Process for making phenol and/or cyclohexanone
    32.
    发明授权
    Process for making phenol and/or cyclohexanone 有权
    制备苯酚和/或环己酮的方法

    公开(公告)号:US09546121B2

    公开(公告)日:2017-01-17

    申请号:US15031759

    申请日:2014-10-17

    Abstract: A process for making phenol and/or cyclohexanone comprises: (A) oxidizing a cyclohexylbenzene feed to obtain an oxidation product comprising cyclohexylbenzene, cyclohexyl-1-phenyl-1-hydroperoxide and phenol; (B) separating at least a portion of the oxidation product to obtain a first fraction comprising cyclohexyl-1-phenyl-1-hydroperoxide and a second fraction comprising cyclohexylbenzene and phenol; (C) removing at least a portion of the phenol from at least a portion of the second fraction to obtain a third fraction; (D) recycling at least a portion of the cyclohexylbenzene in the third fraction to the oxidizing step (A); and (E) contacting at least a portion of the cyclohexyl-1-phenyl-1-hydroperoxide in the first fraction with an acid catalyst in a cleavage reactor under cleavage conditions to obtain a cleavage product comprising phenol and cyclohexanone.

    Abstract translation: 制备苯酚和/或环己酮的方法包括:(A)氧化环己基苯进料以获得包含环己基苯,环己基-1-苯基-1-氢过氧化物和苯酚的氧化产物; (B)分离至少一部分氧化产物以获得包含环己基-1-苯基-1-氢过氧化物的第一级分和包含环己基苯和苯酚的第二级分; (C)从第二级分的至少一部分除去至少一部分苯酚以获得第三级分; (D)将第三馏分中的至少一部分环己基苯回收至氧化步骤(A); 和(E)在裂解反应器中在裂解条件下使第一馏分中的环己基-1-苯基-1-氢过氧化物的至少一部分与酸催化剂接触,得到包含苯酚和环己酮的裂解产物。

    Activation of Dehydrogenation Catalysts
    36.
    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 Producing Phenol and/or Cyclohexanone from Cyclohexylbenzene
    37.
    发明申请
    Process for Producing Phenol and/or Cyclohexanone from Cyclohexylbenzene 有权
    从环己基苯生产苯酚和/或环己酮的方法

    公开(公告)号:US20150218075A1

    公开(公告)日:2015-08-06

    申请号:US14422444

    申请日:2013-09-12

    Abstract: In a process for producing phenol and/or cyclohexanone, cyclohexylbenzene is contacted with an oxygen-containing gas to produce an oxidation effluent containing cyclohexylbenzene hydroperoxide. At least a portion of the cyclohexylbenzene hydroperoxide is then contacted with a cleavage catalyst to produce a cleavage effluent containing phenol and cyclohexanone and by-products including phenylcyclohexanol. The cleavage effluent or a neutralized product thereof also comprises at least one compound comprising an atom not being carbon, hydrogen or oxygen, which is separated from the cleavage effluent and/or the neutralized product thereof to leave a cleavage fraction lean in the compound comprising an atom not being carbon, hydrogen or oxygen and containing at least a portion of the phenylcyclohexanol. At least a portion of the phenylcyclohexanol is then contacted with a dehydration catalyst comprising a molecular sieve of the MCM-22 type to convert at least a portion of the phenylcyclohexanol to phenyl cyclohexene.

    Abstract translation: 在生产苯酚和/或环己酮的方法中,使环己基苯与含氧气体接触以产生含有环己基苯氢过氧化物的氧化流出物。 然后将至少一部分环己基苯氢过氧化物与裂解催化剂接触,以产生包含苯酚和环己酮的裂解流出物以及包括苯基环己醇在内的副产物。 裂解流出物或其中和产物还包含至少一种包含不是碳,氢或氧的原子的化合物,其从裂解流出物和/或其中和产物中分离出来,以在含有 原子不是碳,氢或氧并且含有至少一部分苯基环己醇。 然后至少一部分苯基环己醇与包含MCM-22型分子筛的脱水催化剂接触,以将至少一部分苯基环己醇转化成苯基环己烯。

    Process for producing phenol
    38.
    发明授权
    Process for producing phenol 有权
    苯酚生产工艺

    公开(公告)号:US09096509B2

    公开(公告)日:2015-08-04

    申请号:US14369865

    申请日:2012-12-03

    Abstract: In a process for producing phenol, a mixture of cyclohexylbenzene with from 10 to 90 wt % of a solvent is contacted with oxygen in the presence of a catalyst and under conditions effective to oxidize at least a portion of the cyclohexylbenzene to cyclohexylbenzene hydroperoxide. The catalyst comprises a cyclic imide having an imide group of formula (I): wherein X represents an oxygen atom, a hydroxyl group, or an acyloxy group. At least a portion of the oxygen is dissolved in the mixture and the liquid phase molar ratio of cyclohexylbenzene to oxygen dissolved in the mixture is less than or equal to 20,000:1.

    Abstract translation: 在生产酚的方法中,将环己基苯与10至90重量%的溶剂的混合物在催化剂存在下并在有效氧化至少一部分环己基苯至环己基苯氢过氧化物的条件下与氧接触。 催化剂包含具有式(I)的酰亚胺基的环状酰亚胺:其中X表示氧原子,羟基或酰氧基。 氧气的至少一部分溶解在混合物中,环己基苯与溶解在混合物中的氧的液相摩尔比小于或等于20,000:1。

Patent Agency Ranking