Loading…
Synthesis of Lactulose in Continuous Stirred Tank Reactor With β-Galactosidase of Apergillus oryzae Immobilized in Monofunctional Glyoxyl Agarose Support
Lactulose synthesis from fructose and lactose in continuous stirred tank (CSTR) reactor operation with glyoxyl-agarose immobilized Aspergillus oryzae β-galactosidase is reported for the first time. The effect of operational variables: inlet concentrations of sugar substrates, temperature, feed subst...
Saved in:
Published in: | Frontiers in bioengineering and biotechnology 2020-06, Vol.8, p.699-699 |
---|---|
Main Authors: | , , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
cited_by | cdi_FETCH-LOGICAL-c439t-98f6a8cdf721719595dbbd7aaefa264391afd5f971df7376f7f4dadf98afd5f13 |
---|---|
cites | cdi_FETCH-LOGICAL-c439t-98f6a8cdf721719595dbbd7aaefa264391afd5f971df7376f7f4dadf98afd5f13 |
container_end_page | 699 |
container_issue | |
container_start_page | 699 |
container_title | Frontiers in bioengineering and biotechnology |
container_volume | 8 |
creator | Ubilla, Claudia Ramírez, Nicolás Valdivia, Felipe Vera, Carlos Illanes, Andrés Guerrero, Cecilia |
description | Lactulose synthesis from fructose and lactose in continuous stirred tank (CSTR) reactor operation with glyoxyl-agarose immobilized
Aspergillus oryzae
β-galactosidase is reported for the first time. The effect of operational variables: inlet concentrations of sugar substrates, temperature, feed substrate molar ratio, enzyme loading and feed flow rate was studied on reactor performance. Even though the variation of each one affected to a certain extent lactulose yield (Y
Lactulose
), specific productivity (π
Lactulose
) and selectivity of the reaction (lactulose/transgalactosylated oligosaccharides molar ratio) (S
Lu/TOS
), the most significant effects were obtained by varying the inlet concentrations of sugar substrates and the feed substrate molar ratio. Maximum Y
Lactulose
of 0.54 g⋅g
–1
was obtained at 50°C, pH 4.5, 50% w/w inlet concentrations of sugar substrates, feed flowrate of 12 mL⋅min
–1
, fructose/lactose molar ratio of 8 and reactor enzyme load of 29.06 IU
H
⋅mL
–1
. At such conditions S
Lu/TOS
was 3.7, lactose conversion (X
Lactose
) was 0.39 and total transgalactosylation yield was 0.762 g⋅g
–1
, meaning that 76% of the reacted lactose corresponded to transgalactosylation and 24% to hydrolysis, which is a definite advantage of this mode of operation. Even though X
Lactose
in CSTR was lower than in other reported modes of operation for lactulose synthesis, transgalactosylation was more favored over hydrolysis which reduced the inhibitory effect of galactose on β-galactosidase. |
doi_str_mv | 10.3389/fbioe.2020.00699 |
format | article |
fullrecord | <record><control><sourceid>proquest_doaj_</sourceid><recordid>TN_cdi_doaj_primary_oai_doaj_org_article_2afbc2591252448991fd7fde7a5324f5</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><doaj_id>oai_doaj_org_article_2afbc2591252448991fd7fde7a5324f5</doaj_id><sourcerecordid>2426174514</sourcerecordid><originalsourceid>FETCH-LOGICAL-c439t-98f6a8cdf721719595dbbd7aaefa264391afd5f971df7376f7f4dadf98afd5f13</originalsourceid><addsrcrecordid>eNpVksFuEzEQhlcIRKvSO0cfuWxYe9fr9QUpiiBECkIiRRyt2bWduHjtYHsr0kfhMfogfSacpEL0ZOuff76RZv6ieIurWV13_L3ujVczUpFqVlUt5y-KS0J4Wza4oy__-18U1zHeVlWFCWW0I6-Li5q0nLK2uyz-bA4u7VQ0EXmN1jCkyfqokHFo4V0ybvJTRJtkQlAS3YD7ib6p7PIB_TBphx4fyiXYoxCNhNyYKfO9CltjbW704XAPCq3G0ffGmvvMyOQv3nk9uSEZ78CipT343weL5lsIx9mbab_3Ib0pXmmwUV0_vVfF908fbxafy_XX5WoxX5dDU_NU8k630A1SM4IZ5pRT2feSASgNpM0WDFpSzRnOlpq1mulGgtS8O-m4vipWZ670cCv2wYwQDsKDESfBh62AkMxglSCg-4FQnjdJmqbjHGvJtFQMaE0aTTPrw5m1n_pRyUG5FMA-gz6vOLMTW38nWD5pjY-Ad0-A4H9NKiYxmjgoa8GpfAlBGtJi1lDcZGt1tg55azEo_W8MrsQxIeKUEHFMiDglpP4L_km0Ug</addsrcrecordid><sourcetype>Open Website</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2426174514</pqid></control><display><type>article</type><title>Synthesis of Lactulose in Continuous Stirred Tank Reactor With β-Galactosidase of Apergillus oryzae Immobilized in Monofunctional Glyoxyl Agarose Support</title><source>PubMed Central</source><creator>Ubilla, Claudia ; Ramírez, Nicolás ; Valdivia, Felipe ; Vera, Carlos ; Illanes, Andrés ; Guerrero, Cecilia</creator><creatorcontrib>Ubilla, Claudia ; Ramírez, Nicolás ; Valdivia, Felipe ; Vera, Carlos ; Illanes, Andrés ; Guerrero, Cecilia</creatorcontrib><description>Lactulose synthesis from fructose and lactose in continuous stirred tank (CSTR) reactor operation with glyoxyl-agarose immobilized
Aspergillus oryzae
β-galactosidase is reported for the first time. The effect of operational variables: inlet concentrations of sugar substrates, temperature, feed substrate molar ratio, enzyme loading and feed flow rate was studied on reactor performance. Even though the variation of each one affected to a certain extent lactulose yield (Y
Lactulose
), specific productivity (π
Lactulose
) and selectivity of the reaction (lactulose/transgalactosylated oligosaccharides molar ratio) (S
Lu/TOS
), the most significant effects were obtained by varying the inlet concentrations of sugar substrates and the feed substrate molar ratio. Maximum Y
Lactulose
of 0.54 g⋅g
–1
was obtained at 50°C, pH 4.5, 50% w/w inlet concentrations of sugar substrates, feed flowrate of 12 mL⋅min
–1
, fructose/lactose molar ratio of 8 and reactor enzyme load of 29.06 IU
H
⋅mL
–1
. At such conditions S
Lu/TOS
was 3.7, lactose conversion (X
Lactose
) was 0.39 and total transgalactosylation yield was 0.762 g⋅g
–1
, meaning that 76% of the reacted lactose corresponded to transgalactosylation and 24% to hydrolysis, which is a definite advantage of this mode of operation. Even though X
Lactose
in CSTR was lower than in other reported modes of operation for lactulose synthesis, transgalactosylation was more favored over hydrolysis which reduced the inhibitory effect of galactose on β-galactosidase.</description><identifier>ISSN: 2296-4185</identifier><identifier>EISSN: 2296-4185</identifier><identifier>DOI: 10.3389/fbioe.2020.00699</identifier><identifier>PMID: 32695768</identifier><language>eng</language><publisher>Frontiers Media S.A</publisher><subject>agarose support ; Bioengineering and Biotechnology ; galacto-oligossacharides ; immobilization ; lactulose ; prebiotic ; β-galactosidase</subject><ispartof>Frontiers in bioengineering and biotechnology, 2020-06, Vol.8, p.699-699</ispartof><rights>Copyright © 2020 Ubilla, Ramírez, Valdivia, Vera, Illanes and Guerrero. 2020 Ubilla, Ramírez, Valdivia, Vera, Illanes and Guerrero</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c439t-98f6a8cdf721719595dbbd7aaefa264391afd5f971df7376f7f4dadf98afd5f13</citedby><cites>FETCH-LOGICAL-c439t-98f6a8cdf721719595dbbd7aaefa264391afd5f971df7376f7f4dadf98afd5f13</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC7338315/pdf/$$EPDF$$P50$$Gpubmedcentral$$Hfree_for_read</linktopdf><linktohtml>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC7338315/$$EHTML$$P50$$Gpubmedcentral$$Hfree_for_read</linktohtml><link.rule.ids>230,314,727,780,784,885,27923,27924,53790,53792</link.rule.ids></links><search><creatorcontrib>Ubilla, Claudia</creatorcontrib><creatorcontrib>Ramírez, Nicolás</creatorcontrib><creatorcontrib>Valdivia, Felipe</creatorcontrib><creatorcontrib>Vera, Carlos</creatorcontrib><creatorcontrib>Illanes, Andrés</creatorcontrib><creatorcontrib>Guerrero, Cecilia</creatorcontrib><title>Synthesis of Lactulose in Continuous Stirred Tank Reactor With β-Galactosidase of Apergillus oryzae Immobilized in Monofunctional Glyoxyl Agarose Support</title><title>Frontiers in bioengineering and biotechnology</title><description>Lactulose synthesis from fructose and lactose in continuous stirred tank (CSTR) reactor operation with glyoxyl-agarose immobilized
Aspergillus oryzae
β-galactosidase is reported for the first time. The effect of operational variables: inlet concentrations of sugar substrates, temperature, feed substrate molar ratio, enzyme loading and feed flow rate was studied on reactor performance. Even though the variation of each one affected to a certain extent lactulose yield (Y
Lactulose
), specific productivity (π
Lactulose
) and selectivity of the reaction (lactulose/transgalactosylated oligosaccharides molar ratio) (S
Lu/TOS
), the most significant effects were obtained by varying the inlet concentrations of sugar substrates and the feed substrate molar ratio. Maximum Y
Lactulose
of 0.54 g⋅g
–1
was obtained at 50°C, pH 4.5, 50% w/w inlet concentrations of sugar substrates, feed flowrate of 12 mL⋅min
–1
, fructose/lactose molar ratio of 8 and reactor enzyme load of 29.06 IU
H
⋅mL
–1
. At such conditions S
Lu/TOS
was 3.7, lactose conversion (X
Lactose
) was 0.39 and total transgalactosylation yield was 0.762 g⋅g
–1
, meaning that 76% of the reacted lactose corresponded to transgalactosylation and 24% to hydrolysis, which is a definite advantage of this mode of operation. Even though X
Lactose
in CSTR was lower than in other reported modes of operation for lactulose synthesis, transgalactosylation was more favored over hydrolysis which reduced the inhibitory effect of galactose on β-galactosidase.</description><subject>agarose support</subject><subject>Bioengineering and Biotechnology</subject><subject>galacto-oligossacharides</subject><subject>immobilization</subject><subject>lactulose</subject><subject>prebiotic</subject><subject>β-galactosidase</subject><issn>2296-4185</issn><issn>2296-4185</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><sourceid>DOA</sourceid><recordid>eNpVksFuEzEQhlcIRKvSO0cfuWxYe9fr9QUpiiBECkIiRRyt2bWduHjtYHsr0kfhMfogfSacpEL0ZOuff76RZv6ieIurWV13_L3ujVczUpFqVlUt5y-KS0J4Wza4oy__-18U1zHeVlWFCWW0I6-Li5q0nLK2uyz-bA4u7VQ0EXmN1jCkyfqokHFo4V0ybvJTRJtkQlAS3YD7ib6p7PIB_TBphx4fyiXYoxCNhNyYKfO9CltjbW704XAPCq3G0ffGmvvMyOQv3nk9uSEZ78CipT343weL5lsIx9mbab_3Ib0pXmmwUV0_vVfF908fbxafy_XX5WoxX5dDU_NU8k630A1SM4IZ5pRT2feSASgNpM0WDFpSzRnOlpq1mulGgtS8O-m4vipWZ670cCv2wYwQDsKDESfBh62AkMxglSCg-4FQnjdJmqbjHGvJtFQMaE0aTTPrw5m1n_pRyUG5FMA-gz6vOLMTW38nWD5pjY-Ad0-A4H9NKiYxmjgoa8GpfAlBGtJi1lDcZGt1tg55azEo_W8MrsQxIeKUEHFMiDglpP4L_km0Ug</recordid><startdate>20200630</startdate><enddate>20200630</enddate><creator>Ubilla, Claudia</creator><creator>Ramírez, Nicolás</creator><creator>Valdivia, Felipe</creator><creator>Vera, Carlos</creator><creator>Illanes, Andrés</creator><creator>Guerrero, Cecilia</creator><general>Frontiers Media S.A</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7X8</scope><scope>5PM</scope><scope>DOA</scope></search><sort><creationdate>20200630</creationdate><title>Synthesis of Lactulose in Continuous Stirred Tank Reactor With β-Galactosidase of Apergillus oryzae Immobilized in Monofunctional Glyoxyl Agarose Support</title><author>Ubilla, Claudia ; Ramírez, Nicolás ; Valdivia, Felipe ; Vera, Carlos ; Illanes, Andrés ; Guerrero, Cecilia</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c439t-98f6a8cdf721719595dbbd7aaefa264391afd5f971df7376f7f4dadf98afd5f13</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>agarose support</topic><topic>Bioengineering and Biotechnology</topic><topic>galacto-oligossacharides</topic><topic>immobilization</topic><topic>lactulose</topic><topic>prebiotic</topic><topic>β-galactosidase</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ubilla, Claudia</creatorcontrib><creatorcontrib>Ramírez, Nicolás</creatorcontrib><creatorcontrib>Valdivia, Felipe</creatorcontrib><creatorcontrib>Vera, Carlos</creatorcontrib><creatorcontrib>Illanes, Andrés</creatorcontrib><creatorcontrib>Guerrero, Cecilia</creatorcontrib><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><collection>PubMed Central (Full Participant titles)</collection><collection>DOAJ Directory of Open Access Journals</collection><jtitle>Frontiers in bioengineering and biotechnology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ubilla, Claudia</au><au>Ramírez, Nicolás</au><au>Valdivia, Felipe</au><au>Vera, Carlos</au><au>Illanes, Andrés</au><au>Guerrero, Cecilia</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Synthesis of Lactulose in Continuous Stirred Tank Reactor With β-Galactosidase of Apergillus oryzae Immobilized in Monofunctional Glyoxyl Agarose Support</atitle><jtitle>Frontiers in bioengineering and biotechnology</jtitle><date>2020-06-30</date><risdate>2020</risdate><volume>8</volume><spage>699</spage><epage>699</epage><pages>699-699</pages><issn>2296-4185</issn><eissn>2296-4185</eissn><abstract>Lactulose synthesis from fructose and lactose in continuous stirred tank (CSTR) reactor operation with glyoxyl-agarose immobilized
Aspergillus oryzae
β-galactosidase is reported for the first time. The effect of operational variables: inlet concentrations of sugar substrates, temperature, feed substrate molar ratio, enzyme loading and feed flow rate was studied on reactor performance. Even though the variation of each one affected to a certain extent lactulose yield (Y
Lactulose
), specific productivity (π
Lactulose
) and selectivity of the reaction (lactulose/transgalactosylated oligosaccharides molar ratio) (S
Lu/TOS
), the most significant effects were obtained by varying the inlet concentrations of sugar substrates and the feed substrate molar ratio. Maximum Y
Lactulose
of 0.54 g⋅g
–1
was obtained at 50°C, pH 4.5, 50% w/w inlet concentrations of sugar substrates, feed flowrate of 12 mL⋅min
–1
, fructose/lactose molar ratio of 8 and reactor enzyme load of 29.06 IU
H
⋅mL
–1
. At such conditions S
Lu/TOS
was 3.7, lactose conversion (X
Lactose
) was 0.39 and total transgalactosylation yield was 0.762 g⋅g
–1
, meaning that 76% of the reacted lactose corresponded to transgalactosylation and 24% to hydrolysis, which is a definite advantage of this mode of operation. Even though X
Lactose
in CSTR was lower than in other reported modes of operation for lactulose synthesis, transgalactosylation was more favored over hydrolysis which reduced the inhibitory effect of galactose on β-galactosidase.</abstract><pub>Frontiers Media S.A</pub><pmid>32695768</pmid><doi>10.3389/fbioe.2020.00699</doi><tpages>1</tpages><oa>free_for_read</oa></addata></record> |
fulltext | fulltext |
identifier | ISSN: 2296-4185 |
ispartof | Frontiers in bioengineering and biotechnology, 2020-06, Vol.8, p.699-699 |
issn | 2296-4185 2296-4185 |
language | eng |
recordid | cdi_doaj_primary_oai_doaj_org_article_2afbc2591252448991fd7fde7a5324f5 |
source | PubMed Central |
subjects | agarose support Bioengineering and Biotechnology galacto-oligossacharides immobilization lactulose prebiotic β-galactosidase |
title | Synthesis of Lactulose in Continuous Stirred Tank Reactor With β-Galactosidase of Apergillus oryzae Immobilized in Monofunctional Glyoxyl Agarose Support |
url | http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-11T08%3A49%3A30IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_doaj_&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Synthesis%20of%20Lactulose%20in%20Continuous%20Stirred%20Tank%20Reactor%20With%20%CE%B2-Galactosidase%20of%20Apergillus%20oryzae%20Immobilized%20in%20Monofunctional%20Glyoxyl%20Agarose%20Support&rft.jtitle=Frontiers%20in%20bioengineering%20and%20biotechnology&rft.au=Ubilla,%20Claudia&rft.date=2020-06-30&rft.volume=8&rft.spage=699&rft.epage=699&rft.pages=699-699&rft.issn=2296-4185&rft.eissn=2296-4185&rft_id=info:doi/10.3389/fbioe.2020.00699&rft_dat=%3Cproquest_doaj_%3E2426174514%3C/proquest_doaj_%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-c439t-98f6a8cdf721719595dbbd7aaefa264391afd5f971df7376f7f4dadf98afd5f13%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_pqid=2426174514&rft_id=info:pmid/32695768&rfr_iscdi=true |