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三元醇类间歇精馏模拟和实验
郝文峰1; 樊栓狮2; 李文秀3; 王金渠1; 殷德宏1
2004
Source Publication化工学报
ISSN0438-1157
Volume055Issue:006Pages:934
Abstract在ASOG相平衡理论的基础上,利用托马斯法(Thomas)模拟三元醇类间歇精馏过程,用精确校正法防止模拟结果的失真现象.实验结果证明了数学模型的正确性及计算方法的可靠性.定义了单位时间经济效益目标函数,并讨论了回流比和理论板数对单位时间经济效益的影响关系,得出了在给定条件下的最佳回流比为5.5,最佳操作理论板数为20的结论。
Language英语
Document Type期刊论文
Identifierhttp://ir.giec.ac.cn/handle/344007/19981
Collection中国科学院广州能源研究所
Affiliation1.大连理工大学
2.中国科学院广州能源研究所
3.沈阳化工大学
Recommended Citation
GB/T 7714
郝文峰,樊栓狮,李文秀,等. 三元醇类间歇精馏模拟和实验[J]. 化工学报,2004,055(006):934.
APA 郝文峰,樊栓狮,李文秀,王金渠,&殷德宏.(2004).三元醇类间歇精馏模拟和实验.化工学报,055(006),934.
MLA 郝文峰,et al."三元醇类间歇精馏模拟和实验".化工学报 055.006(2004):934.
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