摘要
在计算机上模拟优化设计了醋酸甲酯的精馏方案。采用新型高效导向筛板塔解决了含发泡物质物系的精馏难点。技术改造后扩产约50%、节能40%左右并提高了产品质量和回收率。技术改造投资30万元、年增经济效益400万元,投资回收期不到1个月。
In the technology reform of methanol-methyl acetate recovery distillation column,the computer was used to simulate the process, and an optimized distillation technology reform plan was obtained.After the technology reform,the product capacity was increased by 50%,the column pressure drop was decreased by 30%~ 50%,the energy consumption was decreased by about 40%.
出处
《化工进展》
EI
CAS
CSCD
1997年第5期27-29,48,共4页
Chemical Industry and Engineering Progress
关键词
计算机模拟
筛板
乙酸甲酯
精馏塔
技术改造
distillation,computer simulation,methanol-methyl acetate, methanol,flow-guided sieve tray