Loading…

Enzymatic synthesis of oligosaccharides: Product removal during a kinetically controlled reaction

In this article, the enzymatic production of oligosaccharides, which is an example of a kinetically controlled reaction, is studied. The aim is to show that the product yield can be enhanced by continuous removal of oligosaccharides from the reaction mixture. The oligosaccharides were removed by ads...

Full description

Saved in:
Bibliographic Details
Published in:Biotechnology and bioengineering 2000-11, Vol.70 (4), p.411-420
Main Authors: Boon, M. A., van't Riet, K., Janssen, A. E. M.
Format: Article
Language:English
Subjects:
Citations: Items that this one cites
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
cited_by
cites cdi_FETCH-LOGICAL-c4546-395475fb7cbc41238f67026350922b1b0970e422db9d1aeb822926762e2116b03
container_end_page 420
container_issue 4
container_start_page 411
container_title Biotechnology and bioengineering
container_volume 70
creator Boon, M. A.
van't Riet, K.
Janssen, A. E. M.
description In this article, the enzymatic production of oligosaccharides, which is an example of a kinetically controlled reaction, is studied. The aim is to show that the product yield can be enhanced by continuous removal of oligosaccharides from the reaction mixture. The oligosaccharides were removed by adsorption on activated carbon. The absorption could be described by the multicomponent Langmuir isotherm with different maximum saturation constants for mono‐, di‐, and trisaccharides. The affinity for trisaccharides was larger (ktri = 3.52 l/g) than for di‐ (kdi = 0.94 l/g) and monosaccharides (kmono = 0.11 l/g). A model combining kinetics, adsorption on activated carbon, and mass transfer in an adsorption column was developed. Model calculations for the batch process with removal showed a yield improvement of 23% compared to the batch process without removal. Experimentally, a yield improvement of 30% was obtained. Model calculations for the continuous process studied did not result in an increase of the yield. The advantages of removal were masked by the negative influence of recirculation and the relative large time between formation and removal. © John Wiley & Sons, Inc. Biotechnol Bioeng 70: 411–420, 2000.
doi_str_mv 10.1002/1097-0290(20001120)70:4<411::AID-BIT6>3.0.CO;2-W
format article
fullrecord <record><control><sourceid>proquest_wagen</sourceid><recordid>TN_cdi_wageningen_narcis_oai_library_wur_nl_wurpubs_64050</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>72291339</sourcerecordid><originalsourceid>FETCH-LOGICAL-c4546-395475fb7cbc41238f67026350922b1b0970e422db9d1aeb822926762e2116b03</originalsourceid><addsrcrecordid>eNqVkV-LEzEUxQdR3Fr9CjIgiD5Mvcn8yUwVYa1rLSx2hWp9u2QymW7cNKnJjGv99GZsd30RxKdwwznnnuQXRSWBCQGgLwhULAFawTMKAIRQeM5gmr3KCJlOTxdvkzeLVfE6ncBktnxJk_WdaHRruRuNgqdI0ryiJ9ED77-GkZVFcT86ISE9XKejiJ-Zn_st75SI_d50l9IrH9s2tlptrOdCXHKnGumn8YWzTS-62Mmt_c513PROmU3M4ytlZPBzrfexsKZzVmvZBB0XnbLmYXSv5drLR8dzHH16d7aavU_Ol_PF7PQ8EVmehZpVnrG8rZmoRUZoWrYFA1qkOVSU1qQOzwKZUdrUVUO4rEtKK1qwgkpKSFFDOo6qQ-4130gTqkmDhjuhPFquUKvacbfH696h0cOx62uPRQb54H168O6c_dZL3-FWeSG15kba3iMLy0iaVv8UEsagJOFnx9HFQSic9d7JFndObYcCBHBgiwMoHEDhDVtkgBkGtoiBLQ5sMUXA2RIprkPk4-Puvt7K5k_gEWYQPDkKuA84WsfN8PobXQmMQB5UH4__pLTc_1etv7T6PYfM5JCpfCd_3GZyd4UFS1mO6w9zXGXzz9n8C2Ce_gLCC9jF</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>17708192</pqid></control><display><type>article</type><title>Enzymatic synthesis of oligosaccharides: Product removal during a kinetically controlled reaction</title><source>Wiley-Blackwell Read &amp; Publish Collection</source><creator>Boon, M. A. ; van't Riet, K. ; Janssen, A. E. M.</creator><creatorcontrib>Boon, M. A. ; van't Riet, K. ; Janssen, A. E. M.</creatorcontrib><description>In this article, the enzymatic production of oligosaccharides, which is an example of a kinetically controlled reaction, is studied. The aim is to show that the product yield can be enhanced by continuous removal of oligosaccharides from the reaction mixture. The oligosaccharides were removed by adsorption on activated carbon. The absorption could be described by the multicomponent Langmuir isotherm with different maximum saturation constants for mono‐, di‐, and trisaccharides. The affinity for trisaccharides was larger (ktri = 3.52 l/g) than for di‐ (kdi = 0.94 l/g) and monosaccharides (kmono = 0.11 l/g). A model combining kinetics, adsorption on activated carbon, and mass transfer in an adsorption column was developed. Model calculations for the batch process with removal showed a yield improvement of 23% compared to the batch process without removal. Experimentally, a yield improvement of 30% was obtained. Model calculations for the continuous process studied did not result in an increase of the yield. The advantages of removal were masked by the negative influence of recirculation and the relative large time between formation and removal. © John Wiley &amp; Sons, Inc. Biotechnol Bioeng 70: 411–420, 2000.</description><identifier>ISSN: 0006-3592</identifier><identifier>EISSN: 1097-0290</identifier><identifier>DOI: 10.1002/1097-0290(20001120)70:4&lt;411::AID-BIT6&gt;3.0.CO;2-W</identifier><identifier>PMID: 11005923</identifier><identifier>CODEN: BIBIAU</identifier><language>eng</language><publisher>New York: John Wiley &amp; Sons, Inc</publisher><subject>adsorption ; beta-Galactosidase - chemistry ; beta-Galactosidase - metabolism ; Bioconversions. Hemisynthesis ; Biological and medical sciences ; Biotechnology ; Biotechnology - methods ; enzymatic synthesis ; Fundamental and applied biological sciences. Psychology ; kinetically controlled reaction ; Kinetics ; Methods. Procedures. Technologies ; modeling ; Models, Chemical ; oligosaccharides ; Oligosaccharides - chemical synthesis ; Oligosaccharides - metabolism ; product removal ; Sectie Proceskunde ; Sub-department of Food and Bioprocess Engineering ; VLAG</subject><ispartof>Biotechnology and bioengineering, 2000-11, Vol.70 (4), p.411-420</ispartof><rights>Copyright © 2000 John Wiley &amp; Sons, Inc.</rights><rights>2001 INIST-CNRS</rights><rights>Copyright John Wiley &amp; Sons, Inc.</rights><rights>Wageningen University &amp; Research</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><cites>FETCH-LOGICAL-c4546-395475fb7cbc41238f67026350922b1b0970e422db9d1aeb822926762e2116b03</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>230,314,776,780,881,27901,27902</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&amp;idt=807105$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/11005923$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Boon, M. A.</creatorcontrib><creatorcontrib>van't Riet, K.</creatorcontrib><creatorcontrib>Janssen, A. E. M.</creatorcontrib><title>Enzymatic synthesis of oligosaccharides: Product removal during a kinetically controlled reaction</title><title>Biotechnology and bioengineering</title><addtitle>Biotechnol. Bioeng</addtitle><description>In this article, the enzymatic production of oligosaccharides, which is an example of a kinetically controlled reaction, is studied. The aim is to show that the product yield can be enhanced by continuous removal of oligosaccharides from the reaction mixture. The oligosaccharides were removed by adsorption on activated carbon. The absorption could be described by the multicomponent Langmuir isotherm with different maximum saturation constants for mono‐, di‐, and trisaccharides. The affinity for trisaccharides was larger (ktri = 3.52 l/g) than for di‐ (kdi = 0.94 l/g) and monosaccharides (kmono = 0.11 l/g). A model combining kinetics, adsorption on activated carbon, and mass transfer in an adsorption column was developed. Model calculations for the batch process with removal showed a yield improvement of 23% compared to the batch process without removal. Experimentally, a yield improvement of 30% was obtained. Model calculations for the continuous process studied did not result in an increase of the yield. The advantages of removal were masked by the negative influence of recirculation and the relative large time between formation and removal. © John Wiley &amp; Sons, Inc. Biotechnol Bioeng 70: 411–420, 2000.</description><subject>adsorption</subject><subject>beta-Galactosidase - chemistry</subject><subject>beta-Galactosidase - metabolism</subject><subject>Bioconversions. Hemisynthesis</subject><subject>Biological and medical sciences</subject><subject>Biotechnology</subject><subject>Biotechnology - methods</subject><subject>enzymatic synthesis</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>kinetically controlled reaction</subject><subject>Kinetics</subject><subject>Methods. Procedures. Technologies</subject><subject>modeling</subject><subject>Models, Chemical</subject><subject>oligosaccharides</subject><subject>Oligosaccharides - chemical synthesis</subject><subject>Oligosaccharides - metabolism</subject><subject>product removal</subject><subject>Sectie Proceskunde</subject><subject>Sub-department of Food and Bioprocess Engineering</subject><subject>VLAG</subject><issn>0006-3592</issn><issn>1097-0290</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2000</creationdate><recordtype>article</recordtype><recordid>eNqVkV-LEzEUxQdR3Fr9CjIgiD5Mvcn8yUwVYa1rLSx2hWp9u2QymW7cNKnJjGv99GZsd30RxKdwwznnnuQXRSWBCQGgLwhULAFawTMKAIRQeM5gmr3KCJlOTxdvkzeLVfE6ncBktnxJk_WdaHRruRuNgqdI0ryiJ9ED77-GkZVFcT86ISE9XKejiJ-Zn_st75SI_d50l9IrH9s2tlptrOdCXHKnGumn8YWzTS-62Mmt_c513PROmU3M4ytlZPBzrfexsKZzVmvZBB0XnbLmYXSv5drLR8dzHH16d7aavU_Ol_PF7PQ8EVmehZpVnrG8rZmoRUZoWrYFA1qkOVSU1qQOzwKZUdrUVUO4rEtKK1qwgkpKSFFDOo6qQ-4130gTqkmDhjuhPFquUKvacbfH696h0cOx62uPRQb54H168O6c_dZL3-FWeSG15kba3iMLy0iaVv8UEsagJOFnx9HFQSic9d7JFndObYcCBHBgiwMoHEDhDVtkgBkGtoiBLQ5sMUXA2RIprkPk4-Puvt7K5k_gEWYQPDkKuA84WsfN8PobXQmMQB5UH4__pLTc_1etv7T6PYfM5JCpfCd_3GZyd4UFS1mO6w9zXGXzz9n8C2Ce_gLCC9jF</recordid><startdate>20001120</startdate><enddate>20001120</enddate><creator>Boon, M. A.</creator><creator>van't Riet, K.</creator><creator>Janssen, A. E. M.</creator><general>John Wiley &amp; Sons, Inc</general><general>Wiley</general><scope>BSCLL</scope><scope>IQODW</scope><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QO</scope><scope>8FD</scope><scope>FR3</scope><scope>P64</scope><scope>7X8</scope><scope>QVL</scope></search><sort><creationdate>20001120</creationdate><title>Enzymatic synthesis of oligosaccharides: Product removal during a kinetically controlled reaction</title><author>Boon, M. A. ; van't Riet, K. ; Janssen, A. E. M.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c4546-395475fb7cbc41238f67026350922b1b0970e422db9d1aeb822926762e2116b03</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2000</creationdate><topic>adsorption</topic><topic>beta-Galactosidase - chemistry</topic><topic>beta-Galactosidase - metabolism</topic><topic>Bioconversions. Hemisynthesis</topic><topic>Biological and medical sciences</topic><topic>Biotechnology</topic><topic>Biotechnology - methods</topic><topic>enzymatic synthesis</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>kinetically controlled reaction</topic><topic>Kinetics</topic><topic>Methods. Procedures. Technologies</topic><topic>modeling</topic><topic>Models, Chemical</topic><topic>oligosaccharides</topic><topic>Oligosaccharides - chemical synthesis</topic><topic>Oligosaccharides - metabolism</topic><topic>product removal</topic><topic>Sectie Proceskunde</topic><topic>Sub-department of Food and Bioprocess Engineering</topic><topic>VLAG</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Boon, M. A.</creatorcontrib><creatorcontrib>van't Riet, K.</creatorcontrib><creatorcontrib>Janssen, A. E. M.</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>Biotechnology Research Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Biotechnology and BioEngineering Abstracts</collection><collection>MEDLINE - Academic</collection><collection>NARCIS:Publications</collection><jtitle>Biotechnology and bioengineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Boon, M. A.</au><au>van't Riet, K.</au><au>Janssen, A. E. M.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Enzymatic synthesis of oligosaccharides: Product removal during a kinetically controlled reaction</atitle><jtitle>Biotechnology and bioengineering</jtitle><addtitle>Biotechnol. Bioeng</addtitle><date>2000-11-20</date><risdate>2000</risdate><volume>70</volume><issue>4</issue><spage>411</spage><epage>420</epage><pages>411-420</pages><issn>0006-3592</issn><eissn>1097-0290</eissn><coden>BIBIAU</coden><abstract>In this article, the enzymatic production of oligosaccharides, which is an example of a kinetically controlled reaction, is studied. The aim is to show that the product yield can be enhanced by continuous removal of oligosaccharides from the reaction mixture. The oligosaccharides were removed by adsorption on activated carbon. The absorption could be described by the multicomponent Langmuir isotherm with different maximum saturation constants for mono‐, di‐, and trisaccharides. The affinity for trisaccharides was larger (ktri = 3.52 l/g) than for di‐ (kdi = 0.94 l/g) and monosaccharides (kmono = 0.11 l/g). A model combining kinetics, adsorption on activated carbon, and mass transfer in an adsorption column was developed. Model calculations for the batch process with removal showed a yield improvement of 23% compared to the batch process without removal. Experimentally, a yield improvement of 30% was obtained. Model calculations for the continuous process studied did not result in an increase of the yield. The advantages of removal were masked by the negative influence of recirculation and the relative large time between formation and removal. © John Wiley &amp; Sons, Inc. Biotechnol Bioeng 70: 411–420, 2000.</abstract><cop>New York</cop><pub>John Wiley &amp; Sons, Inc</pub><pmid>11005923</pmid><doi>10.1002/1097-0290(20001120)70:4&lt;411::AID-BIT6&gt;3.0.CO;2-W</doi><tpages>10</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0006-3592
ispartof Biotechnology and bioengineering, 2000-11, Vol.70 (4), p.411-420
issn 0006-3592
1097-0290
language eng
recordid cdi_wageningen_narcis_oai_library_wur_nl_wurpubs_64050
source Wiley-Blackwell Read & Publish Collection
subjects adsorption
beta-Galactosidase - chemistry
beta-Galactosidase - metabolism
Bioconversions. Hemisynthesis
Biological and medical sciences
Biotechnology
Biotechnology - methods
enzymatic synthesis
Fundamental and applied biological sciences. Psychology
kinetically controlled reaction
Kinetics
Methods. Procedures. Technologies
modeling
Models, Chemical
oligosaccharides
Oligosaccharides - chemical synthesis
Oligosaccharides - metabolism
product removal
Sectie Proceskunde
Sub-department of Food and Bioprocess Engineering
VLAG
title Enzymatic synthesis of oligosaccharides: Product removal during a kinetically controlled reaction
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-02-02T11%3A14%3A48IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_wagen&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Enzymatic%20synthesis%20of%20oligosaccharides:%20Product%20removal%20during%20a%20kinetically%20controlled%20reaction&rft.jtitle=Biotechnology%20and%20bioengineering&rft.au=Boon,%20M.%20A.&rft.date=2000-11-20&rft.volume=70&rft.issue=4&rft.spage=411&rft.epage=420&rft.pages=411-420&rft.issn=0006-3592&rft.eissn=1097-0290&rft.coden=BIBIAU&rft_id=info:doi/10.1002/1097-0290(20001120)70:4%3C411::AID-BIT6%3E3.0.CO;2-W&rft_dat=%3Cproquest_wagen%3E72291339%3C/proquest_wagen%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-c4546-395475fb7cbc41238f67026350922b1b0970e422db9d1aeb822926762e2116b03%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_pqid=17708192&rft_id=info:pmid/11005923&rfr_iscdi=true