Fed-batch bioconversion of indene to cis-indandiol

被引:15
作者
Amanullah, A
Hewitt, CJ
Nienow, AW
Lee, C
Chartrain, M
Buckland, BC
Drew, SW
Woodley, JM
机构
[1] Merck & Co Inc, Merck Res Labs, Dept Bioproc R&D, West Point, PA 19486 USA
[2] UCL, Adv Ctr Biochem Engn, Dept Biochem Engn, London WC1E 7JE, England
[3] Univ Birmingham, Sch Chem Engn, Ctr Bioproc Engn, Birmingham B15 2TT, W Midlands, England
关键词
indene; cis-indandiol; fed-batch bioconversion; flow cytometry; Rhodococcus; HIV protease inhibitor;
D O I
10.1016/S0141-0229(02)00183-7
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 bioconversion of indene to cis-(1S,2R) indandiol, a key intermediate in the synthesis of Merck's HIV protease inhibitor, CRIXIVAN(TM) can be achieved during the growth of a Rhodococcus strain. In a previous study, we reported on the application of multi-parameter flow cytometry for the measurement of indene toxicity to the strain, and found that concentrations up to 0.25 g/l of indene (0.037 g indene/g dry cell weight) in batch bioconversions did not influence cell physiology. Using this information, this study reports on the implementation of a single phase indene fed-batch bioconversion. Cytoplasmic membrane (membrane) integrity and membrane polarisation of a large number of cells were measured during such bioconversions using multi-parameter flow cytometry and compared to a control in order to assess any toxic effects of indene feeding. The results indicate that indene supply at a rate of 0.1 g/l/h is feasible without any deleterious effects on cell physiology. The delay in indene metabolism was significantly shorter, with lower concentrations of by-product formation, when it was added to the culture in the stationary phase than when it was added at the beginning of the exponential phase of the fermentation. cis-Indandiol production rates could be enhanced from 20 mg/l/h, in a previously reported silicone oil two-liquid phase system, up to 200 mg/l/h by a combination of suitable indene feeding rates in the stationary phase and operating with a high biomass concentration to limit the effects of toxicity. In addition, the yield of cis-indandiol on indene (g/g) was higher at 0.48 in the single phase system compared to 0.20 in the two-liquid phase system. However, the final concentration of cis-indandiol was considerably lower, possibly as a result of higher dehydrogenase activity resulting in an increased transformation of cis-indandiol to 1-keto-2-hydroxy indan. This study has demonstrated that it is feasible to feed indene directly in the stationary phase of the bioconversion using high biomass concentrations to obtain enhanced cis-indandiol formation rates as well as yields based on indene utilisation compared to a two-phase silicone oil system. (C) 2002 Elsevier Science Inc. All rights reserved.
引用
收藏
页码:954 / 967
页数:14
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