SEPARATION OF PHENYLACETIC ACID, 6-AMINOPENICILLANIC ACID AND PENICILLIN-G WITH ELECTRODIALYSIS UNDER CONSTANT-CURRENT

被引:15
作者
CHEN, DH [1 ]
WANG, SS [1 ]
HUANG, TC [1 ]
机构
[1] NATL CHENG KUNG UNIV,DEPT CHEM ENGN,TAINAN 70101,TAIWAN
关键词
PHENYLACETIC ACID; 6-AMINOPENICILLANIC ACID; PENICILLIN G; SEPARATION; ELECTRODIALYSIS;
D O I
10.1002/jctb.280640311
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The separation behavior of phenylacetic acid (PAA), 6-aminopenicillanic acid (6-APA) and penicillin-G (Pen-G) with electrodialysis under constant current was studied. The effects of ionic concentrations and current density on their separation behavior were investigated. The sorption of PAA, 6-APA and Pen-G in the anion exchange membrane, and the variations of applied voltage and current efficiencies with time during electrodialysis were also examined. It was found that the molecular size and the affinity toward the anion exchange membrane played a key role for the electrodialysis of PAA, 6-APA and Pen-G. Phenylacetic acid had the lowest affinity toward the membrane but the fastest transport rate. Penicillin-G had the highest affinity toward the membrane but the slowest transport rate. With the increase of Pen-G concentration, the concentration polarization of Pen-G in the vicinity of anion exchange membrane became very serious, which severely retarded the transport of PAA and 6-APA. Although the increase of current density accelerated the transport of PAA, 6-APA and Pen-G, more serious concentration polarization of Pen-G occurred and the separation ratio of PAA to 6-APA decreased.
引用
收藏
页码:284 / 292
页数:9
相关论文
共 18 条
[1]  
BUNGAY PM, 1986, NATO ASI SERIES, V181
[2]  
Hara Y, 1963, B CHEM SOC JPN, V36, P1373
[3]   COUPLING OF UREA HYDROLYSIS AND AMMONIUM REMOVAL IN AN ELECTRODIALYZER WITH IMMOBILIZED UREASE [J].
HUANG, TC ;
CHEN, DH .
CHEMICAL ENGINEERING COMMUNICATIONS, 1993, 120 :191-201
[4]   CORRELATION OF IONIC TRANSFER RATE IN ELECTRODIALYSIS UNDER LIMITING CURRENT-DENSITY CONDITIONS [J].
HUANG, TC ;
YU, IY .
JOURNAL OF MEMBRANE SCIENCE, 1988, 35 (02) :193-206
[5]   PERMSELECTIVITY OF CALCIUM-ION TO POTASSIUM-ION IN ION-EXCHANGE MEMBRANE ELECTRODIALYSIS OF SUGAR SOLUTION [J].
HUANG, TC ;
YU, TM .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1983, 26 (02) :119-125
[6]  
HUANG TC, 1992, J CHEM TECHNOL BIOT, V55, P191
[7]   RECOVERY OF SULFURIC-ACID WITH MULTICOMPARTMENT ELECTRODIALYSIS [J].
HUANG, TC ;
JUANG, RS .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1986, 25 (02) :537-542
[8]   PREFERENTIAL TRANSPORT OF CUPRIC AND FERRIC IONS THROUGH ION-EXCHANGE MEMBRANES WITH ELECTRODIALYSIS IN THE PRESENCE OF CITRIC-ACID [J].
HUANG, TC ;
WANG, JK .
CHEMICAL ENGINEERING COMMUNICATIONS, 1993, 122 :213-225
[9]   PREFERENTIAL TRANSPORT OF NICKEL AND CUPRIC IONS THROUGH CATION-EXCHANGE MEMBRANE IN ELECTRODIALYSIS WITH A COMPLEX AGENT [J].
HUANG, TC ;
WANG, JK .
DESALINATION, 1992, 86 (03) :257-271
[10]   A STUDY OF IONIC TRANSFER IN ELECTRODIALYSIS PROCESS WITH LAMINAR-FLOW [J].
HUANG, TC ;
WANG, JH .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1989, 67 (03) :385-391