摘要
建立了间歇精馏塔的数学模型,在MATLAB/SIMULINK中用S-函数编制了间歇精馏塔的模拟程序,相平衡计算采用严格的热力学模型,该方法为间歇精馏的设计及操作提供了参考.
Mathematical models of batch distillation column are presented. The Sfunction in MATLAB/SIMULINK is used to programming the simulation programs of batch distillation column, and the rigorous thermodynamics model is used to calculate phase equilibrium. The method provides references for the design and operation of batch distillation.
出处
《吉林化工学院学报》
CAS
2003年第2期1-3,共3页
Journal of Jilin Institute of Chemical Technology
