Desulfation method for SCR catalyst

    公开(公告)号:US11097264B2

    公开(公告)日:2021-08-24

    申请号:US16142451

    申请日:2018-09-26

    Abstract: The present invention provides methods for low temperature desulfating sulfur-poisoned SCR catalysts, and emission control systems adapted to apply such desulfating methods, in order to regenerate catalytic NOx conversion activity. The methods are adapted for treating an SCR catalyst to desorb sulfur from the surface of the SCR catalyst and increase NOx conversion activity of the SCR catalyst, the treating step including treating the SCR catalyst with a gaseous stream comprising a reductant for a first treatment time period and at a first treatment temperature, wherein the first treatment temperature is about 350° C. or less, followed by a second treatment time period and a second treatment temperature higher than the first treatment temperature, wherein the molar ratio of reductant to NOx during the treating step is about 1.05:1 or higher.

    Method for preparing diamino-dicyclohexyl methane
    24.
    发明授权
    Method for preparing diamino-dicyclohexyl methane 有权
    二氨基二环己基甲烷的制备方法

    公开(公告)号:US09580380B2

    公开(公告)日:2017-02-28

    申请号:US14761890

    申请日:2013-11-22

    Abstract: Disclosed is a method for preparing diamino-dicyclohexyl methane (H12MDA) by hydrogenation of diamino-diphenyl methane (MDA). In the process, 4,4′-MDA used as the starting material is firstly hydrogenated to prepare 4,4′-H12MDA. When the activity of the catalyst is reduced, the feed is switched from 4,4′-MDA to the mixture of 2,4′-MDA and 4,4′-MDA, and then when the conversion is stabilized, the feed is switched to 4,4′-MDA again. The deactivated catalyst is activated on line by switching the feed to the mixture of 2,4′-MDA and 4,4′-MDA. 4,4′-H12MDA having the trans-trans isomer content of 16˜24 wt % is produced, and the mixture of 2,4′-H12MDA and 4,4′-H12MDA is also produced, wherein the content of 2,4′-H12MDA in the mixture is 4˜15 wt %.

    Abstract translation: 公开了通过二氨基二苯基甲烷(MDA)的氢化制备二氨基二环己基甲烷(H12MDA)的方法。 在此过程中,首先氢化4,4'-MDA作为原料,制备4,4'-H12MDA。 当催化剂的活性降低时,进料从4,4'-MDA转变为2,4'-MDA和4,4'-MDA的混合物,然后当转化稳定时,进料被切换 至4,4'-MDA。 通过将进料转化为2,4'-MDA和4,4'-MDA的混合物,使活化的催化剂在线活化。 制备反式异构体含量为16〜24重量%的4,4'-H12MDA,并且还生产2,4'-H12MDA和4,4'-H12MDA的混合物,其中2,4 混合物中的-H12MDA为4〜15重量%。

    Regeneration and stabilization of dehydrogenation catalyst
    29.
    发明授权
    Regeneration and stabilization of dehydrogenation catalyst 失效
    脱氢催化剂的再生和稳定化

    公开(公告)号:US5695724A

    公开(公告)日:1997-12-09

    申请号:US557088

    申请日:1995-12-05

    Abstract: A method and associated apparatus for regenerating and/or stabilizing catalyst used in dehydrogenation of alkylaromatic hydrocarbons is disclosed. The alkylaromatic hydrocarbon (1) and steam (2) are combined to form feedstream (3) and pass into reactor (50). The ensuing product stream (4) is reheated in heater (52) to restore the heat lost and passed as partially converted reactant stream (5) into second reactor (54) and leaves as stream (6) comprising the dehydrogen product. Restoration and/or stabilization of catalyst is accomplished by an alkali metal compound which is fed into feedstream (2) and/or product stream (5) via supply means (46 and 66), respectively. The amount of alkali metal compound entering the reactor(s) is monitored by means (42 and 62) which may in turn be coupled to activating means (44 and 64) to signal and activate the supply means. This method and apparatus permit the restoration and/or stabilization of the catalyst to be performed without interrupting the dehydrogenation reaction.

    Abstract translation: PCT No.PCT / US94 / 07474 Sec。 371 1995年12月5日第 102(e)日期1995年12月5日PCT提交1994年6月30日PCT公布。 第WO95 / 01947号公报 公开了一种用于烷基芳族烃脱氢中用于再生和/或稳定催化剂的方法和相关装置,1995年1月19日。 将烷基芳族烃(1)和蒸汽(2)组合以形成原料流(3)并进入反应器(50)。 随后的产物流(4)在加热器(52)中再加热以恢复热量的损失,并且作为部分转化的反应物流(5)进入第二反应器(54)并作为包含脱氢产物的流(6)离开。 催化剂的还原和/或稳定通过分别经由供给装置(46和66)进料到进料流(2)和/或产物流(5)中的碱金属化合物来实现。 通过装置(42和62)监测进入反应器的碱金属化合物的量,该装置又可耦合到激活装置(44和64)以发出信号并激活供应装置。 该方法和装置允许催化剂的恢复和/或稳定化而不中断脱氢反应。

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