PeniciUium purpurogenum Li-3, a fungus producing β-glucuronidase (PGUS), can con- vert glycyrrhizin (GL) to glycyrrhetinic acid monoglucuronide (GAMG) when grown in medium with GL as the sole carbon source. In ...PeniciUium purpurogenum Li-3, a fungus producing β-glucuronidase (PGUS), can con- vert glycyrrhizin (GL) to glycyrrhetinic acid monoglucuronide (GAMG) when grown in medium with GL as the sole carbon source. In order to improve the conversion rate of GL and the yield of GAMG, licorice extract (LE) was added as an inducer to enhance the production of GAMG by the PGUS. In this work, the influence of LE on the conversion rate of GL to GAMG was studied. When the Penicil- lium purpurogenum Li-3 was grown in the medium containing LE and GL ( concentration ratio of LE to GL was 2: 3), the conversion rate of GL was 84. 12% with 38. 18% increase and the yield of GAMG was 80. 47% with 37. 18% increase, comparing with to the medium only containing GL at 48 h. The enzyme activity of ^-glucuronidase was also enhanced from 22. 4 U/mL to 82.3 U/mL, which in- creased up to about 3. 67 fold. The results showed that LE could significantly improve the induced expression level of PGUS.展开更多
Glycyrrhetic acid 3-O-mono-β-D-glucuronide (GAMG), the major functional ingredient in licorice, has widespread applications in food, pharmacy and cosmetics industry. The production of GAMG through Penicillium purpu...Glycyrrhetic acid 3-O-mono-β-D-glucuronide (GAMG), the major functional ingredient in licorice, has widespread applications in food, pharmacy and cosmetics industry. The production of GAMG through Penicillium purpurogenum Li-3 cultivation was for the first time performed through both batch and fed-batch processes in bioreactors. In batch process, under optimal conditions (pH 5.0, temperature 32℃, agitation speed 100 r. rain 1), 3.55 g. L^-1 GAMG was obtained in a 2.5 L fermentor. To further enhance GAMG production, a fine fed-batch process was developed by using pH and DO as feedback parameters. Starting from 48 h, 100 m190 g-L 1 substrate Glycyrrhizin (GL) was fed each time when pH increased to above 5.0 and DO was increased to above 80%. This strategy can significantly enhance GAMG production: the achieved GL conversion was 95.34% with GAMG yield of 95.15%, and GAMG concentration was 16.62 g. L^-1 which was 5 times higher than that of batch. Then, a two-step separation strat- egy was established to separate GAMG from fermentation broth by crude extraction of 15 ml column packed with D10I resin followed by fine purification with preparative C18 chromatography. The obtained GAMG purity was 95.79%. This study provides a new insight into the industrial bioprocess of high-level GAMG production.展开更多
基金Supported by the National Science Foundation of China(21276024,21276025)National High-Tech Research and Development Program of China("863"Program)(2012AA02A704)
文摘PeniciUium purpurogenum Li-3, a fungus producing β-glucuronidase (PGUS), can con- vert glycyrrhizin (GL) to glycyrrhetinic acid monoglucuronide (GAMG) when grown in medium with GL as the sole carbon source. In order to improve the conversion rate of GL and the yield of GAMG, licorice extract (LE) was added as an inducer to enhance the production of GAMG by the PGUS. In this work, the influence of LE on the conversion rate of GL to GAMG was studied. When the Penicil- lium purpurogenum Li-3 was grown in the medium containing LE and GL ( concentration ratio of LE to GL was 2: 3), the conversion rate of GL was 84. 12% with 38. 18% increase and the yield of GAMG was 80. 47% with 37. 18% increase, comparing with to the medium only containing GL at 48 h. The enzyme activity of ^-glucuronidase was also enhanced from 22. 4 U/mL to 82.3 U/mL, which in- creased up to about 3. 67 fold. The results showed that LE could significantly improve the induced expression level of PGUS.
基金Supported by the National Natural Science Foundation of China(21176028 and21506011)the National Science Fund for Distinguished Young Scholars of China(21425624)Doctoral Fund of Ministry of Education of China(20121101110050)
文摘Glycyrrhetic acid 3-O-mono-β-D-glucuronide (GAMG), the major functional ingredient in licorice, has widespread applications in food, pharmacy and cosmetics industry. The production of GAMG through Penicillium purpurogenum Li-3 cultivation was for the first time performed through both batch and fed-batch processes in bioreactors. In batch process, under optimal conditions (pH 5.0, temperature 32℃, agitation speed 100 r. rain 1), 3.55 g. L^-1 GAMG was obtained in a 2.5 L fermentor. To further enhance GAMG production, a fine fed-batch process was developed by using pH and DO as feedback parameters. Starting from 48 h, 100 m190 g-L 1 substrate Glycyrrhizin (GL) was fed each time when pH increased to above 5.0 and DO was increased to above 80%. This strategy can significantly enhance GAMG production: the achieved GL conversion was 95.34% with GAMG yield of 95.15%, and GAMG concentration was 16.62 g. L^-1 which was 5 times higher than that of batch. Then, a two-step separation strat- egy was established to separate GAMG from fermentation broth by crude extraction of 15 ml column packed with D10I resin followed by fine purification with preparative C18 chromatography. The obtained GAMG purity was 95.79%. This study provides a new insight into the industrial bioprocess of high-level GAMG production.