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Simulation and Optimization for Production of Cyclopentyl Alcohol through Cyclopentene Hydration
Pages: 39-42
Year: Issue:  6
Journal: Techno-Economics in Petrochemicals

Keyword:  环戊烯环戊醇水合模拟;
Abstract: 运用ASPEN PLUS化工过程模拟软件对由环戊烯制备环戊醇的间接水合工艺中的分离提纯部分进行了模拟计算和参数优化,模拟结果显示:汽提塔的理论板数为10,采用0.35 MPa的低压蒸汽,流量为10 kg/h;环戊醇精制塔的理论板数为10,进料位置为第7块理论板处,合适的回流比为0.6~0.8.
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