In a review article published in 2019, Sprakel and Schuur reviewed studies on the development of suitable solvents in the liquid-liquid extraction process of carboxylic acids. The distribution...


In a review article published in 2019,<br>Sprakel and Schuur reviewed studies on<br>the development of suitable solvents in the<br>liquid-liquid extraction process of carboxylic<br>acids. The distribution coefficients (KD)<br>obtained in the liquid-liquid extraction of<br>acetic acid from trioctylamine (TOA) with<br>various solvents are given in the figure<br>below. By interpreting the figure, interpret<br>which solvents can be used effectively in<br>extraction, and the results obtained change<br>depending on which properties of the<br>solvents.<br>4.0<br>3.5<br>3.0-<br>2.5<br>C 2.0-<br>1.5-<br>1.0 -<br>0.5-<br>0.04<br>1-octanol<br>chloroform<br>ethyl acetate<br>1-decanol<br>mibk<br>2-ethyl-hexanol<br>dichloromethane<br>toluene<br>n-decane<br>n-octane<br>Shape.<br>Distribution coefficients (KD)<br>obtained in liquid-liquid extraction of acetic<br>acid ([HAc]0=0.6M) from 0.5 M trioctylamine<br>(TOA) with various solvents<br>Mi Notlar ile oluşturuldu<br>

Extracted text: In a review article published in 2019, Sprakel and Schuur reviewed studies on the development of suitable solvents in the liquid-liquid extraction process of carboxylic acids. The distribution coefficients (KD) obtained in the liquid-liquid extraction of acetic acid from trioctylamine (TOA) with various solvents are given in the figure below. By interpreting the figure, interpret which solvents can be used effectively in extraction, and the results obtained change depending on which properties of the solvents. 4.0 3.5 3.0- 2.5 C 2.0- 1.5- 1.0 - 0.5- 0.04 1-octanol chloroform ethyl acetate 1-decanol mibk 2-ethyl-hexanol dichloromethane toluene n-decane n-octane Shape. Distribution coefficients (KD) obtained in liquid-liquid extraction of acetic acid ([HAc]0=0.6M) from 0.5 M trioctylamine (TOA) with various solvents Mi Notlar ile oluşturuldu

Jun 07, 2022
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