Co-production of Gluconic Acid and Fructo-oligosaccharides by Aureobasidium pullulans from Sugarcane Molasses: Effect of Oxygen Transfer Rate in Stirred Tank and Airlift Bioreactors
Aureobasidium pullulans NCYC 4012 was used to produce gluconic acid (GA) and fructo-oligosaccharides (FOS) from sugarcane molasses (ScM). For the first time, three types of bioreactors operating at different conditions of oxygenation—a stirred tank reactor (STR) operating under atmospheric pressure...
Gespeichert in:
| Veröffentlicht in: | Food and bioprocess technology 2024-05, Vol.17 (5), p.1321-1334 |
|---|---|
| Hauptverfasser: | , , , , , |
| Format: | Artikel |
| Sprache: | eng |
| Schlagworte: | |
| Online-Zugang: | Volltext |
| Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
| container_end_page | 1334 |
|---|---|
| container_issue | 5 |
| container_start_page | 1321 |
| container_title | Food and bioprocess technology |
| container_volume | 17 |
| creator | Fernandes, Sílvia Dias, Bruna Gonçalves, Daniela A. Nobre, Clarisse Belo, Isabel Lopes, Marlene |
| description | Aureobasidium pullulans
NCYC 4012 was used to produce gluconic acid (GA) and fructo-oligosaccharides (FOS) from sugarcane molasses (ScM). For the first time, three types of bioreactors operating at different conditions of oxygenation—a stirred tank reactor (STR) operating under atmospheric pressure varying stirring rate, a pressurized STR under increased air pressure up to 4 bar of air, and an airlift reactor under atmospheric pressure varying aeration rate—were employed for GA and FOS biosynthesis by
A
.
pullulans
. The highest oxygenation conditions favored GA production in the three bioreactors, whereas the synthesis of FOS was not favored by high oxygen availability. GA yields close to 1 g·g
−1
(grams of GA produced per grams of glucose consumed) were achieved in bioreactors under atmospheric pressure, and the highest titer of GA of 75 g·L
−
1
was obtained in the airlift bioreactor. In this last, the highest concentration of total FOS of 65 g·L
−1
and yield of FOS of 0.58 g·g
−1
were obtained. |
| doi_str_mv | 10.1007/s11947-023-03201-2 |
| format | Article |
| fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_3153633314</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>3153633314</sourcerecordid><originalsourceid>FETCH-LOGICAL-c347t-26e858b7245e4e116aca62b6b48181431778d63ada5c7d1e9889d51fd75567053</originalsourceid><addsrcrecordid>eNp9kc-KFDEQxhtRcB19AU8BL15a86fT6fY2DrursLLgjueQTqrHrJlkrHTAeTDfz8yOKHjwVIH6fV9V6mual4y-YZSqt5mxsVMt5aKlglPW8kfNBRuFbCXrxsd_3oI-bZ7lfE9pTzsmLpqfm9QeMLliF58iSTO5DsWm6C1ZW--IiY5cYe2mNgW_S9lY-9Wgd5DJdCTrgpAmk73zZU8OJYQSTMxkxrQnd2Vn0JoI5FMKJmfI78jlPINdTnNufxx3EMkWKz8Dks9mAeIjuVs8IjiyNfHbw_i1x-Dnhbz3CcHUTTA_b57MJmR48buumi9Xl9vNh_bm9vrjZn3TWtGppeU9DHKYFO8kdMBYb6zp-dRP3cAG1gmm1OB6YZyRVjkG4zCMTrLZKSl7RaVYNa_PvvVE3wvkRe99thDqHyGVrAWTohdCVK9V8-of9D4VjHU7LeqpFeWj4pXiZ8piyhlh1gf0e4NHzag-JanPSeqapH5IUp9E4izKFY47wL_W_1H9AntGosk</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>3041702972</pqid></control><display><type>article</type><title>Co-production of Gluconic Acid and Fructo-oligosaccharides by Aureobasidium pullulans from Sugarcane Molasses: Effect of Oxygen Transfer Rate in Stirred Tank and Airlift Bioreactors</title><source>SpringerLink Journals - AutoHoldings</source><creator>Fernandes, Sílvia ; Dias, Bruna ; Gonçalves, Daniela A. ; Nobre, Clarisse ; Belo, Isabel ; Lopes, Marlene</creator><creatorcontrib>Fernandes, Sílvia ; Dias, Bruna ; Gonçalves, Daniela A. ; Nobre, Clarisse ; Belo, Isabel ; Lopes, Marlene</creatorcontrib><description>Aureobasidium pullulans
NCYC 4012 was used to produce gluconic acid (GA) and fructo-oligosaccharides (FOS) from sugarcane molasses (ScM). For the first time, three types of bioreactors operating at different conditions of oxygenation—a stirred tank reactor (STR) operating under atmospheric pressure varying stirring rate, a pressurized STR under increased air pressure up to 4 bar of air, and an airlift reactor under atmospheric pressure varying aeration rate—were employed for GA and FOS biosynthesis by
A
.
pullulans
. The highest oxygenation conditions favored GA production in the three bioreactors, whereas the synthesis of FOS was not favored by high oxygen availability. GA yields close to 1 g·g
−1
(grams of GA produced per grams of glucose consumed) were achieved in bioreactors under atmospheric pressure, and the highest titer of GA of 75 g·L
−
1
was obtained in the airlift bioreactor. In this last, the highest concentration of total FOS of 65 g·L
−1
and yield of FOS of 0.58 g·g
−1
were obtained.</description><identifier>ISSN: 1935-5130</identifier><identifier>EISSN: 1935-5149</identifier><identifier>DOI: 10.1007/s11947-023-03201-2</identifier><language>eng</language><publisher>New York: Springer US</publisher><subject>Aeration ; Agriculture ; air ; Airlifts ; Atmospheric pressure ; Aureobasidium pullulans ; bioprocessing ; Bioreactors ; Biosynthesis ; Biotechnology ; Chemistry ; Chemistry and Materials Science ; Chemistry/Food Science ; Food Science ; Fructooligosaccharides ; Fungi ; Gluconic acid ; glucose ; Molasses ; Oligosaccharides ; oxygen ; Oxygen transfer ; Oxygenation ; Reactors ; Sugarcane ; Syrups & sweeteners</subject><ispartof>Food and bioprocess technology, 2024-05, Vol.17 (5), p.1321-1334</ispartof><rights>The Author(s) 2023</rights><rights>The Author(s) 2023. This work is published under http://creativecommons.org/licenses/by/4.0/ (the “License”). Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><cites>FETCH-LOGICAL-c347t-26e858b7245e4e116aca62b6b48181431778d63ada5c7d1e9889d51fd75567053</cites><orcidid>0000-0001-9693-2395 ; 0000-0002-5559-2600 ; 0000-0002-4799-7296 ; 0000-0002-5860-614X ; 0000-0002-6747-8389 ; 0000-0001-6830-4471</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s11947-023-03201-2$$EPDF$$P50$$Gspringer$$Hfree_for_read</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s11947-023-03201-2$$EHTML$$P50$$Gspringer$$Hfree_for_read</linktohtml><link.rule.ids>314,778,782,27911,27912,41475,42544,51306</link.rule.ids></links><search><creatorcontrib>Fernandes, Sílvia</creatorcontrib><creatorcontrib>Dias, Bruna</creatorcontrib><creatorcontrib>Gonçalves, Daniela A.</creatorcontrib><creatorcontrib>Nobre, Clarisse</creatorcontrib><creatorcontrib>Belo, Isabel</creatorcontrib><creatorcontrib>Lopes, Marlene</creatorcontrib><title>Co-production of Gluconic Acid and Fructo-oligosaccharides by Aureobasidium pullulans from Sugarcane Molasses: Effect of Oxygen Transfer Rate in Stirred Tank and Airlift Bioreactors</title><title>Food and bioprocess technology</title><addtitle>Food Bioprocess Technol</addtitle><description>Aureobasidium pullulans
NCYC 4012 was used to produce gluconic acid (GA) and fructo-oligosaccharides (FOS) from sugarcane molasses (ScM). For the first time, three types of bioreactors operating at different conditions of oxygenation—a stirred tank reactor (STR) operating under atmospheric pressure varying stirring rate, a pressurized STR under increased air pressure up to 4 bar of air, and an airlift reactor under atmospheric pressure varying aeration rate—were employed for GA and FOS biosynthesis by
A
.
pullulans
. The highest oxygenation conditions favored GA production in the three bioreactors, whereas the synthesis of FOS was not favored by high oxygen availability. GA yields close to 1 g·g
−1
(grams of GA produced per grams of glucose consumed) were achieved in bioreactors under atmospheric pressure, and the highest titer of GA of 75 g·L
−
1
was obtained in the airlift bioreactor. In this last, the highest concentration of total FOS of 65 g·L
−1
and yield of FOS of 0.58 g·g
−1
were obtained.</description><subject>Aeration</subject><subject>Agriculture</subject><subject>air</subject><subject>Airlifts</subject><subject>Atmospheric pressure</subject><subject>Aureobasidium pullulans</subject><subject>bioprocessing</subject><subject>Bioreactors</subject><subject>Biosynthesis</subject><subject>Biotechnology</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Chemistry/Food Science</subject><subject>Food Science</subject><subject>Fructooligosaccharides</subject><subject>Fungi</subject><subject>Gluconic acid</subject><subject>glucose</subject><subject>Molasses</subject><subject>Oligosaccharides</subject><subject>oxygen</subject><subject>Oxygen transfer</subject><subject>Oxygenation</subject><subject>Reactors</subject><subject>Sugarcane</subject><subject>Syrups & sweeteners</subject><issn>1935-5130</issn><issn>1935-5149</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2024</creationdate><recordtype>article</recordtype><sourceid>C6C</sourceid><recordid>eNp9kc-KFDEQxhtRcB19AU8BL15a86fT6fY2DrursLLgjueQTqrHrJlkrHTAeTDfz8yOKHjwVIH6fV9V6mual4y-YZSqt5mxsVMt5aKlglPW8kfNBRuFbCXrxsd_3oI-bZ7lfE9pTzsmLpqfm9QeMLliF58iSTO5DsWm6C1ZW--IiY5cYe2mNgW_S9lY-9Wgd5DJdCTrgpAmk73zZU8OJYQSTMxkxrQnd2Vn0JoI5FMKJmfI78jlPINdTnNufxx3EMkWKz8Dks9mAeIjuVs8IjiyNfHbw_i1x-Dnhbz3CcHUTTA_b57MJmR48buumi9Xl9vNh_bm9vrjZn3TWtGppeU9DHKYFO8kdMBYb6zp-dRP3cAG1gmm1OB6YZyRVjkG4zCMTrLZKSl7RaVYNa_PvvVE3wvkRe99thDqHyGVrAWTohdCVK9V8-of9D4VjHU7LeqpFeWj4pXiZ8piyhlh1gf0e4NHzag-JanPSeqapH5IUp9E4izKFY47wL_W_1H9AntGosk</recordid><startdate>20240501</startdate><enddate>20240501</enddate><creator>Fernandes, Sílvia</creator><creator>Dias, Bruna</creator><creator>Gonçalves, Daniela A.</creator><creator>Nobre, Clarisse</creator><creator>Belo, Isabel</creator><creator>Lopes, Marlene</creator><general>Springer US</general><general>Springer Nature B.V</general><scope>C6C</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7S9</scope><scope>L.6</scope><orcidid>https://orcid.org/0000-0001-9693-2395</orcidid><orcidid>https://orcid.org/0000-0002-5559-2600</orcidid><orcidid>https://orcid.org/0000-0002-4799-7296</orcidid><orcidid>https://orcid.org/0000-0002-5860-614X</orcidid><orcidid>https://orcid.org/0000-0002-6747-8389</orcidid><orcidid>https://orcid.org/0000-0001-6830-4471</orcidid></search><sort><creationdate>20240501</creationdate><title>Co-production of Gluconic Acid and Fructo-oligosaccharides by Aureobasidium pullulans from Sugarcane Molasses: Effect of Oxygen Transfer Rate in Stirred Tank and Airlift Bioreactors</title><author>Fernandes, Sílvia ; Dias, Bruna ; Gonçalves, Daniela A. ; Nobre, Clarisse ; Belo, Isabel ; Lopes, Marlene</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c347t-26e858b7245e4e116aca62b6b48181431778d63ada5c7d1e9889d51fd75567053</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2024</creationdate><topic>Aeration</topic><topic>Agriculture</topic><topic>air</topic><topic>Airlifts</topic><topic>Atmospheric pressure</topic><topic>Aureobasidium pullulans</topic><topic>bioprocessing</topic><topic>Bioreactors</topic><topic>Biosynthesis</topic><topic>Biotechnology</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Chemistry/Food Science</topic><topic>Food Science</topic><topic>Fructooligosaccharides</topic><topic>Fungi</topic><topic>Gluconic acid</topic><topic>glucose</topic><topic>Molasses</topic><topic>Oligosaccharides</topic><topic>oxygen</topic><topic>Oxygen transfer</topic><topic>Oxygenation</topic><topic>Reactors</topic><topic>Sugarcane</topic><topic>Syrups & sweeteners</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Fernandes, Sílvia</creatorcontrib><creatorcontrib>Dias, Bruna</creatorcontrib><creatorcontrib>Gonçalves, Daniela A.</creatorcontrib><creatorcontrib>Nobre, Clarisse</creatorcontrib><creatorcontrib>Belo, Isabel</creatorcontrib><creatorcontrib>Lopes, Marlene</creatorcontrib><collection>Springer Nature OA Free Journals</collection><collection>CrossRef</collection><collection>AGRICOLA</collection><collection>AGRICOLA - Academic</collection><jtitle>Food and bioprocess technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Fernandes, Sílvia</au><au>Dias, Bruna</au><au>Gonçalves, Daniela A.</au><au>Nobre, Clarisse</au><au>Belo, Isabel</au><au>Lopes, Marlene</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Co-production of Gluconic Acid and Fructo-oligosaccharides by Aureobasidium pullulans from Sugarcane Molasses: Effect of Oxygen Transfer Rate in Stirred Tank and Airlift Bioreactors</atitle><jtitle>Food and bioprocess technology</jtitle><stitle>Food Bioprocess Technol</stitle><date>2024-05-01</date><risdate>2024</risdate><volume>17</volume><issue>5</issue><spage>1321</spage><epage>1334</epage><pages>1321-1334</pages><issn>1935-5130</issn><eissn>1935-5149</eissn><abstract>Aureobasidium pullulans
NCYC 4012 was used to produce gluconic acid (GA) and fructo-oligosaccharides (FOS) from sugarcane molasses (ScM). For the first time, three types of bioreactors operating at different conditions of oxygenation—a stirred tank reactor (STR) operating under atmospheric pressure varying stirring rate, a pressurized STR under increased air pressure up to 4 bar of air, and an airlift reactor under atmospheric pressure varying aeration rate—were employed for GA and FOS biosynthesis by
A
.
pullulans
. The highest oxygenation conditions favored GA production in the three bioreactors, whereas the synthesis of FOS was not favored by high oxygen availability. GA yields close to 1 g·g
−1
(grams of GA produced per grams of glucose consumed) were achieved in bioreactors under atmospheric pressure, and the highest titer of GA of 75 g·L
−
1
was obtained in the airlift bioreactor. In this last, the highest concentration of total FOS of 65 g·L
−1
and yield of FOS of 0.58 g·g
−1
were obtained.</abstract><cop>New York</cop><pub>Springer US</pub><doi>10.1007/s11947-023-03201-2</doi><tpages>14</tpages><orcidid>https://orcid.org/0000-0001-9693-2395</orcidid><orcidid>https://orcid.org/0000-0002-5559-2600</orcidid><orcidid>https://orcid.org/0000-0002-4799-7296</orcidid><orcidid>https://orcid.org/0000-0002-5860-614X</orcidid><orcidid>https://orcid.org/0000-0002-6747-8389</orcidid><orcidid>https://orcid.org/0000-0001-6830-4471</orcidid><oa>free_for_read</oa></addata></record> |
| fulltext | fulltext |
| identifier | ISSN: 1935-5130 |
| ispartof | Food and bioprocess technology, 2024-05, Vol.17 (5), p.1321-1334 |
| issn | 1935-5130 1935-5149 |
| language | eng |
| recordid | cdi_proquest_miscellaneous_3153633314 |
| source | SpringerLink Journals - AutoHoldings |
| subjects | Aeration Agriculture air Airlifts Atmospheric pressure Aureobasidium pullulans bioprocessing Bioreactors Biosynthesis Biotechnology Chemistry Chemistry and Materials Science Chemistry/Food Science Food Science Fructooligosaccharides Fungi Gluconic acid glucose Molasses Oligosaccharides oxygen Oxygen transfer Oxygenation Reactors Sugarcane Syrups & sweeteners |
| title | Co-production of Gluconic Acid and Fructo-oligosaccharides by Aureobasidium pullulans from Sugarcane Molasses: Effect of Oxygen Transfer Rate in Stirred Tank and Airlift Bioreactors |
| url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-15T11%3A36%3A18IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Co-production%20of%20Gluconic%20Acid%20and%20Fructo-oligosaccharides%20by%20Aureobasidium%20pullulans%20from%20Sugarcane%20Molasses:%20Effect%20of%20Oxygen%20Transfer%20Rate%20in%20Stirred%20Tank%20and%20Airlift%20Bioreactors&rft.jtitle=Food%20and%20bioprocess%20technology&rft.au=Fernandes,%20S%C3%ADlvia&rft.date=2024-05-01&rft.volume=17&rft.issue=5&rft.spage=1321&rft.epage=1334&rft.pages=1321-1334&rft.issn=1935-5130&rft.eissn=1935-5149&rft_id=info:doi/10.1007/s11947-023-03201-2&rft_dat=%3Cproquest_cross%3E3153633314%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=3041702972&rft_id=info:pmid/&rfr_iscdi=true |