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Separation of ethylbenzene and p-xylene using extractive distillation with p-dinitrobenzene

机译:用P-二硝基苯萃取蒸馏分离乙苯和对二甲苯

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Though p-xylene derived from naphtha reformate is in high demand as a raw material in the production of polyesters and polyethylene terephthalates, its separation from the FCC reformate is not easy due to close boiling points among the components in the reformate. When a proper solvent for the p-xylene separation is available, an extractive distillation can be applied in the separation. Currently the separation utilizes an adsorption process requiring a large amount of costly adsorbent and a desorption process followed by distillation. In the proposed extractive distillation here, p-dinitrobenzene has been utilized to improve the separation of p-xylene from its ethylbenzene mixture. The VLE data of the ternary mixture estimated with the UNIFAC were compared to those computed from molecular simulation to show their reliability. An extractive distillation and solvent recovery were applied to obtain 99.6% purity p-xylene with 99.1% recovery. The economics of the proposed process demonstrates its comparability to the existing Parex process.
机译:虽然来自石脑油重整的石磷脂是在生产聚酯和聚对苯二甲酸乙二醇酯的原料中的高需求中,但由于重整产物中组分的沸点沸点,其与FCC重构的分离并不容易。当可获得对二甲苯分离的适当溶剂时,可以在分离中施加萃取蒸馏。目前,分离利用需要大量昂贵的吸附剂和解吸过程的吸附过程,然后蒸馏。在此提出的萃取蒸馏在此,已利用p-二硝基苯来改善对二甲苯的分离乙苯混合物。将使用UNIFAC估计的三元混合物的VLE数据与来自分子模拟计算的那些进行比较,以显示其可靠性。施用萃取蒸馏和溶剂回收率,得到99.6%的纯度对二甲苯,回收率为99.1%。拟议过程的经济学证明了对现有Parex过程的可比性。

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