pH Control of Yeast Fed-Batch Fermentation Process by Improved Input-Output Linearization Method
In general, there are many influencing factors in the cultivation of microorganisms, including yeast, among which pH control is of great importance. Since the pH characteristics of yeast fermentation processes are nonlinearity and the production of acid during yeast fermentation is typically nonline...
Gespeichert in:
Veröffentlicht in: | Theoretical foundations of chemical engineering 2023-12, Vol.57 (6), p.1403-1413 |
---|---|
Hauptverfasser: | , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 1413 |
---|---|
container_issue | 6 |
container_start_page | 1403 |
container_title | Theoretical foundations of chemical engineering |
container_volume | 57 |
creator | Ju, Hyok-Chol Ri, Kuk-Chol Jon, Ji-Song Kim, Chol-Jin |
description | In general, there are many influencing factors in the cultivation of microorganisms, including yeast, among which pH control is of great importance. Since the pH characteristics of yeast fermentation processes are nonlinearity and the production of acid during yeast fermentation is typically nonlinearity, the process pH values cannot be adjusted rapidly and accurately by conventional linear control techniques. Hence, the intrinsic nonlinear characteristics of the pH control system are approximated by several nonlinear models including Hammerstein–Wiener model, and a controller is designed based on the models. To increase the yield in yeast cultures, fed-batch fermentation method should be used more than batch cultivation method. In brief, fed-batch fermentation is a method of continuous addition of the nutrient solution(glucose fluid) following the number of yeast cells present inside the yeast fermentation tank. In this paper, a mathematical model based on chemical equilibrium is proposed to control the pH of an industrial yeast fermentation tank with only inflow, no outflow, and relatively large internal volume, and a controller is designed using the input-output linearization method. The performance of the designed controller is verified by numerical simulation and field experiments. |
doi_str_mv | 10.1134/S0040579523060088 |
format | Article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_journals_2954866865</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>2954866865</sourcerecordid><originalsourceid>FETCH-LOGICAL-c268t-4e7a7b9ad7817f28a8ff019e5774f5af99b16d78a72b278bd9cebb5c641acf163</originalsourceid><addsrcrecordid>eNp1kEtLAzEUhYMoWKs_wF3A9WgyM3kttdgHVCqoC1djkknslHYyJhmh_npTRnAhru6F851zLweAS4yuMS7KmyeESkSYIHmBKEKcH4ERpohnRVngYzA6yNlBPwVnIWwQQoJSMQJv3RxOXBu920Jn4auRIcKpqbM7GfU6bX5n2ihj41r46J02IUC1h4td592nqeGi7fqYrfqYBlw2rZG--RrwBxPXrj4HJ1Zug7n4mWPwMr1_nsyz5Wq2mNwuM51THrPSMMmUkDXjmNmcS24twsIQxkpLpBVCYZpEyXKVM65qoY1SRNMSS20xLcbgashNj330JsRq43rfppNVLkjJKeWUJAoPlPYuBG9s1flmJ_2-wqg6FFn9KTJ58sETEtu-G_-b_L_pGwshdVE</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2954866865</pqid></control><display><type>article</type><title>pH Control of Yeast Fed-Batch Fermentation Process by Improved Input-Output Linearization Method</title><source>Springer Nature - Complete Springer Journals</source><creator>Ju, Hyok-Chol ; Ri, Kuk-Chol ; Jon, Ji-Song ; Kim, Chol-Jin</creator><creatorcontrib>Ju, Hyok-Chol ; Ri, Kuk-Chol ; Jon, Ji-Song ; Kim, Chol-Jin</creatorcontrib><description>In general, there are many influencing factors in the cultivation of microorganisms, including yeast, among which pH control is of great importance. Since the pH characteristics of yeast fermentation processes are nonlinearity and the production of acid during yeast fermentation is typically nonlinearity, the process pH values cannot be adjusted rapidly and accurately by conventional linear control techniques. Hence, the intrinsic nonlinear characteristics of the pH control system are approximated by several nonlinear models including Hammerstein–Wiener model, and a controller is designed based on the models. To increase the yield in yeast cultures, fed-batch fermentation method should be used more than batch cultivation method. In brief, fed-batch fermentation is a method of continuous addition of the nutrient solution(glucose fluid) following the number of yeast cells present inside the yeast fermentation tank. In this paper, a mathematical model based on chemical equilibrium is proposed to control the pH of an industrial yeast fermentation tank with only inflow, no outflow, and relatively large internal volume, and a controller is designed using the input-output linearization method. The performance of the designed controller is verified by numerical simulation and field experiments.</description><identifier>ISSN: 0040-5795</identifier><identifier>EISSN: 1608-3431</identifier><identifier>DOI: 10.1134/S0040579523060088</identifier><language>eng</language><publisher>Moscow: Pleiades Publishing</publisher><subject>Chemistry ; Chemistry and Materials Science ; Control systems design ; Controllers ; Cultivation ; Fed batch ; Fermentation ; Industrial Chemistry/Chemical Engineering ; Linear control ; Linearization ; Mathematical models ; Nonlinearity ; pH control ; Yeast</subject><ispartof>Theoretical foundations of chemical engineering, 2023-12, Vol.57 (6), p.1403-1413</ispartof><rights>Pleiades Publishing, Ltd. 2023. ISSN 0040-5795, Theoretical Foundations of Chemical Engineering, 2023, Vol. 57, No. 6, pp. 1403–1413. © Pleiades Publishing, Ltd., 2023.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><cites>FETCH-LOGICAL-c268t-4e7a7b9ad7817f28a8ff019e5774f5af99b16d78a72b278bd9cebb5c641acf163</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1134/S0040579523060088$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1134/S0040579523060088$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,776,780,27903,27904,41467,42536,51297</link.rule.ids></links><search><creatorcontrib>Ju, Hyok-Chol</creatorcontrib><creatorcontrib>Ri, Kuk-Chol</creatorcontrib><creatorcontrib>Jon, Ji-Song</creatorcontrib><creatorcontrib>Kim, Chol-Jin</creatorcontrib><title>pH Control of Yeast Fed-Batch Fermentation Process by Improved Input-Output Linearization Method</title><title>Theoretical foundations of chemical engineering</title><addtitle>Theor Found Chem Eng</addtitle><description>In general, there are many influencing factors in the cultivation of microorganisms, including yeast, among which pH control is of great importance. Since the pH characteristics of yeast fermentation processes are nonlinearity and the production of acid during yeast fermentation is typically nonlinearity, the process pH values cannot be adjusted rapidly and accurately by conventional linear control techniques. Hence, the intrinsic nonlinear characteristics of the pH control system are approximated by several nonlinear models including Hammerstein–Wiener model, and a controller is designed based on the models. To increase the yield in yeast cultures, fed-batch fermentation method should be used more than batch cultivation method. In brief, fed-batch fermentation is a method of continuous addition of the nutrient solution(glucose fluid) following the number of yeast cells present inside the yeast fermentation tank. In this paper, a mathematical model based on chemical equilibrium is proposed to control the pH of an industrial yeast fermentation tank with only inflow, no outflow, and relatively large internal volume, and a controller is designed using the input-output linearization method. The performance of the designed controller is verified by numerical simulation and field experiments.</description><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Control systems design</subject><subject>Controllers</subject><subject>Cultivation</subject><subject>Fed batch</subject><subject>Fermentation</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Linear control</subject><subject>Linearization</subject><subject>Mathematical models</subject><subject>Nonlinearity</subject><subject>pH control</subject><subject>Yeast</subject><issn>0040-5795</issn><issn>1608-3431</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2023</creationdate><recordtype>article</recordtype><recordid>eNp1kEtLAzEUhYMoWKs_wF3A9WgyM3kttdgHVCqoC1djkknslHYyJhmh_npTRnAhru6F851zLweAS4yuMS7KmyeESkSYIHmBKEKcH4ERpohnRVngYzA6yNlBPwVnIWwQQoJSMQJv3RxOXBu920Jn4auRIcKpqbM7GfU6bX5n2ihj41r46J02IUC1h4td592nqeGi7fqYrfqYBlw2rZG--RrwBxPXrj4HJ1Zug7n4mWPwMr1_nsyz5Wq2mNwuM51THrPSMMmUkDXjmNmcS24twsIQxkpLpBVCYZpEyXKVM65qoY1SRNMSS20xLcbgashNj330JsRq43rfppNVLkjJKeWUJAoPlPYuBG9s1flmJ_2-wqg6FFn9KTJ58sETEtu-G_-b_L_pGwshdVE</recordid><startdate>20231201</startdate><enddate>20231201</enddate><creator>Ju, Hyok-Chol</creator><creator>Ri, Kuk-Chol</creator><creator>Jon, Ji-Song</creator><creator>Kim, Chol-Jin</creator><general>Pleiades Publishing</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20231201</creationdate><title>pH Control of Yeast Fed-Batch Fermentation Process by Improved Input-Output Linearization Method</title><author>Ju, Hyok-Chol ; Ri, Kuk-Chol ; Jon, Ji-Song ; Kim, Chol-Jin</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c268t-4e7a7b9ad7817f28a8ff019e5774f5af99b16d78a72b278bd9cebb5c641acf163</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2023</creationdate><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Control systems design</topic><topic>Controllers</topic><topic>Cultivation</topic><topic>Fed batch</topic><topic>Fermentation</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Linear control</topic><topic>Linearization</topic><topic>Mathematical models</topic><topic>Nonlinearity</topic><topic>pH control</topic><topic>Yeast</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ju, Hyok-Chol</creatorcontrib><creatorcontrib>Ri, Kuk-Chol</creatorcontrib><creatorcontrib>Jon, Ji-Song</creatorcontrib><creatorcontrib>Kim, Chol-Jin</creatorcontrib><collection>CrossRef</collection><jtitle>Theoretical foundations of chemical engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ju, Hyok-Chol</au><au>Ri, Kuk-Chol</au><au>Jon, Ji-Song</au><au>Kim, Chol-Jin</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>pH Control of Yeast Fed-Batch Fermentation Process by Improved Input-Output Linearization Method</atitle><jtitle>Theoretical foundations of chemical engineering</jtitle><stitle>Theor Found Chem Eng</stitle><date>2023-12-01</date><risdate>2023</risdate><volume>57</volume><issue>6</issue><spage>1403</spage><epage>1413</epage><pages>1403-1413</pages><issn>0040-5795</issn><eissn>1608-3431</eissn><abstract>In general, there are many influencing factors in the cultivation of microorganisms, including yeast, among which pH control is of great importance. Since the pH characteristics of yeast fermentation processes are nonlinearity and the production of acid during yeast fermentation is typically nonlinearity, the process pH values cannot be adjusted rapidly and accurately by conventional linear control techniques. Hence, the intrinsic nonlinear characteristics of the pH control system are approximated by several nonlinear models including Hammerstein–Wiener model, and a controller is designed based on the models. To increase the yield in yeast cultures, fed-batch fermentation method should be used more than batch cultivation method. In brief, fed-batch fermentation is a method of continuous addition of the nutrient solution(glucose fluid) following the number of yeast cells present inside the yeast fermentation tank. In this paper, a mathematical model based on chemical equilibrium is proposed to control the pH of an industrial yeast fermentation tank with only inflow, no outflow, and relatively large internal volume, and a controller is designed using the input-output linearization method. The performance of the designed controller is verified by numerical simulation and field experiments.</abstract><cop>Moscow</cop><pub>Pleiades Publishing</pub><doi>10.1134/S0040579523060088</doi><tpages>11</tpages></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0040-5795 |
ispartof | Theoretical foundations of chemical engineering, 2023-12, Vol.57 (6), p.1403-1413 |
issn | 0040-5795 1608-3431 |
language | eng |
recordid | cdi_proquest_journals_2954866865 |
source | Springer Nature - Complete Springer Journals |
subjects | Chemistry Chemistry and Materials Science Control systems design Controllers Cultivation Fed batch Fermentation Industrial Chemistry/Chemical Engineering Linear control Linearization Mathematical models Nonlinearity pH control Yeast |
title | pH Control of Yeast Fed-Batch Fermentation Process by Improved Input-Output Linearization Method |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-27T04%3A17%3A06IST&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=pH%20Control%20of%20Yeast%20Fed-Batch%20Fermentation%20Process%20by%20Improved%20Input-Output%20Linearization%20Method&rft.jtitle=Theoretical%20foundations%20of%20chemical%20engineering&rft.au=Ju,%20Hyok-Chol&rft.date=2023-12-01&rft.volume=57&rft.issue=6&rft.spage=1403&rft.epage=1413&rft.pages=1403-1413&rft.issn=0040-5795&rft.eissn=1608-3431&rft_id=info:doi/10.1134/S0040579523060088&rft_dat=%3Cproquest_cross%3E2954866865%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=2954866865&rft_id=info:pmid/&rfr_iscdi=true |