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大小:2.27 MB
页数:54页
时间:2020-01-27
《化工原理课程设计乙醇水精馏塔设计(浮阀塔).doc》由会员上传分享,免费在线阅读,更多相关内容在行业资料-天天文库。
1、目录1目录1目录.................................................................................................................................12设计任务书.....................................................................................................................43设计方案的确定及流程说明.........................
2、................................................................53.1塔的类型选择......................................................................................................53.2塔板类型的选择..................................................................................................53.3塔压确定.......
3、.......................................................................................................53.4进料热状况的选择..............................................................................................53.5塔釜加热方式的确定..............................................................................
4、............53.6塔顶冷凝方式......................................................................................................63.7塔板溢流形式......................................................................................................63.8塔径的选取.......................................................
5、...................................................63.9适宜回流比的选取..............................................................................................63.10操作流程............................................................................................................64塔的工艺设计..................
6、...............................................................................................74.1精馏塔全塔物料浓度计算:..............................................................................74.2理论板的计算.....................................................................................................
7、.74.2.1最小回流比的计算...................................................................................74.2.2理论板数的计算.......................................................................................84
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