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A new model for solvent extraction in columns

Conference ·
OSTI ID:7179310
A new model was developed for analyzing solvent extraction processes carried out in columns. Each column is treated as a series of well-defined equilibrium stages where the backmixing (other-phase carryover) between stages can be large. By including all mass transfer effects in the backmixing value, the same number of stages can be used for all extracted components no matter what their distribution coefficients. This greatly simplifies the calculations required when modeling multicomponent solvent extraction processes. Initial testing shows the new model to be better than either the Height of an Equivalent Theoretical Plate (HETP) or the Height of a Transfer Unit (HTU) method.
Research Organization:
Argonne National Lab., IL (USA)
Sponsoring Organization:
DOE/NE
DOE Contract Number:
W-31109-ENG-38
OSTI ID:
7179310
Report Number(s):
CONF-891013-10; ON: DE90010416
Country of Publication:
United States
Language:
English