摘要
应用Aspen化工模拟软件对甲醇主精馏塔进行了模拟计算,算出主精馏塔的最小回流比和最小理论板数,进而做出全塔的浓度和温度分布,为生产实际提供参考。
Simulation of ASPEN was applied in the methanol distillation pressed. The min-reflux-ratio and the mintheoretically perfect tray were calculated. The profiles of the compositions in distillation column was constructed. So it was reference in locale process.
出处
《安徽化工》
CAS
2008年第3期30-32,共3页
Anhui Chemical Industry
关键词
ASPEN
甲醇
精馏
模拟
Aspen
methanol
distillation
simulation