EXTRACTION RATE OF PRASEODYMIUM AND NEODYMIUM WITH PHOSPHONIC ACID MONO ESTER

被引:4
作者
MORI, Y
HAMADA, T
KORESAWA, E
EGUCHI, W
机构
[1] Department of Chemical Engineering, Kyoto University
关键词
Extraction Rate EHPNA; Solvent Extraction Rare Earth Elements Phosphonic Acid Mono Ester Mass Transfer;
D O I
10.1252/jcej.23.616
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Recently, interest has increased in the practical application of solvent extraction technology for the mutual separation and purification of rare earth metals. 2-Ethylhexyl phosphonic acid mono-2-ethylhexyl ester (henceforth EHPNA) has recently been developed, and was found to have high capability of lanthanoid extraction. This paper reports the extraction rate of praseodymium and neodymium with EHPNA in toluene from hydrochloric acid solution by use of a stirred transfer cell of Lewis type at 298 K. The experimental results suggested the existence of chemical reaction resistance at the interface at low extractant concentration and high pH value in the forward extraction, in addition to the film mass transfer resistances in the aqueous and the organic phases. The time course change of the extraction from mixed lanthanoid aqueous solution was satisfactorily predicted by the extraction model presented. © 1990, The Society of Chemical Engineers, Japan. All rights reserved.
引用
收藏
页码:616 / 620
页数:5
相关论文
共 16 条
[1]  
BENRAN KK, 1978, MARUZEN, P55
[2]   KINETICS AND MECHANISM OF THE INTERFACIAL MASS-TRANSFER OF EU3+ AND AM3+ IN THE SYSTEM BIS(2-ETHYLHEXYL) PHOSPHATE-NORMAL-DODECANE-NACL-HCL-WATER [J].
DANESI, PR ;
VANDEGRIFT, GF .
JOURNAL OF PHYSICAL CHEMISTRY, 1981, 85 (24) :3646-3651
[3]  
DUYCKAERTS G, 1960, J INORG NUCL CHEM, V13, P332
[4]   SEPARATION FACTORS FOR SOLVENT EXTRACTION PROCESSES - SYSTEM OF 1 M DI-(2-ETHYL-HEXYL) PHOSPHORIC ACID (IN AMSCO 125-82)-PR-ND SALTS AS AN EXAMPLE [J].
GOTO, T ;
SMUTZ, M .
JOURNAL OF INORGANIC & NUCLEAR CHEMISTRY, 1965, 27 (06) :1369-&
[5]   EXTRACTION RATE OF LANTHANUM BY D2EHPA [J].
IMAI, M ;
FURUSAKI, S .
KAGAKU KOGAKU RONBUNSHU, 1987, 13 (03) :355-362
[6]   KINETICS OF EXTRACTION OF TM+3 BY DIETHYLHEXYLPHOSPHORIC ACID AND DINONYLNAPHTHALENESULFONIC ACID [J].
KANDIL, AT ;
CHOPPIN, GR .
JOURNAL OF INORGANIC & NUCLEAR CHEMISTRY, 1975, 37 (7-8) :1787-1789
[7]   ACIDIC ORGANOPHOSPHORUS EXTRACTANTS .12. EFFECT OF EXTRACTANT STRUCTURE ON EXTRACTION OF LANTHANIDES(III) [J].
KOLARIK, Z ;
DRAZANOV.S ;
CHOTIVKA, V .
JOURNAL OF INORGANIC & NUCLEAR CHEMISTRY, 1971, 33 (04) :1125-&
[8]   EXTRACTION EQUILIBRIUM OF CE(III), PR(III) AND ND(III) WITH ACIDIC ORGANO-PHOSPHORUS EXTRACTANTS [J].
MORI, Y ;
OHYA, H ;
ONO, H ;
EGUCHI, W .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1988, 21 (01) :86-91
[9]   STUDY OF KINETIC FACTORS AFFECTING THE EFFICIENCY OF SEPARATION OF TRANSPLUTONIUM AND RARE-EARTH ELEMENTS DURING THE EXTRACTION BY DI-(2-ETHYLHEXYL)PHOSPHORIC ACID [J].
NOVIKOV, AP ;
MYASOEDOV, BF .
SOLVENT EXTRACTION AND ION EXCHANGE, 1985, 3 (03) :267-282
[10]   EXTRACTION OF SOME HEAVIER LANTHANIDES IN ACIDIC CHLORIDE SOLUTIONS BY DI(2-ETHYLHEXYL) PHOSPHORIC ACID [J].
OWENS, TC ;
SMUTZ, M .
JOURNAL OF INORGANIC & NUCLEAR CHEMISTRY, 1968, 30 (06) :1617-&