Evaluation of Height Equivalent Theoretical Plate of Packing Distillation Column for Benzaldehyde Purification Processing

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Abstract

This study analyzes the literature review of the techniques for estimating Height Equivalent Theoretical Plate (HETP) values for various packing structure models, ranging from theoretical to semi-empirical to shortcut methods. Packing structures of various meshes and shapes were studied on the purification of benzaldehyde from the mixture of benzaldehyde and cinnamaldehyde. The packing structures M-50, M-80, O-80, and S-80 were estimated using Fenske’s approach as 0.052, 0.053, 0.045, and 0.056, respectively. Experiment data and simulation result obtained by commercial software were utilized to validate the packing's HETP value. A pilot of the vacuum batch distillation system was fabricated including a column filled with packing structures. The results indicated that the HETP value between experiment and simulation is within 0.6 percent deviation. On the pilot scale, the results of the benzaldehyde purifying were validated in a batch distillation system with the O-80 packing structure. This system will be developed for the larger scale, and it will practical.
苯甲醛净化填料精馏塔高度等效理论板的评价
本文对各种填料结构模型的高度等效理论板(HETP)估算方法进行了文献综述,包括理论方法、半经验方法和快捷方法。从苯甲醛和肉桂醛的混合物中提纯苯甲醛,研究了不同网格和形状的填充结构。采用Fenske方法估计M-50、M-80、O-80和S-80的填充结构分别为0.052、0.053、0.045和0.056。利用商业软件获得的实验数据和仿真结果对填料的HETP值进行了验证。制作了一个真空间歇精馏系统的试验装置,其中包括一个填充填料结构的塔。结果表明,实验值与仿真值的偏差在0.6%以内。在中试规模上,采用O-80填料结构的间歇精馏系统对苯甲醛的净化效果进行了验证。该系统将用于更大规模的开发,具有一定的实用性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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