ISSN: 0304-128X ISSN: 2233-9558
Copyright © 2024 KICHE. All rights reserved

Articles & Issues

Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.

All issues

용매-물-아세톤계에 대한 삼성분계의 액-액 평형

Liquid-Liquid Equilibria for Ternary Systems with Solvent-Water-Acetone

HWAHAK KONGHAK, June 1986, 24(3), 185-194(10), NONE
downloadDownload PDF

Abstract

25 ℃에서 다음 3성분계, 1-1-2 trichloroethane-water-acetone, monochlorobenzene-water-acetone, cyclohexane-water-acetone, ethylacetate-water-acetone, chloroform-water-acetone, methylisobutyl ketone-water-acetone에 대한 용해도곡선을 측정하여 tie-line, plait point를 결정하였다.
Tie-line계산치를 추산하기 위하여 최소자승법을 사용하여 tie-line실험치만으로 NRTL식 중의 parameter를 결정하였다.
또한 각각의 3성분계에 대한 분배곡선, 선택도곡선을 결정하여 용매의 추출성능을 조사하였다.
The binodal curves for following ternary systems : 1-1-2 trichloroethane-water-acetone, monochlorobenzene-water-acetone, cyclohexane-water-acetone, ethylacetate-water-acetone, chloroform-water-acetone, and methylisobutyl ketone-water-acetone were determined at 25 ℃.
From these binodal curves, tie-line and plait-point were determined.
The parameters in NRTL model were determined with only experimental tie-lines by the least-squares method to predict the value of tie-lines.
The distribution and the selectivity curves were determined for ternary systems and solvents extraction effectiveness was also examined.

Keywords

The Korean Institute of Chemical Engineers. F5, 119, Anam-ro, Seongbuk-gu, 233 Spring Street Seoul 02856, South Korea.
Phone No. +82-2-458-3078FAX No. +82-507-804-0669E-mail : kiche@kiche.or.kr

Copyright (C) KICHE.all rights reserved.

- Korean Chemical Engineering Research 상단으로