Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution
Abstract 95.3% of the sucrose in a feed batch fermentation (300 g/L) was hydrolyzed by Leuconostoc mesenteroides subp. mesenteroides NRRL B-23188 glucansucrase. Further, the glucose of sucrose formed glucooligosaccharides (GOS) of degree of polymerization (DP) over 2, together with 91.6% of the malt...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Lee, Sun [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2016 |
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| Schlagwörter: |
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| Anmerkung: |
© The Korean Society for Biotechnology and Bioengineering and Springer-Verlag Berlin Heidelberg 2016 |
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| Übergeordnetes Werk: |
Enthalten in: Biotechnology and bioprocess engineering - Seoul : Society, 1996, 21(2016), 1 vom: Jan., Seite 39-45 |
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| Übergeordnetes Werk: |
volume:21 ; year:2016 ; number:1 ; month:01 ; pages:39-45 |
| Links: |
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| DOI / URN: |
10.1007/s12257-015-0587-x |
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| Katalog-ID: |
SPR024565024 |
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| 245 | 1 | 0 | |a Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution |
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| 520 | |a Abstract 95.3% of the sucrose in a feed batch fermentation (300 g/L) was hydrolyzed by Leuconostoc mesenteroides subp. mesenteroides NRRL B-23188 glucansucrase. Further, the glucose of sucrose formed glucooligosaccharides (GOS) of degree of polymerization (DP) over 2, together with 91.6% of the maltose (200 g/L). Lime saccharate (lime sucrate) was used to control the pH during fermentation. The GOS products had DP between 2 and 7. When Streptococcus mutans mutansucrase (0.1 U/mL) reacted with 0.1% sucrose, addition of 0.1 ~ 10% GOS to the mutansucrase reaction digest resulted in a 56 ~ 90% reduction of mutan formation. GOS also reduced E. coli (72.2%) and Salmonella sp. (over 40.0%) growth, when 2.5% GOS was used as a single carbon source, compared to growth using glucose. The calculated glycemic index and glycemic load of GOS was 8 and 1, respectively, based on a 10 g carbohydrate serving. GOS was calculated to have 2.43 kcal/g. After a glucose tolerance test was performed using C57BL/6 mice, we found that mice treated with GOS showed a 59.4% lower increase in plasma glucose than those treated with maltose. | ||
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| 650 | 4 | |a glucooligosaccharides |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a calcium hydroxide |7 (dpeaa)DE-He213 | |
| 700 | 1 | |a Hanh, Nguyen Thi Thanh |4 aut | |
| 700 | 1 | |a Cho, Jae-Young |4 aut | |
| 700 | 1 | |a Kim, Ji Youn |4 aut | |
| 700 | 1 | |a Moon, Young Hwan |4 aut | |
| 700 | 1 | |a Yeom, Su-Cheong |4 aut | |
| 700 | 1 | |a Kim, Geun-Joong |4 aut | |
| 700 | 1 | |a Kim, Doman |4 aut | |
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10.1007/s12257-015-0587-x doi (DE-627)SPR024565024 (SPR)s12257-015-0587-x-e DE-627 ger DE-627 rakwb eng Lee, Sun verfasserin aut Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution 2016 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Korean Society for Biotechnology and Bioengineering and Springer-Verlag Berlin Heidelberg 2016 Abstract 95.3% of the sucrose in a feed batch fermentation (300 g/L) was hydrolyzed by Leuconostoc mesenteroides subp. mesenteroides NRRL B-23188 glucansucrase. Further, the glucose of sucrose formed glucooligosaccharides (GOS) of degree of polymerization (DP) over 2, together with 91.6% of the maltose (200 g/L). Lime saccharate (lime sucrate) was used to control the pH during fermentation. The GOS products had DP between 2 and 7. When Streptococcus mutans mutansucrase (0.1 U/mL) reacted with 0.1% sucrose, addition of 0.1 ~ 10% GOS to the mutansucrase reaction digest resulted in a 56 ~ 90% reduction of mutan formation. GOS also reduced E. coli (72.2%) and Salmonella sp. (over 40.0%) growth, when 2.5% GOS was used as a single carbon source, compared to growth using glucose. The calculated glycemic index and glycemic load of GOS was 8 and 1, respectively, based on a 10 g carbohydrate serving. GOS was calculated to have 2.43 kcal/g. After a glucose tolerance test was performed using C57BL/6 mice, we found that mice treated with GOS showed a 59.4% lower increase in plasma glucose than those treated with maltose. glucansucrase (dpeaa)DE-He213 glucooligosaccharides (dpeaa)DE-He213 calcium hydroxide (dpeaa)DE-He213 Hanh, Nguyen Thi Thanh aut Cho, Jae-Young aut Kim, Ji Youn aut Moon, Young Hwan aut Yeom, Su-Cheong aut Kim, Geun-Joong aut Kim, Doman aut Enthalten in Biotechnology and bioprocess engineering Seoul : Society, 1996 21(2016), 1 vom: Jan., Seite 39-45 (DE-627)373321821 (DE-600)2125481-3 1976-3816 nnns volume:21 year:2016 number:1 month:01 pages:39-45 https://dx.doi.org/10.1007/s12257-015-0587-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 21 2016 1 01 39-45 |
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10.1007/s12257-015-0587-x doi (DE-627)SPR024565024 (SPR)s12257-015-0587-x-e DE-627 ger DE-627 rakwb eng Lee, Sun verfasserin aut Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution 2016 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Korean Society for Biotechnology and Bioengineering and Springer-Verlag Berlin Heidelberg 2016 Abstract 95.3% of the sucrose in a feed batch fermentation (300 g/L) was hydrolyzed by Leuconostoc mesenteroides subp. mesenteroides NRRL B-23188 glucansucrase. Further, the glucose of sucrose formed glucooligosaccharides (GOS) of degree of polymerization (DP) over 2, together with 91.6% of the maltose (200 g/L). Lime saccharate (lime sucrate) was used to control the pH during fermentation. The GOS products had DP between 2 and 7. When Streptococcus mutans mutansucrase (0.1 U/mL) reacted with 0.1% sucrose, addition of 0.1 ~ 10% GOS to the mutansucrase reaction digest resulted in a 56 ~ 90% reduction of mutan formation. GOS also reduced E. coli (72.2%) and Salmonella sp. (over 40.0%) growth, when 2.5% GOS was used as a single carbon source, compared to growth using glucose. The calculated glycemic index and glycemic load of GOS was 8 and 1, respectively, based on a 10 g carbohydrate serving. GOS was calculated to have 2.43 kcal/g. After a glucose tolerance test was performed using C57BL/6 mice, we found that mice treated with GOS showed a 59.4% lower increase in plasma glucose than those treated with maltose. glucansucrase (dpeaa)DE-He213 glucooligosaccharides (dpeaa)DE-He213 calcium hydroxide (dpeaa)DE-He213 Hanh, Nguyen Thi Thanh aut Cho, Jae-Young aut Kim, Ji Youn aut Moon, Young Hwan aut Yeom, Su-Cheong aut Kim, Geun-Joong aut Kim, Doman aut Enthalten in Biotechnology and bioprocess engineering Seoul : Society, 1996 21(2016), 1 vom: Jan., Seite 39-45 (DE-627)373321821 (DE-600)2125481-3 1976-3816 nnns volume:21 year:2016 number:1 month:01 pages:39-45 https://dx.doi.org/10.1007/s12257-015-0587-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 21 2016 1 01 39-45 |
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10.1007/s12257-015-0587-x doi (DE-627)SPR024565024 (SPR)s12257-015-0587-x-e DE-627 ger DE-627 rakwb eng Lee, Sun verfasserin aut Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution 2016 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Korean Society for Biotechnology and Bioengineering and Springer-Verlag Berlin Heidelberg 2016 Abstract 95.3% of the sucrose in a feed batch fermentation (300 g/L) was hydrolyzed by Leuconostoc mesenteroides subp. mesenteroides NRRL B-23188 glucansucrase. Further, the glucose of sucrose formed glucooligosaccharides (GOS) of degree of polymerization (DP) over 2, together with 91.6% of the maltose (200 g/L). Lime saccharate (lime sucrate) was used to control the pH during fermentation. The GOS products had DP between 2 and 7. When Streptococcus mutans mutansucrase (0.1 U/mL) reacted with 0.1% sucrose, addition of 0.1 ~ 10% GOS to the mutansucrase reaction digest resulted in a 56 ~ 90% reduction of mutan formation. GOS also reduced E. coli (72.2%) and Salmonella sp. (over 40.0%) growth, when 2.5% GOS was used as a single carbon source, compared to growth using glucose. The calculated glycemic index and glycemic load of GOS was 8 and 1, respectively, based on a 10 g carbohydrate serving. GOS was calculated to have 2.43 kcal/g. After a glucose tolerance test was performed using C57BL/6 mice, we found that mice treated with GOS showed a 59.4% lower increase in plasma glucose than those treated with maltose. glucansucrase (dpeaa)DE-He213 glucooligosaccharides (dpeaa)DE-He213 calcium hydroxide (dpeaa)DE-He213 Hanh, Nguyen Thi Thanh aut Cho, Jae-Young aut Kim, Ji Youn aut Moon, Young Hwan aut Yeom, Su-Cheong aut Kim, Geun-Joong aut Kim, Doman aut Enthalten in Biotechnology and bioprocess engineering Seoul : Society, 1996 21(2016), 1 vom: Jan., Seite 39-45 (DE-627)373321821 (DE-600)2125481-3 1976-3816 nnns volume:21 year:2016 number:1 month:01 pages:39-45 https://dx.doi.org/10.1007/s12257-015-0587-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 21 2016 1 01 39-45 |
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10.1007/s12257-015-0587-x doi (DE-627)SPR024565024 (SPR)s12257-015-0587-x-e DE-627 ger DE-627 rakwb eng Lee, Sun verfasserin aut Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution 2016 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Korean Society for Biotechnology and Bioengineering and Springer-Verlag Berlin Heidelberg 2016 Abstract 95.3% of the sucrose in a feed batch fermentation (300 g/L) was hydrolyzed by Leuconostoc mesenteroides subp. mesenteroides NRRL B-23188 glucansucrase. Further, the glucose of sucrose formed glucooligosaccharides (GOS) of degree of polymerization (DP) over 2, together with 91.6% of the maltose (200 g/L). Lime saccharate (lime sucrate) was used to control the pH during fermentation. The GOS products had DP between 2 and 7. When Streptococcus mutans mutansucrase (0.1 U/mL) reacted with 0.1% sucrose, addition of 0.1 ~ 10% GOS to the mutansucrase reaction digest resulted in a 56 ~ 90% reduction of mutan formation. GOS also reduced E. coli (72.2%) and Salmonella sp. (over 40.0%) growth, when 2.5% GOS was used as a single carbon source, compared to growth using glucose. The calculated glycemic index and glycemic load of GOS was 8 and 1, respectively, based on a 10 g carbohydrate serving. GOS was calculated to have 2.43 kcal/g. After a glucose tolerance test was performed using C57BL/6 mice, we found that mice treated with GOS showed a 59.4% lower increase in plasma glucose than those treated with maltose. glucansucrase (dpeaa)DE-He213 glucooligosaccharides (dpeaa)DE-He213 calcium hydroxide (dpeaa)DE-He213 Hanh, Nguyen Thi Thanh aut Cho, Jae-Young aut Kim, Ji Youn aut Moon, Young Hwan aut Yeom, Su-Cheong aut Kim, Geun-Joong aut Kim, Doman aut Enthalten in Biotechnology and bioprocess engineering Seoul : Society, 1996 21(2016), 1 vom: Jan., Seite 39-45 (DE-627)373321821 (DE-600)2125481-3 1976-3816 nnns volume:21 year:2016 number:1 month:01 pages:39-45 https://dx.doi.org/10.1007/s12257-015-0587-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 21 2016 1 01 39-45 |
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10.1007/s12257-015-0587-x doi (DE-627)SPR024565024 (SPR)s12257-015-0587-x-e DE-627 ger DE-627 rakwb eng Lee, Sun verfasserin aut Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution 2016 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Korean Society for Biotechnology and Bioengineering and Springer-Verlag Berlin Heidelberg 2016 Abstract 95.3% of the sucrose in a feed batch fermentation (300 g/L) was hydrolyzed by Leuconostoc mesenteroides subp. mesenteroides NRRL B-23188 glucansucrase. Further, the glucose of sucrose formed glucooligosaccharides (GOS) of degree of polymerization (DP) over 2, together with 91.6% of the maltose (200 g/L). Lime saccharate (lime sucrate) was used to control the pH during fermentation. The GOS products had DP between 2 and 7. When Streptococcus mutans mutansucrase (0.1 U/mL) reacted with 0.1% sucrose, addition of 0.1 ~ 10% GOS to the mutansucrase reaction digest resulted in a 56 ~ 90% reduction of mutan formation. GOS also reduced E. coli (72.2%) and Salmonella sp. (over 40.0%) growth, when 2.5% GOS was used as a single carbon source, compared to growth using glucose. The calculated glycemic index and glycemic load of GOS was 8 and 1, respectively, based on a 10 g carbohydrate serving. GOS was calculated to have 2.43 kcal/g. After a glucose tolerance test was performed using C57BL/6 mice, we found that mice treated with GOS showed a 59.4% lower increase in plasma glucose than those treated with maltose. glucansucrase (dpeaa)DE-He213 glucooligosaccharides (dpeaa)DE-He213 calcium hydroxide (dpeaa)DE-He213 Hanh, Nguyen Thi Thanh aut Cho, Jae-Young aut Kim, Ji Youn aut Moon, Young Hwan aut Yeom, Su-Cheong aut Kim, Geun-Joong aut Kim, Doman aut Enthalten in Biotechnology and bioprocess engineering Seoul : Society, 1996 21(2016), 1 vom: Jan., Seite 39-45 (DE-627)373321821 (DE-600)2125481-3 1976-3816 nnns volume:21 year:2016 number:1 month:01 pages:39-45 https://dx.doi.org/10.1007/s12257-015-0587-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 21 2016 1 01 39-45 |
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Lee, Sun @@aut@@ Hanh, Nguyen Thi Thanh @@aut@@ Cho, Jae-Young @@aut@@ Kim, Ji Youn @@aut@@ Moon, Young Hwan @@aut@@ Yeom, Su-Cheong @@aut@@ Kim, Geun-Joong @@aut@@ Kim, Doman @@aut@@ |
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<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a22002652 4500</leader><controlfield tag="001">SPR024565024</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230519072159.0</controlfield><controlfield tag="007">cr uuu---uuuuu</controlfield><controlfield tag="008">201007s2016 xx |||||o 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1007/s12257-015-0587-x</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)SPR024565024</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(SPR)s12257-015-0587-x-e</subfield></datafield><datafield tag="040" ind1=" " ind2=" "><subfield code="a">DE-627</subfield><subfield code="b">ger</subfield><subfield code="c">DE-627</subfield><subfield code="e">rakwb</subfield></datafield><datafield tag="041" ind1=" " ind2=" "><subfield code="a">eng</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Lee, Sun</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2016</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">Computermedien</subfield><subfield code="b">c</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Online-Ressource</subfield><subfield code="b">cr</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="500" ind1=" " ind2=" "><subfield code="a">© The Korean Society for Biotechnology and Bioengineering and Springer-Verlag Berlin Heidelberg 2016</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract 95.3% of the sucrose in a feed batch fermentation (300 g/L) was hydrolyzed by Leuconostoc mesenteroides subp. mesenteroides NRRL B-23188 glucansucrase. Further, the glucose of sucrose formed glucooligosaccharides (GOS) of degree of polymerization (DP) over 2, together with 91.6% of the maltose (200 g/L). Lime saccharate (lime sucrate) was used to control the pH during fermentation. The GOS products had DP between 2 and 7. When Streptococcus mutans mutansucrase (0.1 U/mL) reacted with 0.1% sucrose, addition of 0.1 ~ 10% GOS to the mutansucrase reaction digest resulted in a 56 ~ 90% reduction of mutan formation. GOS also reduced E. coli (72.2%) and Salmonella sp. (over 40.0%) growth, when 2.5% GOS was used as a single carbon source, compared to growth using glucose. The calculated glycemic index and glycemic load of GOS was 8 and 1, respectively, based on a 10 g carbohydrate serving. GOS was calculated to have 2.43 kcal/g. 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Lee, Sun |
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Lee, Sun misc glucansucrase misc glucooligosaccharides misc calcium hydroxide Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution |
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Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution glucansucrase (dpeaa)DE-He213 glucooligosaccharides (dpeaa)DE-He213 calcium hydroxide (dpeaa)DE-He213 |
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glucooligosaccharide production by leuconostoc mesenteroides fermentation with efficient ph control, using a calcium hydroxide-sucrose solution |
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Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution |
| abstract |
Abstract 95.3% of the sucrose in a feed batch fermentation (300 g/L) was hydrolyzed by Leuconostoc mesenteroides subp. mesenteroides NRRL B-23188 glucansucrase. Further, the glucose of sucrose formed glucooligosaccharides (GOS) of degree of polymerization (DP) over 2, together with 91.6% of the maltose (200 g/L). Lime saccharate (lime sucrate) was used to control the pH during fermentation. The GOS products had DP between 2 and 7. When Streptococcus mutans mutansucrase (0.1 U/mL) reacted with 0.1% sucrose, addition of 0.1 ~ 10% GOS to the mutansucrase reaction digest resulted in a 56 ~ 90% reduction of mutan formation. GOS also reduced E. coli (72.2%) and Salmonella sp. (over 40.0%) growth, when 2.5% GOS was used as a single carbon source, compared to growth using glucose. The calculated glycemic index and glycemic load of GOS was 8 and 1, respectively, based on a 10 g carbohydrate serving. GOS was calculated to have 2.43 kcal/g. After a glucose tolerance test was performed using C57BL/6 mice, we found that mice treated with GOS showed a 59.4% lower increase in plasma glucose than those treated with maltose. © The Korean Society for Biotechnology and Bioengineering and Springer-Verlag Berlin Heidelberg 2016 |
| abstractGer |
Abstract 95.3% of the sucrose in a feed batch fermentation (300 g/L) was hydrolyzed by Leuconostoc mesenteroides subp. mesenteroides NRRL B-23188 glucansucrase. Further, the glucose of sucrose formed glucooligosaccharides (GOS) of degree of polymerization (DP) over 2, together with 91.6% of the maltose (200 g/L). Lime saccharate (lime sucrate) was used to control the pH during fermentation. The GOS products had DP between 2 and 7. When Streptococcus mutans mutansucrase (0.1 U/mL) reacted with 0.1% sucrose, addition of 0.1 ~ 10% GOS to the mutansucrase reaction digest resulted in a 56 ~ 90% reduction of mutan formation. GOS also reduced E. coli (72.2%) and Salmonella sp. (over 40.0%) growth, when 2.5% GOS was used as a single carbon source, compared to growth using glucose. The calculated glycemic index and glycemic load of GOS was 8 and 1, respectively, based on a 10 g carbohydrate serving. GOS was calculated to have 2.43 kcal/g. After a glucose tolerance test was performed using C57BL/6 mice, we found that mice treated with GOS showed a 59.4% lower increase in plasma glucose than those treated with maltose. © The Korean Society for Biotechnology and Bioengineering and Springer-Verlag Berlin Heidelberg 2016 |
| abstract_unstemmed |
Abstract 95.3% of the sucrose in a feed batch fermentation (300 g/L) was hydrolyzed by Leuconostoc mesenteroides subp. mesenteroides NRRL B-23188 glucansucrase. Further, the glucose of sucrose formed glucooligosaccharides (GOS) of degree of polymerization (DP) over 2, together with 91.6% of the maltose (200 g/L). Lime saccharate (lime sucrate) was used to control the pH during fermentation. The GOS products had DP between 2 and 7. When Streptococcus mutans mutansucrase (0.1 U/mL) reacted with 0.1% sucrose, addition of 0.1 ~ 10% GOS to the mutansucrase reaction digest resulted in a 56 ~ 90% reduction of mutan formation. GOS also reduced E. coli (72.2%) and Salmonella sp. (over 40.0%) growth, when 2.5% GOS was used as a single carbon source, compared to growth using glucose. The calculated glycemic index and glycemic load of GOS was 8 and 1, respectively, based on a 10 g carbohydrate serving. GOS was calculated to have 2.43 kcal/g. After a glucose tolerance test was performed using C57BL/6 mice, we found that mice treated with GOS showed a 59.4% lower increase in plasma glucose than those treated with maltose. © The Korean Society for Biotechnology and Bioengineering and Springer-Verlag Berlin Heidelberg 2016 |
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Glucooligosaccharide production by Leuconostoc mesenteroides fermentation with efficient pH control, using a calcium hydroxide-sucrose solution |
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Hanh, Nguyen Thi Thanh Cho, Jae-Young Kim, Ji Youn Moon, Young Hwan Yeom, Su-Cheong Kim, Geun-Joong Kim, Doman |
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Hanh, Nguyen Thi Thanh Cho, Jae-Young Kim, Ji Youn Moon, Young Hwan Yeom, Su-Cheong Kim, Geun-Joong Kim, Doman |
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10.1007/s12257-015-0587-x |
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2024-07-04T01:28:36.086Z |
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| score |
7.4011555 |