Alkyl-Demethylation Processes and Catalyst Compositions Therefor

    公开(公告)号:US20230021410A1

    公开(公告)日:2023-01-26

    申请号:US17781086

    申请日:2020-11-16

    Abstract: Catalyst compositions to perform selective alkyl-demethylation of C2+-hydrocarbyl-substituted aromatic hydrocarbon may exhibit a hydrogen chemisorption of at least 15% and comprise an oxide support material selected from the group consisting of an alkaline earth metal oxide, silica, a composite of an alkaline earth metal oxide and Al2O3, a composite of ZnO and Al2O3, a lanthanide oxide, a composite of a lanthanide oxide and Al2O3, and combinations and mixtures of two or more thereof; and a transition metal element dispersed upon the oxide support material. Alkyl-demethylation processes of a C6+ aromatic hydrocarbon-containing stream comprising C2+-hydrocarbyl-substituted aromatic hydrocarbons may comprise contacting the catalyst compositions in an alkyl-demethylation zone under alkyl-demethylation conditions to form an alkyl-demethylated aromatic hydrocarbon as an effluent exiting the alkyl-demethylation zone.

    Activation of Dehydrogenation Catalysts
    6.
    发明申请
    Activation of Dehydrogenation Catalysts 有权
    脱氢催化剂的活化

    公开(公告)号:US20160115095A1

    公开(公告)日:2016-04-28

    申请号:US14878753

    申请日:2015-10-08

    Abstract: In a process for dehydrogenating cyclohexylbenzene and/or alkyl-substituted cyclohexylbenzene compounds, a dehydrogenation catalyst comprising at least one Group 10 metal compound on a support is heated in the presence of hydrogen from a first temperature from 0° C. to 200° C. to a second, higher temperature from 60° C. to 500° C. at a ramp rate no more than 100° C./hour. The dehydrogenation catalyst is contacted with hydrogen at the second temperature for a time from 3 to 300 hours to produce an activated dehydrogenation catalyst. A feed comprising cyclohexylbenzene and/or an alkyl-substituted cyclohexylbenzene compound is then contacted with hydrogen in the presence of the activated dehydrogenation catalyst under conditions effective to produce a dehydrogenation reaction product comprising biphenyl and/or an alkyl-substituted biphenyl compound.

    Abstract translation: 在环己基苯和/或烷基取代的环己基苯化合物脱氢的方法中,在载体上包含至少一种第10族金属化合物的脱氢催化剂在0℃至200℃的第一温度下在氢气存在下加热。 到第二个更高的温度,从60℃到500℃,升温速率不超过100℃/小时。 脱氢催化剂在第二温度下与氢气接触3至300小时,以产生活化脱氢催化剂。 然后在有效产生包含联苯和/或烷基取代的联苯化合物的脱氢反应产物的条件下,在活化的脱氢催化剂存在下,将包含环己基苯和/或烷基取代的环己基苯化合物的进料与氢气接触。

    Process for Preparing Dialkylbiphenyl Isomer Mixtures
    7.
    发明申请
    Process for Preparing Dialkylbiphenyl Isomer Mixtures 有权
    制备二烷基联苯异构体混合物的方法

    公开(公告)号:US20150361011A1

    公开(公告)日:2015-12-17

    申请号:US14723546

    申请日:2015-05-28

    Abstract: In a process for producing dialkylbiphenyl compounds, a feed comprising substituted cyclohexylbenzene isomers having the formula (I): wherein each of R1 and R2 is an alkyl group and wherein the feed comprises m % by weight of isomers in which R1 is in the 2-position, based on the total weight of substituted cyclohexylbenzene isomers in the feed; is transalkylated with a compound of formula (II): to produce a transalkylation product comprising substituted cyclohexylbenzene isomers having the formula (I) and including n % by weight of isomers in which R1 is in the 2-position, based on the total weight of substituted cyclohexylbenzene isomers in the transalkylation product, wherein n

    Abstract translation: 在制备二烷基联苯化合物的方法中,包含具有式(I)的取代的环己基苯异构体的进料:其中R1和R2各自为烷基,并且其中所述进料包含m%(重量)其中R 1为2- 基于进料中取代的环己基苯异构体的总重量; 与式(II)化合物进行烷基转移:产生包含具有式(I)的取代的环己基苯异构体的烷基转移产物,并且包括n重量%的R1在2-位的异构体,基于 在烷基转移产物中的取代的环己基苯异构体,其中n

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