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    • 4. 发明公开
    • SYSTEMS AND METHODS FOR PRODUCING DESIRED XYLENE ISOMERS
    • SYSTEME UND VERFAHREN ZUR ERZEUGUNGGEWÜNSCHTERXYLENISOMERE
    • EP3049379A4
    • 2017-05-17
    • EP14846839
    • 2014-08-28
    • UOP LLC
    • CORRADI JASON TWERBA GREGORYGATTUPALLI RAJESWAR
    • C07C7/10B01D15/00C07C5/22C07C7/09C07C7/11C07C15/08
    • C07C7/005B01D15/362C07C5/2729C07C5/2732C07C7/09C07C15/08
    • Methods and systems are provided for producing a desired xylene isomer. The method includes adsorbing the desired xylene isomer from a mixed xylene stream in an adsorbent chamber. The desired xylene isomer is desorbed with a desorbent to produce an extract stream with the desired xylene isomer and the desorbent, where the desorbent has a lower boiling point than the desired xylene isomer. The extract stream is fractionated in an extract fractionator to produce a low pressure extract overhead stream with gaseous desorbent. The low pressure extract overhead stream is pressurized to produce a high pressure extract overhead stream with a temperature greater than an extract reboiler temperature. The high pressure extract overhead stream is condensed in an extract process reboiler, and produces a liquid extract overhead stream.
    • 提供了用于生产所需二甲苯异构体的方法和系统。 该方法包括在吸附剂室中从混合二甲苯流中吸附期望的二甲苯异构体。 所需的二甲苯异构体用解吸剂解吸以产生具有期望的二甲苯异构体和解吸剂的提取物流,其中解吸剂具有比期望的二甲苯异构体更低的沸点。 提取物流在提取物分馏器中分馏以产生具有气体解吸剂的低压提取物顶部物流。 将低压萃取物顶部物流加压以产生温度高于萃取物再沸器温度的高压萃取物顶部物流。 高压萃取物顶部物流在萃取过程再沸器中冷凝,并产生液体萃取物顶部物流。
    • 5. 发明公开
    • SYSTEMS AND METHODS FOR PRODUCING DESIRED XYLENE ISOMERS
    • 德国维也纳国家工程师协会GEWÜNSCHTERXYLENISOMERE
    • EP3049379A1
    • 2016-08-03
    • EP14846839.0
    • 2014-08-28
    • UOP LLC
    • CORRADI, Jason T.WERBA, GregoryGATTUPALLI, Rajeswar
    • C07C7/10C07C7/09C07C7/11C07C5/22C07C15/08
    • C07C7/005B01D15/362C07C5/2729C07C5/2732C07C7/09C07C15/08
    • Methods and systems are provided for producing a desired xylene isomer. The method includes adsorbing the desired xylene isomer from a mixed xylene stream in an adsorbent chamber. The desired xylene isomer is desorbed with a desorbent to produce an extract stream with the desired xylene isomer and the desorbent, where the desorbent has a lower boiling point than the desired xylene isomer. The extract stream is fractionated in an extract fractionator to produce a low pressure extract overhead stream with gaseous desorbent. The low pressure extract overhead stream is pressurized to produce a high pressure extract overhead stream with a temperature greater than an extract reboiler temperature. The high pressure extract overhead stream is condensed in an extract process reboiler, and produces a liquid extract overhead stream
    • 提供了用于产生所需二甲苯异构体的方法和系统。 该方法包括从吸附剂室中的混合二甲苯流中吸收所需的二甲苯异构体。 所需的二甲苯异构体用解吸剂解吸以产生具有所需二甲苯异构体和解吸剂的萃取物流,其中解吸剂的沸点低于所需的二甲苯异构体。 将提取物流在萃取分馏器中分馏,以产生具有气体解吸剂的低压提取塔顶物流。 将低压提取物塔顶物流加压以产生温度高于提取再沸器温度的高压提取塔顶物流。 高压萃取物塔顶馏出物在萃取过程再沸器中冷凝,并产生液体萃取塔顶馏出液。