| 1. | Simulation analysis of four towers flow in methanol distillation process
甲醇四塔精馏过程模拟分析 |
| 2. | Extractive distillation process simulation for dmc - meoh azeotropic system
甲醇共沸物萃取精馏过程模拟研究 |
| 3. | Distillation process of formaldehyde aqueous solution with low - content methanol
低甲醇含量甲醛水溶液的精馏过程研究 |
| 4. | Application of unifac method to the mathematic simulatio n distillation of methanol
法在甲醇精馏过程模拟计算中的应用 |
| 5. | More packing section divisions in three - phase distillation are needed compared to two - phase distillation
. .两相填料塔精馏过程需要更多的填料分段数目。 |
| 6. | Therefore , a novel optimization method for calculating the effective interfacial area is developed for two and three - phase distillations
由此，本文提出了一种两相和三相精馏过程有效相接触面积优化计算方法。 |
| 7. | However , these values are not the same in systems with more than two components and cannot be correlated
然而对于多组份精馏过程而言， murphree板效率和等板高度值对各组份并不完全相同，且组份间不存在直接关联关系。 |
| 8. | A batch extractive distillation process with mixed solvents was studied experimentally in a middle - vessel batch distillation column
摘要采用一个带有中间贮罐的间歇精馏实验塔，对混合溶剂间歇萃取精馏过程进行了实验研究。 |
| 9. | During the course of rectifying zinc , the fluid of coarse liquid zinc put into pb column from furnace works as a key technical parameter
在锌的精馏过程中，液态粗锌从熔化炉加入到铅塔这个过程的流量是一个关键的技术参数。 |
| 10. | Especially for complicated multicomponent distillation processes , such as three - phase distillations in this work , the equilibrium model will lead to a significant error in the distillation modelling
尤其对于复杂的多组份精馏过程，例如本文所讨论的三相精馏过程，平衡模型对过程的描述会造成较大误差。 |
