CIESC Journal

• 化工学报 •    下一篇

精密精馏填料塔的稳态特性

余国琮,杨志才,顾芳珍   

  1. 天津大学化工系 ,天津大学化工系 ,天津大学化工系
  • 出版日期:1980-06-25 发布日期:1980-06-25

The Steady Characteristics of Packed Column for Close-Boiling Fractionation

Yu Kuo-tsung Yang Zhi-cai Gu Fang-zhen Department of Chemical Engineering, Tianjin University   

  • Online:1980-06-25 Published:1980-06-25

摘要: 本文第一部分探讨精密精馏填料塔的最佳回流比。文中提出一个关联式来估算在一定回流比下的传质单元数,并由此导出最佳回流比图。精密精馏最佳回流比的最大值约为1.4R_m。 本文第二部分探讨最佳的塔径与填料尺寸比。实验是在内径分别为20、28、32、44mm,填料层高从1020到1475mm四个填料塔中用2.5×2.5mm三角螺旋填料以正庚烷-甲基环己烷系统进行。根据实验求得的全塔浓度分布曲线,在除去塔顶及塔底两端的端效应后,得出填料层的真实分离效率(即传质单元高度或每米填料高的传质单元数)。以真实分离效率与塔径及填料尺寸比作图,所有恒气速下的曲线都呈现出最佳点,并且其比值几乎相同。对于这种填料,最佳塔径与填料尺寸比约为13—14,此值与普通填料或工业填料大致相似。

Abstract: The first part of this paper concerns with optimum reflux ratio of packed column for close-boiling fractionation. A correlation is proposed to find the NTU at finite reflux and from which a graph representing the optimum reflux ratio is derived. It is found that the maximum value of optimum reflux ratio is about 1.4Rm. The second part of this paper concerns with optimum ratio of column diameter to packing size. Experimental work has been conducted with four laboratory columns of 20, 28,32 and 44 mm in diameter respectively, the height of packed bed ranging from 1020 to 1475mm, the packing used being 2.5x2.5 mm angular helices and the testing system to be n-heptane-methylcyclohe-xane. The true separation efficiency (i. e. true HTU or true NTU per meter of bed height)is evaluated from the experimental composition profile by discarding the end effect at the top and the bottom ends of packing. By plotting the true separation efficiency versus the ratio of column diameter to packing size, all the curves at constant vapor velocity exhibit an optimum reflux ratio with nearly identical value. The optimum reflux ratio for this packing is found to be 13-14 which is in rough agreement with that for ordinary or industrial size of packing.