摘要
针对DMAC-水溶液的精馏回收工艺中塔顶塔底温差大的特点,提出了中间再沸式热泵精馏工艺。利用Aspen Plus化工流程模拟软件对该工艺多种工况进行模拟,得出了最佳的中间再沸器位置和再沸比参数;通过分析,讨论了压缩机在系统中的控制作用。结果表明,在压缩机压缩比为2.0,再沸器最小传热温差为10.9℃情况下,本工艺相对于常规精馏可节能约85.9%。
Inter-reboiler mechanical vapor recompression (MVR) heat pump distillation is proposed based on the large temperature difference between tower top and tower bottom.The simulations for inter-reboiler MVR heat pump distillation are carried out by Aspen Plus software which includes a variety of condition.The location of inter-reboiler and reflux ratio are obtained.Besides that,the compressor in the system control function is also discussed.The results show that the inter-reboiler MVR heat pump distillation can save energy by 85.9%,compared with conventional distillation under the condition as follows:2.0 of the compressor compression ratio and 10.9℃ of reboiler minimum heat transfer temperature.
出处
《现代化工》
CAS
CSCD
北大核心
2013年第8期114-116,共3页
Modern Chemical Industry
关键词
稀二甲基乙酰胺水溶液
热泵精馏
中间再沸精馏
流程模拟
节能
diluted DMAC water solution
heat pump distillation
Inter-reboiler
process simulation
energy-saving