Extraction of Cephalosporin Antibiotics with Aqueous Two-phase Systems Composed of Water-miscible Organic Solvents and Salts

被引:6
作者
Matsumoto, Michiaki [1 ]
Ueda, Takashi [1 ]
机构
[1] Doshisha Univ, Dept Chem Engn & Mat Sci, Kyoto 6100321, Japan
关键词
SUCCINIC ACID; CEPHALEXIN; SEPARATION; BROTH;
D O I
10.15261/serdj.26.63
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The beta-lactam antibiotics such as penicillin and cephalosporin account for over 65% of the market. Development of a more effective separation technique is desired to extract and purify the biologically active cephalosporin antibiotics. In this study, to recover cephalosporin antibiotics, cephalosporin C and cephalexin, an aqueous two-phase system (ATPS) composed of a water-miscible organic solvent and salts was used. For cephalosporin C extraction with the ATPS, the extent of extraction of cephalosporin C was small because of its high hydrophilicity. For cephalexin, which is more hydrophobic, it was successfully extracted with ATPS. From binodal experiments, tetrahydrofuran (THF), 1-propanol and acetone were selected as the candidates for the extraction solvent. In the extraction experiments, THF was found to be suitable because it gave the highest extractability of cephalexin and the lowest water content in the top (solvent) phase among the candidates. When the initial volume ratio of water to solvent was unity, the maximum distribution ratio was 3.13. The value of the distribution ratio increased up to 9.87 with increasing initial volume ratio. The ATPS composed of a water-miscible organic solvent and salt was found to be promising for purification of antibiotics under such mild conditions.
引用
收藏
页码:63 / 68
页数:6
相关论文
共 17 条
  • [1] Aqueous two-phase partitioning of cephalosporin antibiotics: effect of solute chemical nature
    Bora, MM
    Borthakur, S
    Rao, PC
    Dutta, NN
    [J]. SEPARATION AND PURIFICATION TECHNOLOGY, 2005, 45 (02) : 153 - 156
  • [2] Extraction equilibria of cephalosporin antibiotics with Aliquat-33
    Bora, MM
    Dutta, NN
    Bhattacharya, KG
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2000, 45 (02) : 399 - 403
  • [3] Industrial production of β-lactam antibiotics
    Elander, RP
    [J]. APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 2003, 61 (5-6) : 385 - 392
  • [4] Ghosh A C, 1997, Adv Biochem Eng Biotechnol, V56, P111
  • [5] REACTIVE EXTRACTION OF CEPHALOSPORIN-C
    HANO, T
    MATSUMOTO, M
    OHTAKE, T
    HORI, F
    [J]. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1992, 25 (03) : 293 - 297
  • [6] Hansch C., 1987, The Log P Database
  • [7] Extraction and Esterification of Succinic Acid Using Aqueous Two-phase Systems Composed of Ethanol and Salts
    Matsumoto, Michiaki
    Tatsumi, Masahiro
    [J]. SOLVENT EXTRACTION RESEARCH AND DEVELOPMENT-JAPAN, 2018, 25 (02) : 101 - 107
  • [8] Extraction of 2,3-Butanediol with Aqueous Two-Phase Systems Formed by Water-Miscible Organic Solvents and Inorganic Salts
    Matsumoto, Michiaki
    Okuno, Ryosuke
    Kondo, Kazuo
    [J]. SOLVENT EXTRACTION RESEARCH AND DEVELOPMENT-JAPAN, 2014, 21 : 181 - 190
  • [9] Mokhtari A., 2017, J APPL CHEM RES, V11, P21
  • [10] Extraction of tetracycline from fermentation broth using aqueous two-phase systems composed of polyethylene glycol and cholinium-based salts
    Pereira, Jorge F. B.
    Vicente, Filipa
    Santos-Ebinuma, Valeria C.
    Araujo, Janete M.
    Pessoa, Adalberto
    Freire, Mara G.
    Coutinho, Joao A. P.
    [J]. PROCESS BIOCHEMISTRY, 2013, 48 (04) : 716 - 722