13C同位素低温精馏过程动态模拟

Dynamic Simulation of Isotope 13C Separation by Cryogenic Distillation

  • 摘要: 为深入了解CO低温精馏分离13C系统的动态特性,建立了系统的动态模型,借助软件Aspen Dynamics对该系统的全回流、开车以及物料量发生扰动过程进行了动态模拟。塔釜热负荷和塔釜持液量对全回流过程的影响结果显示,全回流动态浓缩过程耗时约1周,稳定时塔釜13C16O摩尔分数约为3.9%。模拟研究结果显示,先浓缩后稳态出料的开工方案可大幅缩减装置动态开工时间,产品摩尔分数达到14.5%,耗时约需38.6 d;而对应的同时稳态进出料开车方案平衡时间需127.7 d;开发持液量低的填料可进一步缩短开工时间,降低产品成本。对进料扰动的计算表明,本工作采用的分离装置对物料量的波动具有较强的抗干扰能力,波幅50%、时间为4 h的进出料量波动对产品品质的影响可忽略。

     

    Abstract: A dynamic model of the carbon monoxide cryogenic distillation system was set up to deeply study the dynamic characteristics of the system in which the isotope 13C was enriched. The processes of total reflux, startup and fluctuation of material of the system were studied by dynamic simulation software, Aspen Dynamics. The effects of boiling power and bottom holdup in total reflux were studied, the balance time of total reflux was about one week, and the mole fraction of 13C16O at the bottom of the column was about 3.9%. The startup program that first enriching then product outputting can reduce the startup time of the setup, and the balance time with the mole fraction of 13C16O reached to 14.5% was 38.6 d; however, the balance time with feeding and outputting at the same time was 127.7 d. The development of lower holdup packing will shorten the startup time, and then reduce the cost of products. The fluctuation calculation showed that the setup can preferably handle material fluctuation. When in a feeding and outputting fluctuation amplitude up to 50%, and the time lasting 4 hours, the changes of product quality can be neglected.

     

/

返回文章
返回