Separation of La and Ce with PC-88A by counter-current mixer-settler extraction column

被引:76
作者
Abdeltawab, AA [1 ]
Nii, S [1 ]
Kawaizumi, F [1 ]
Takahashi, K [1 ]
机构
[1] Nagoya Univ, Dept Chem Engn, Chikusa Ku, Nagoya, Aichi 4648603, Japan
关键词
solvent extraction; separation of lanthanides; multistage extraction; extraction column; PC-88A;
D O I
10.1016/S1383-5866(01)00180-0
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The separation of La and Ce with 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester (commercially known as PC-88A) from nitrate media was studied with a multistage counter-current mixer-settler extraction column of seven stages developed by the authors. The effect of flow rate ratio of the aqueous phase (Q(w)) to the organic phase (Q(o)) on the separation was studied. The maximum separation was obtained at Q(w)/Q(o) = 3.2 and the separation degree was 63. Scrubbing of the organic phase was also studied in order to enhance the separation. La was scrubbed from the organic phase with nitric acid at pH 2.7 and the separation degree during scrubbing was 45. Simulations of the extraction and scrubbing processes were carried out and compared with the obtained experimental results. Stripping of Ce was achieved by using 100 mol/m(3) nitric acid. The organic phase was successfully recycled during the experiments without any effect on the extraction efficiency. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:265 / 272
页数:8
相关论文
共 17 条
[1]  
Ban T, 2000, SOLVENT EXTR RES DEV, V7, P18
[2]  
Hamidi A, 1999, J CHEM TECHNOL BIOT, V74, P244, DOI 10.1002/(SICI)1097-4660(199903)74:3<244::AID-JCTB31>3.0.CO
[3]  
2-W
[4]   WETTABILITY EFFECTS OF PLATE MATERIALS ON HYDRODYNAMICS IN A PULSED PERFORATED-PLATE EXTRACTION COLUMN OF PULSER FEEDER TYPE [J].
IKEDA, H ;
SUZUKI, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (11) :4110-4117
[5]  
KIROU VI, 1988, AICHE J, V34, P383
[6]   EXTRACTION OF RARE-EARTH-METALS WITH 2-ETHYLHEXYL PHOSPHONIC ACID MONO-2-ETHYLHEXYL ESTER IN THE PRESENCE OF DIETHYLENETRIAMINEPENTAACETIC ACID IN AQUEOUS-PHASE [J].
KUBOTA, F ;
GOTO, M ;
NAKASHIO, F .
SOLVENT EXTRACTION AND ION EXCHANGE, 1993, 11 (03) :437-453
[7]   A UNIFIED CORRELATION FOR THE PREDICTION OF DISPERSED-PHASE HOLD-UP IN LIQUID-LIQUID-EXTRACTION COLUMNS [J].
KUMAR, A ;
HARTLAND, S .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (11) :3925-3940
[8]   CAPACITY AND HYDRODYNAMICS OF AN AGITATED EXTRACTION COLUMN [J].
KUMAR, A ;
STEINER, L ;
HARTLAND, S .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1986, 25 (03) :728-733
[9]   Mass transfer coefficients in mixer-settler extraction column [J].
Nii, S ;
Suzuki, J ;
Tani, K ;
Takahashi, K .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1997, 30 (06) :1083-1089
[10]   Effects of internal structure on throughput of mixer-settler extraction column [J].
Nii, S ;
Suzuki, J ;
Takahashi, K .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1997, 30 (02) :253-259