首页> 外国专利> Regenerating a catalyst, useful to produce or reform aromatic hydrocarbon e.g. benzene, toluene, ortho-, meta- or paraxylene, comprises combustion of the catalyst followed by oxychlorination and calcination

Regenerating a catalyst, useful to produce or reform aromatic hydrocarbon e.g. benzene, toluene, ortho-, meta- or paraxylene, comprises combustion of the catalyst followed by oxychlorination and calcination

机译:再生可用于生产或重整芳烃的催化剂,例如苯,甲苯,邻,间或对二甲苯包括燃烧催化剂,然后进行氧氯化和煅烧

摘要

Process for regenerating a catalyst for producing or reforming aromatic hydrocarbon, comprises (a) combustion in a combustion zone A comprising two combustion beds A1 and A2 in series, (b) oxychlorinating in oxychlorinating zone B comprising one oxychlorinating bed, where the oxychlorinating zone B is fed by a chlorinating agent, water or water precursors and gas comprising oxygen, and (c) calcining in a calcining zone C comprising a calcining bed fed by a gas comprising at least an auxiliary dry air. Process for regenerating a catalyst for producing or reforming aromatic hydrocarbon, comprises (a) combustion in a combustion zone A comprising two combustion beds A1 and A2 in series, (b) oxychlorinating in oxychlorinating zone B comprising one oxychlorinating bed, where the oxychlorinating zone B is fed by a chlorinating agent, water or water precursors and gas comprising oxygen, and (c) calcining in a calcining zone C comprising a calcining bed fed by a gas comprising at least an auxiliary dry air, where: the catalyst comprises a support, chlorine and at least a noble metal and is circulated in beds A1 and A2 serially, in the oxychlorinating zone B and in the calcining zone C; effluent gas of bed A1 is sent to bed A2; the gas feeding in the calcining zone C circulates freely towards the oxychlorinating zone B; the auxiliary gas comprising oxygen is produced in an entry of the calcining zone; the effluent gas of the oxychlorinating zone is partly recycled through washing section D towards the entry of the combustion beds A1 and A2; the effluent gas of the oxychlorinating zone is partly recycled by a blower without passing by the section D towards the combustion bed A2; and the effluent gas of the combustion bed A2 is partly recycled through the section D towards the entry of the beds A1 and A2.
机译:再生用于生产或重整芳族烃的催化剂的方法,包括(a)在包括两个串联的燃烧床A1和A2的燃烧区A中燃烧,(b)在包括一个氧氯化床的氧氯化区B中进行氧氯化,其中氧氯化区B由氯化剂,水或水前体和包含氧气的气体进料,(c)在包含由至少包含辅助干燥空气的气体进料的煅烧床的煅烧区C中煅烧。再生用于生产或重整芳族烃的催化剂的方法包括:(a)在包括两个串联的燃烧床A1和A2的燃烧区A中燃烧,(b)在包括一个氧氯化床的氧氯化区B中进行氧氯化,其中氧氯化区B由氯化剂,水或水前体和含氧气体供入,和(c)在煅烧区C进行煅烧,煅烧区C包含由至少包含辅助干燥空气的气体供入的煅烧床,其中:催化剂包含载体,氯和至少一种贵金属,并在床A1和A2中,在氧氯化区B和煅烧区C中依次循环;床A1的废气送入床A2。进料到煅烧区C中的气体自由地流向氧氯化区B。在煅烧区的入口产生包含氧气的辅助气体。氧氯化区的废气部分地通过洗涤区D再循环至燃烧床A1和A2的入口;氧氯化区的废气部分地由鼓风机再循环,而没有经过段D流向燃烧床A2。燃烧床A2的废气部分经段D再循环到床A1和A2的入口。

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