Loading…
Influence of dilution rate on the acidogenic phase products distribution during two-phase lactose anaerobiosis
Acidogenic fermentation of lactose was carried out in a continuous stirred reactor with a mixed anaerobic culture. From the variation of the reactor products with pH and dilution rate two possible carbon flow schemes were proposed for the reaction. In both schemes the carbon flow from pyruvate to bu...
Saved in:
Published in: | Biotechnology and bioengineering 1989-12, Vol.34 (10), p.1235-1250 |
---|---|
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-c4222-bd5f5047dda18704a16308f1c382843106ec4d249dd2f93f02f626ddc073e2ac3 |
---|---|
cites | cdi_FETCH-LOGICAL-c4222-bd5f5047dda18704a16308f1c382843106ec4d249dd2f93f02f626ddc073e2ac3 |
container_end_page | 1250 |
container_issue | 10 |
container_start_page | 1235 |
container_title | Biotechnology and bioengineering |
container_volume | 34 |
creator | Kisaalita, W. S. Lo, K. V. Pinder, K. L. |
description | Acidogenic fermentation of lactose was carried out in a continuous stirred reactor with a mixed anaerobic culture. From the variation of the reactor products with pH and dilution rate two possible carbon flow schemes were proposed for the reaction. In both schemes the carbon flow from pyruvate to butyrate and lactate was assumed to occur in parallel. A change in gas composition and in product concentrations at dilution rates between 0.1 and 0.15 h−1 for pH levels between 4.5 and 6.0 was ascribed to a shift in microbial population. To clarify the mechanism radiotracer tests were made using [U–14C]‐butyrate, [2–14C]‐propionate and [U–14C]‐lactate to determine the path of carbon flow during acidogenesis of lactose using a mixed culture. At a dilution rate between 0.1 and 0.15 h−1 and pH from 4.5 to 6.0 a rise in the lactate concentration in the product was shown to be due to a microbial population shift which disabled the conversion of lactate to other intermediary metabolites. It was also found that the flow of carbon from pyruvate to butyrate and lactate occurred by parallel pathways. Also, in the presence of hydrogen reducing methanogens, lactate was almost completely converted to acetate and not propionate. Butyrate was found to be converted to acetate at a slow rate as long as hydrogen reducing methanogens were present. The role played by propionibacteria in this lactose acidogenic eocosystem was minor. From the carbon flow model it can be concluded that lactate is the most suitable marker for optimizing an acidogenic reactor in a two‐phase biomethanation process. |
doi_str_mv | 10.1002/bit.260341002 |
format | article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_734189290</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>734189290</sourcerecordid><originalsourceid>FETCH-LOGICAL-c4222-bd5f5047dda18704a16308f1c382843106ec4d249dd2f93f02f626ddc073e2ac3</originalsourceid><addsrcrecordid>eNp9kE1v1DAQhi0EokvhyBXlgMQpZWwntnOEBcqiCg4UOFqOP1pD1t7ajkr_Pa4SLZyQLI3Gembm1YPQcwxnGIC8Hn05Iwxod989QBsMA2-BDPAQbQCAtbQfyAl6kvPP2nLB2GN0gkUvBLBug8IuuGm2Qdsmusb4aS4-hiapUj9CU65to7Q38coGr5vDtcq2OaRoZl1yxXNJflxGzJx8uGrKbWwXbFK6xFpVUDbF0cfs81P0yKkp22drPUXfPry_3H5sL76c77ZvLlrdEULa0fSuh44bo7Dg0CnMKAiHNRVEdBQDs7ozpBuMIW6gDohjhBmjgVNLlKan6NWyt2a9mW0ucu-zttOkgo1zlrz6EkO1VMl2IXWKOSfr5CH5vUp3EoO8dyqrYXk0XPkX6-Z53Fvzl16VVuDlCqis1eSSCtrnI8c4qU9UjC_YrZ_s3f-Pyre7y38TrImrffv7OKnSr7qc8l7--Hwuv3_dvuOYbeUn-geA-KQe</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>734189290</pqid></control><display><type>article</type><title>Influence of dilution rate on the acidogenic phase products distribution during two-phase lactose anaerobiosis</title><source>Wiley Online (Archive)</source><creator>Kisaalita, W. S. ; Lo, K. V. ; Pinder, K. L.</creator><creatorcontrib>Kisaalita, W. S. ; Lo, K. V. ; Pinder, K. L.</creatorcontrib><description>Acidogenic fermentation of lactose was carried out in a continuous stirred reactor with a mixed anaerobic culture. From the variation of the reactor products with pH and dilution rate two possible carbon flow schemes were proposed for the reaction. In both schemes the carbon flow from pyruvate to butyrate and lactate was assumed to occur in parallel. A change in gas composition and in product concentrations at dilution rates between 0.1 and 0.15 h−1 for pH levels between 4.5 and 6.0 was ascribed to a shift in microbial population. To clarify the mechanism radiotracer tests were made using [U–14C]‐butyrate, [2–14C]‐propionate and [U–14C]‐lactate to determine the path of carbon flow during acidogenesis of lactose using a mixed culture. At a dilution rate between 0.1 and 0.15 h−1 and pH from 4.5 to 6.0 a rise in the lactate concentration in the product was shown to be due to a microbial population shift which disabled the conversion of lactate to other intermediary metabolites. It was also found that the flow of carbon from pyruvate to butyrate and lactate occurred by parallel pathways. Also, in the presence of hydrogen reducing methanogens, lactate was almost completely converted to acetate and not propionate. Butyrate was found to be converted to acetate at a slow rate as long as hydrogen reducing methanogens were present. The role played by propionibacteria in this lactose acidogenic eocosystem was minor. From the carbon flow model it can be concluded that lactate is the most suitable marker for optimizing an acidogenic reactor in a two‐phase biomethanation process.</description><identifier>ISSN: 0006-3592</identifier><identifier>EISSN: 1097-0290</identifier><identifier>DOI: 10.1002/bit.260341002</identifier><identifier>PMID: 18588064</identifier><identifier>CODEN: BIBIAU</identifier><language>eng</language><publisher>Hoboken: Wiley Subscription Services, Inc., A Wiley Company</publisher><subject>Biological and medical sciences ; Biotechnology ; Fundamental and applied biological sciences. Psychology ; Methods. Procedures. Technologies ; Microbial engineering. Fermentation and microbial culture technology</subject><ispartof>Biotechnology and bioengineering, 1989-12, Vol.34 (10), p.1235-1250</ispartof><rights>Copyright © 1989 John Wiley & Sons, Inc.</rights><rights>1990 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c4222-bd5f5047dda18704a16308f1c382843106ec4d249dd2f93f02f626ddc073e2ac3</citedby><cites>FETCH-LOGICAL-c4222-bd5f5047dda18704a16308f1c382843106ec4d249dd2f93f02f626ddc073e2ac3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Fbit.260341002$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fbit.260341002$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,780,784,1415,27923,27924,46048,46472</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=6726728$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/18588064$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Kisaalita, W. S.</creatorcontrib><creatorcontrib>Lo, K. V.</creatorcontrib><creatorcontrib>Pinder, K. L.</creatorcontrib><title>Influence of dilution rate on the acidogenic phase products distribution during two-phase lactose anaerobiosis</title><title>Biotechnology and bioengineering</title><addtitle>Biotechnol. Bioeng</addtitle><description>Acidogenic fermentation of lactose was carried out in a continuous stirred reactor with a mixed anaerobic culture. From the variation of the reactor products with pH and dilution rate two possible carbon flow schemes were proposed for the reaction. In both schemes the carbon flow from pyruvate to butyrate and lactate was assumed to occur in parallel. A change in gas composition and in product concentrations at dilution rates between 0.1 and 0.15 h−1 for pH levels between 4.5 and 6.0 was ascribed to a shift in microbial population. To clarify the mechanism radiotracer tests were made using [U–14C]‐butyrate, [2–14C]‐propionate and [U–14C]‐lactate to determine the path of carbon flow during acidogenesis of lactose using a mixed culture. At a dilution rate between 0.1 and 0.15 h−1 and pH from 4.5 to 6.0 a rise in the lactate concentration in the product was shown to be due to a microbial population shift which disabled the conversion of lactate to other intermediary metabolites. It was also found that the flow of carbon from pyruvate to butyrate and lactate occurred by parallel pathways. Also, in the presence of hydrogen reducing methanogens, lactate was almost completely converted to acetate and not propionate. Butyrate was found to be converted to acetate at a slow rate as long as hydrogen reducing methanogens were present. The role played by propionibacteria in this lactose acidogenic eocosystem was minor. From the carbon flow model it can be concluded that lactate is the most suitable marker for optimizing an acidogenic reactor in a two‐phase biomethanation process.</description><subject>Biological and medical sciences</subject><subject>Biotechnology</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>Methods. Procedures. Technologies</subject><subject>Microbial engineering. Fermentation and microbial culture technology</subject><issn>0006-3592</issn><issn>1097-0290</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1989</creationdate><recordtype>article</recordtype><recordid>eNp9kE1v1DAQhi0EokvhyBXlgMQpZWwntnOEBcqiCg4UOFqOP1pD1t7ajkr_Pa4SLZyQLI3Gembm1YPQcwxnGIC8Hn05Iwxod989QBsMA2-BDPAQbQCAtbQfyAl6kvPP2nLB2GN0gkUvBLBug8IuuGm2Qdsmusb4aS4-hiapUj9CU65to7Q38coGr5vDtcq2OaRoZl1yxXNJflxGzJx8uGrKbWwXbFK6xFpVUDbF0cfs81P0yKkp22drPUXfPry_3H5sL76c77ZvLlrdEULa0fSuh44bo7Dg0CnMKAiHNRVEdBQDs7ozpBuMIW6gDohjhBmjgVNLlKan6NWyt2a9mW0ucu-zttOkgo1zlrz6EkO1VMl2IXWKOSfr5CH5vUp3EoO8dyqrYXk0XPkX6-Z53Fvzl16VVuDlCqis1eSSCtrnI8c4qU9UjC_YrZ_s3f-Pyre7y38TrImrffv7OKnSr7qc8l7--Hwuv3_dvuOYbeUn-geA-KQe</recordid><startdate>19891205</startdate><enddate>19891205</enddate><creator>Kisaalita, W. S.</creator><creator>Lo, K. V.</creator><creator>Pinder, K. L.</creator><general>Wiley Subscription Services, Inc., A Wiley Company</general><general>Wiley</general><scope>BSCLL</scope><scope>IQODW</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7X8</scope></search><sort><creationdate>19891205</creationdate><title>Influence of dilution rate on the acidogenic phase products distribution during two-phase lactose anaerobiosis</title><author>Kisaalita, W. S. ; Lo, K. V. ; Pinder, K. L.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c4222-bd5f5047dda18704a16308f1c382843106ec4d249dd2f93f02f626ddc073e2ac3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1989</creationdate><topic>Biological and medical sciences</topic><topic>Biotechnology</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>Methods. Procedures. Technologies</topic><topic>Microbial engineering. Fermentation and microbial culture technology</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Kisaalita, W. S.</creatorcontrib><creatorcontrib>Lo, K. V.</creatorcontrib><creatorcontrib>Pinder, K. L.</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><jtitle>Biotechnology and bioengineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Kisaalita, W. S.</au><au>Lo, K. V.</au><au>Pinder, K. L.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Influence of dilution rate on the acidogenic phase products distribution during two-phase lactose anaerobiosis</atitle><jtitle>Biotechnology and bioengineering</jtitle><addtitle>Biotechnol. Bioeng</addtitle><date>1989-12-05</date><risdate>1989</risdate><volume>34</volume><issue>10</issue><spage>1235</spage><epage>1250</epage><pages>1235-1250</pages><issn>0006-3592</issn><eissn>1097-0290</eissn><coden>BIBIAU</coden><abstract>Acidogenic fermentation of lactose was carried out in a continuous stirred reactor with a mixed anaerobic culture. From the variation of the reactor products with pH and dilution rate two possible carbon flow schemes were proposed for the reaction. In both schemes the carbon flow from pyruvate to butyrate and lactate was assumed to occur in parallel. A change in gas composition and in product concentrations at dilution rates between 0.1 and 0.15 h−1 for pH levels between 4.5 and 6.0 was ascribed to a shift in microbial population. To clarify the mechanism radiotracer tests were made using [U–14C]‐butyrate, [2–14C]‐propionate and [U–14C]‐lactate to determine the path of carbon flow during acidogenesis of lactose using a mixed culture. At a dilution rate between 0.1 and 0.15 h−1 and pH from 4.5 to 6.0 a rise in the lactate concentration in the product was shown to be due to a microbial population shift which disabled the conversion of lactate to other intermediary metabolites. It was also found that the flow of carbon from pyruvate to butyrate and lactate occurred by parallel pathways. Also, in the presence of hydrogen reducing methanogens, lactate was almost completely converted to acetate and not propionate. Butyrate was found to be converted to acetate at a slow rate as long as hydrogen reducing methanogens were present. The role played by propionibacteria in this lactose acidogenic eocosystem was minor. From the carbon flow model it can be concluded that lactate is the most suitable marker for optimizing an acidogenic reactor in a two‐phase biomethanation process.</abstract><cop>Hoboken</cop><pub>Wiley Subscription Services, Inc., A Wiley Company</pub><pmid>18588064</pmid><doi>10.1002/bit.260341002</doi><tpages>16</tpages></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0006-3592 |
ispartof | Biotechnology and bioengineering, 1989-12, Vol.34 (10), p.1235-1250 |
issn | 0006-3592 1097-0290 |
language | eng |
recordid | cdi_proquest_miscellaneous_734189290 |
source | Wiley Online (Archive) |
subjects | Biological and medical sciences Biotechnology Fundamental and applied biological sciences. Psychology Methods. Procedures. Technologies Microbial engineering. Fermentation and microbial culture technology |
title | Influence of dilution rate on the acidogenic phase products distribution during two-phase lactose anaerobiosis |
url | http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-13T07%3A57%3A05IST&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=Influence%20of%20dilution%20rate%20on%20the%20acidogenic%20phase%20products%20distribution%20during%20two-phase%20lactose%20anaerobiosis&rft.jtitle=Biotechnology%20and%20bioengineering&rft.au=Kisaalita,%20W.%20S.&rft.date=1989-12-05&rft.volume=34&rft.issue=10&rft.spage=1235&rft.epage=1250&rft.pages=1235-1250&rft.issn=0006-3592&rft.eissn=1097-0290&rft.coden=BIBIAU&rft_id=info:doi/10.1002/bit.260341002&rft_dat=%3Cproquest_cross%3E734189290%3C/proquest_cross%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-c4222-bd5f5047dda18704a16308f1c382843106ec4d249dd2f93f02f626ddc073e2ac3%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_pqid=734189290&rft_id=info:pmid/18588064&rfr_iscdi=true |