摘要
研究了丙酮水的相平衡曲线与特点。在计算机上进行了丙酮精馏的模拟与优化，并进行了不同进料浓度下的精馏工艺计算，将新型高效填料与计算机计算结果用于丙酮精馏塔的设计，工业应用试车一次成功。与浮阀塔、泡罩塔、板填复合塔等塔型相比，新塔提高生产能力６７５％～１８０％，节能２５％～４０％，同时得到纯度达９９９％的丙酮产品，排放残液中丙酮质量分数ｗ≤００５％。
The curve and its character of the vapor liquid equilibrium of aceton water system was researched. The simulation and optimization of aceton distillation technology was researched applying new type, high efficiency packing and the computer calculation result. The column was proved successful in industry. Compared with traditional collumn such as bubbling tray column, valve tray column, plate packing column, it can increased capacity by 675%～180%, save energy by 25%～40%, obtain aceton product with purity more than 999% and caldron draining raffinate aceton concentration less than 005%.
出处
《北京化工大学学报（自然科学版）》
CAS
CSCD
1998年第2期1-5,26,共6页
Journal of Beijing University of Chemical Technology(Natural Science Edition)
关键词
丙酮
填料塔
节能
精馏塔
生产
aceton
distillation
packing column
energy saving
