN THE REACTION OF NITROAROMATICS WITH HYDROGEN
    32.
    发明申请
    MONITORING OF THE STOICHIOMETRIC RATIO IN THE REACTION OF NITROAROMATICS WITH HYDROGEN 有权
    在氢化反应中监测硝基比例的测定

    公开(公告)号:US20130211141A1

    公开(公告)日:2013-08-15

    申请号:US13759466

    申请日:2013-02-05

    CPC classification number: C07C209/36 C07C211/47 C07C211/50

    Abstract: The present invention relates to a continuous process for preparing at least one aromatic amine by hydrogenation of at least one nitroaromatic by means of hydrogen, where a liquid phase comprising at least the aromatic amine and a gas phase comprising at least hydrogen are present, in the presence of a catalyst suspended in the liquid phase at a temperature of from 50 to 250° C. and a pressure of from 5 to 50 bar, wherein the pressure in the reactor is kept essentially constant by continuous adaptation of the amount of hydrogen fed to the reactor, the total amount of hydrogen fed to the reactor is monitored and the introduction of the at least one nitroaromatic is interrupted if the hydrogen uptake in the reactor is not at least 50 mol % of the amount of hydrogen required for stoichiometric reaction of the at least one nitroaromatic to form the at least one aromatic amine.

    Abstract translation: 本发明涉及通过氢气至少一种硝基芳族化合物来制备至少一种芳族胺的连续方法,其中至少包含芳族胺的液相和至少包含氢的气相存在于 在50至250℃的温度和5至50巴的压力下悬浮在液相中的催化剂的存在,其中反应器中的压力通过连续适应供给到 监测反应器中进料到反应器中的氢气总量,如果反应器中的氢气吸收量不是化学计量反应所需的氢量的至少50摩尔%,则至少一种硝基芳族化合物的引入被中断 至少一种硝基芳族化合物以形成所述至少一种芳族胺。

    Process for preparing (meth)acrolein by heterogeneously catalyzed gas phase partial oxidation
    34.
    发明授权
    Process for preparing (meth)acrolein by heterogeneously catalyzed gas phase partial oxidation 失效
    通过非均相催化气相部分氧化制备(甲基)丙烯醛的方法

    公开(公告)号:US08399711B2

    公开(公告)日:2013-03-19

    申请号:US12954770

    申请日:2010-11-26

    Abstract: A process for preparing (meth)acrolein by heterogeneously catalyzed gas phase partial oxidation of a precursor compound, in which the reaction gas mixture which comprises at least 3% by volume of precursor compound is passed through a fresh fixed catalyst bed whose active material is a multielement oxide which comprises the elements Mo, Fe and Bi and at least one of the elements Ni and Co, and the fixed catalyst bed is loaded with at least 40 l (STP)/l·h of precursor compound, and the precursor compound is converted to an extent of at least 90 mol %, wherein, over the first 8000 operating hours, during X=10 to 500 operating hours, the highest temperature of the reaction gas mixture in the fixed catalyst bed is 400 to 450° C. and, during the remaining 8000−X operating hours, is 300 to

    Abstract translation: 通过前体化合物的非均相催化气相部分氧化制备(甲基)丙烯醛的方法,其中将包含至少3体积%的前体化合物的反应气体混合物通过新鲜的固定催化剂床,活性材料为 包含元素Mo,Fe和Bi以及元素Ni和Co中的至少一种和固定催化剂床的多元素氧化物装载至少40μl(STP)/ l·h的前体化合物,前体化合物是 转化为至少90摩尔%的程度,其中,在第一个8000个工作小时内,在X = 10至500个操作小时期间,固定催化剂床中的反应气体混合物的最高温度为400至450℃, 在剩余的8000-X工作时间内,为300至<400℃,并且在X = 10至500个工作小时的时间内,平均有机前体化合物的固定催化剂床的负载大于 8000-X营业时间。

    PROCESS FOR PREPARING (METH)ACROLEIN BY HETEROGENEOUSLY CATALYZED GAS PHASE PARTIAL OXIDATION
    36.
    发明申请
    PROCESS FOR PREPARING (METH)ACROLEIN BY HETEROGENEOUSLY CATALYZED GAS PHASE PARTIAL OXIDATION 失效
    通过异源催化气相部分氧化制备(甲基)丙烯酸的方法

    公开(公告)号:US20110130596A1

    公开(公告)日:2011-06-02

    申请号:US12954770

    申请日:2010-11-26

    Abstract: A process for preparing (meth)acrolein by heterogeneously catalyzed gas phase partial oxidation of a precursor compound, in which the reaction gas mixture which comprises at least 3% by volume of precursor compound is passed through a fresh fixed catalyst bed whose active material is a multielement oxide which comprises the elements Mo, Fe and Bi and at least one of the elements Ni and Co, and the fixed catalyst bed is loaded with at least 40 l (STP)/l·h of precursor compound, and the precursor compound is converted to an extent of at least 90 mol %, wherein, over the first 8000 operating hours, during X=10 to 500 operating hours, the highest temperature of the reaction gas mixture in the fixed catalyst bed is 400 to 450° C. and, during the remaining 8000−X operating hours, is 300 to

    Abstract translation: 通过前体化合物的非均相催化气相部分氧化制备(甲基)丙烯醛的方法,其中将包含至少3体积%的前体化合物的反应气体混合物通过新鲜的固定催化剂床,活性材料为 包含元素Mo,Fe和Bi以及元素Ni和Co中的至少一种和固定催化剂床的多元素氧化物装载至少40μl(STP)/ l·h的前体化合物,前体化合物是 转化为至少90摩尔%的程度,其中,在第一个8000个工作小时内,在X = 10至500个操作小时期间,固定催化剂床中的反应气体混合物的最高温度为400至450℃, 在剩余的8000-X工作时间内,为300至<400℃,并且在X = 10至500个工作小时的时间内,平均有机前体化合物的固定催化剂床的负载大于 8000-X营业时间。

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