Liquid-liquid extraction using the composition-induced phase separation process

被引:46
作者
Gupta, R [1 ]
Mauri, R [1 ]
Shinnar, R [1 ]
机构
[1] CUNY CITY COLL,DEPT CHEM ENGN,NEW YORK,NY 10031
关键词
D O I
10.1021/ie950362t
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper describes a new separation process of liquid-liquid extraction. It consists of first mixing the system to be extracted with a primary solvent, which is soluble with the native solvent, and subsequently adding a modifier, which is insoluble with either the native or the primary solvent. This process is similar to the phase transition extraction, which was described in a previous paper, where the liquid mixture, together with the solute to be separated, is first heated above its critical temperature, where it forms a uniform solution, and then cooled to the region below the miscibility curve, where it separates. Both processes have the advantage that the resulting separation of the solvents is very rapid, even in the presence of emulsion-forming impurities. In addition, the extraction efficiency of the new process may be 10 times higher than that of the traditional liquid-liquid extraction. The new process is thought of having significant advantages in the extraction of products from fermentation broths, plants, and other natural sources.
引用
收藏
页码:2360 / 2368
页数:9
相关论文
共 8 条
[2]  
ELIYAHU N, 1995 AICHE ANN M MIA
[3]  
FROMENT GF, 1979, CHEM REACTOR ANAL DE, P174
[4]  
Gunton J.D., 1983, Phase Transitions and Critical Phenomena, V8, P267
[5]  
Ludmer Z, 1990, US Patent, Patent No. [4,954,260, 4954260]
[6]  
SORENSEN JM, 1980, CHEM DATA SERIES 2, V5, P183
[7]   PHASE-TRANSITION EXTRACTION USING SOLVENT MIXTURES WITH CRITICAL-POINT OF MISCIBILITY [J].
ULLMANN, A ;
LUDMER, Z ;
SHINNAR, R .
AICHE JOURNAL, 1995, 41 (03) :488-500
[8]  
ULLMANN A, 1993, THESIS CITY U NEW YO