LIQUID-LIQUID EXTRACTION
 

 

 

 

 


FAMU-FSU College of Engineering: Unit Operations Lab



Theory

 

        To analyze the liquid-liquid extraction column, there is only a need for a few equations, which include the overall and component mass balances.  To create a balance that relates inlet and outlet streams, the overall mass balance is used. (Elementary Principles of Chemical Processes 2nd Edition, pg 85)

 

F + S =  E + R

(1)

 

F, S, E, and R in the above equation represent feed, solvent, extract, and raffinate mass flow rates, respectively.  The extract is the new mixture exiting the bottom of the column, while the raffinate is the more pure component exiting the top of the column.

        A further analysis may be needed to relate the compositions of the streams to the flow rates.  By doing this, it is possible to find unknown compositions or flow rates of any stream.  The component mass balances for a three-component system are given as follows: (Elementary Principles of Chemical Processes 2nd Edition, pg 89)

 

F • XAF + S • XAS = E • XAE + R• XAR (Component A)

 

(2)

F • XBF + S • XBS = E • XBE + R • XBR (Component B)

 

(3)

F • XCF + S • XCS = E • XCE + R • XCR (Component C)

 

(4)

 

Variables of Interest

Description

F

Feed flow rate

S

Solvent flow rate

E

Extract flow rate

R

Raffinate flow rate

XAF

Component A composition in feed stream

XAS

Component A composition in solvent stream

XAE

Component A composition in extract stream

XAR

Component A composition in raffinate stream

XBF

Component B composition in feed stream

XBS

Component B composition in solvent stream

XBE

Component B composition in extract stream

XBR

Component B composition in raffinate stream

XCF

Component C composition in feed stream

XCE

Component C composition in extract stream

XCS

Component C composition in solvent stream

XCR

Component C composition in raffinate stream

 

 

NOTES:      

1) A more advanced analysis of liquid-liquid extraction can be found in Perry's Chemical Engineers' Handbook 7th Edition in Section 15, and Transport Processes and Unit Operation 3rd Edition in Chapter 12.

2) The following web site is useful in creating a computer generated ternary plot:

http://www.sfu.ca/~marshall/ternplot.htm

 

 

 

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Last modified: November 26, 2001

Created by Team #2