Biosynthesis of glycyrrhetic acid 3-O-mono-β-D-glucuronide by whole cell in ionic liquid/water biphasic system
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Biosynthesis of glycyrrhetic acid 3-O-mono-β-D-glucuronide by whole cell in ionic liquid/water biphasic system
CIESC JournalIssue 11, Pages: 3136-3142(2011)
作者机构:
1. 石河子大学化学化工学院
2. 北京理工大学生命学院
3. 浙江工业大学生物工程研究所
作者简介:
基金信息:
DOI:
CLC:0.3969/j.issn.0438-1157.2011.11.023
Online First:05 November 2011,
Published:05 November 2011
稿件说明:
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CHEN Jinyan, ZOU Shuping, HE Dongmei, et al. Biosynthesis of glycyrrhetic acid 3-O-mono-β-D-glucuronide by whole cell in ionic liquid/water biphasic system[J]. CIESC Journal, 2011, (11): 3136-3142.
DOI:
CHEN Jinyan, ZOU Shuping, HE Dongmei, et al. Biosynthesis of glycyrrhetic acid 3-O-mono-β-D-glucuronide by whole cell in ionic liquid/water biphasic system[J]. CIESC Journal, 2011, (11): 3136-3142.DOI:
Biosynthesis of glycyrrhetic acid 3-O-mono-β-D-glucuronide by whole cell in ionic liquid/water biphasic system
can be hydrolysed to glycyrrhetic acid 3-O-mono-β-D-glucuronide (GAMG)by whole cells containing β-D-glucuronidase. GAMG is widely used in the pharmaceutical and food industries due to its stronger physiological functions
higher biological activity
more favorable sweetness
and lower caloric value as compared with GL. The recombinant Pichia pastoris (r-PGUS-P)designated in this work expressing β-D-glucuronidase
was used as a whole-cell biocatalyst catalyzing GL to GAMG in non-aqueous solvents systems. The results showed that r-PGUS-P gave the highest yield of GAMG in 1-butyl-3-methylimidazolium hexafluorophosphate ([BMIM]PF6)/water(2∶8
vol)biphasic system. The optimal conditions of this reaction were determined as follows:optimum pH
substrate concentration
temperature and cell content were 5.4
6.0 mmol·L-1
45℃
and 8.0 g·L-1
respectively. Under these optimized conditions
69.6% yield of GAMG and 67.2% of the chemical bond selectivity was achieved after 58 h reaction time
increase by 12.4% and 12.61%
respectively against aqueous phase. Simultaneously
the ionic liquid [BMIM]PF6 alsoremained at higher recovery percentage of about 93.47% during repeated use for 7 reaction cycles. Especially
product GAMG and byproduct glycyrrhetinic acid (GA)got separated in biphasic system automatically that brought convenience for the separation and purification of GAMG.