Non-equilibrium modelling of distillation

作者: J.A. Wesselingh

DOI: 10.1205/026387697524083

关键词:

摘要: … a single tray as a stage. There is no natural boundary to the stages in packed columns (… In nonequilibrium calculations we use the same equations to obtain the driving forces for mass …

参考文章(1)
Ross Taylor, R. Krishna, Multicomponent mass transfer ,(1993)