Bioreactors based on monolith-supported ionic liquid phase for enzyme catalysis in supercritical carbon dioxide

被引:107
作者
Lozano, Pedro
Garcia-Verdugo, Eduardo
Piamtongkam, Rungtiwa
Karbass, Naima
De Diego, Teresa
Burguete, M. Isabel
Luis, Santiago V.
Iborra, Jose L.
机构
[1] Univ Murcia, Fac Quim, Dept Bioquim & Biol Mol B & Inmunol, E-30100 Murcia, Spain
[2] Univ Jaume 1, UAMOA, Dept Quim Inorgan & Organ, Castellon de La Plana 12071, Spain
[3] Chulalongkorn Univ, Fac Sci, Program Biotechnol, Bangkok 10330, Thailand
关键词
continuous processes; enzyme catalysis; green chemistry; supercritical fluids; supported ionic liquids;
D O I
10.1002/adsc.200600554
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Bioreactors with covalently supported ionic liquid phases (SILP) were prepared as polymeric monoliths based on styrene-divinylbenzene or 2-hydroxyethyl methacrylate-ethylene dimethacrylate, and with imidazolium units loadings ranging from 54.7 to 39.8 % wt IL per gram of polymer. The SILPs were able to absorb Candida antarctica lipase B (CALB), leading to highly efficient and robust heterogeneous biocatalysts. The bioreactors were prepared as macroporous monolithic mini-flow systems and tested for the continuous flow synthesis of citronellyl propionate in supercritical carbon dioxide (scCO(2)) by transesterification. The catalytic activity of these mini-flow-bioreactors remained practically unchanged for seven operational cycles of 5 h each in different supercritical conditions. The best results were obtained when the most hydrophobic monolith, M-SILP-8-CALB, was assayed at 80 degrees C and 10MPa, reaching a total turnover number (TON) of 35.8 x 10(4) mol product/mol enzyme. The results substantially exceeded those obtained for packed-bed reactors with supported silica-CALB-Si-4 catalyst under the same experimental conditions.
引用
收藏
页码:1077 / 1084
页数:8
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