Determination of Thermal Inactivation Kinetics by the Multipoint Method in a Pilot Plant Tubular Heat Exchanger
Heat resistance determinations, necessary for the design of safe thermal treatments, are usually performed in batch systems, but those on continuous systems are more realistic. In continuous systems, samples and temperatures are only taken from the inlet and outlet. Therefore, microbial inactivation...
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Veröffentlicht in: | Food and bioprocess technology 2015-07, Vol.8 (7), p.1543-1551 |
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creator | Huertas, Juan-Pablo Ros-Chumillas, María Esteban, María-Dolores Esnoz, Arturo Palop, Alfredo |
description | Heat resistance determinations, necessary for the design of safe thermal treatments, are usually performed in batch systems, but those on continuous systems are more realistic. In continuous systems, samples and temperatures are only taken from the inlet and outlet. Therefore, microbial inactivation kinetics and heat-labile compound degradation on these systems remain a black box. A pilot-scale heat exchanger, with several temperature sensors and sampling tubes along the system, was built. The aims of this research were to determine the residence time distribution, the flow type, and the inactivation kinetics of
Salmonella
Senftenberg and
Staphylococcus aureus
on the heat exchanger. Microbial inactivation data were obtained both under isothermal and non-isothermal conditions and compared to those obtained in a batch system. Flow was estimated as turbulent. Under isothermal conditions, similar inactivation levels were reached for
S. aureus
in both equipments (batch or continuous). Under non-isothermal conditions, for both microorganisms, higher inactivation of the population was observed in the last step of the treatment in the heat exchanger than in the batch system. These differences could be attributed to faster heating rates in the heat exchanger. The heat exchanger used in this investigation is a suitable tool to understand microbial inactivation kinetics in continuous systems. |
doi_str_mv | 10.1007/s11947-015-1525-9 |
format | Article |
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Salmonella
Senftenberg and
Staphylococcus aureus
on the heat exchanger. Microbial inactivation data were obtained both under isothermal and non-isothermal conditions and compared to those obtained in a batch system. Flow was estimated as turbulent. Under isothermal conditions, similar inactivation levels were reached for
S. aureus
in both equipments (batch or continuous). Under non-isothermal conditions, for both microorganisms, higher inactivation of the population was observed in the last step of the treatment in the heat exchanger than in the batch system. These differences could be attributed to faster heating rates in the heat exchanger. The heat exchanger used in this investigation is a suitable tool to understand microbial inactivation kinetics in continuous systems.</description><identifier>ISSN: 1935-5130</identifier><identifier>EISSN: 1935-5149</identifier><identifier>DOI: 10.1007/s11947-015-1525-9</identifier><language>eng</language><publisher>New York: Springer US</publisher><subject>Agriculture ; Biodegradation ; Biotechnology ; Chemistry ; Chemistry and Materials Science ; Chemistry/Food Science ; Deactivation ; Fluid dynamics ; Food Science ; Heat exchangers ; Heat resistance ; Heat treatment ; Inactivation ; Kinetics ; Microorganisms ; Original Paper ; Reaction kinetics ; Residence time distribution ; Salmonella ; Temperature sensors ; Thermal resistance ; Tubes ; Turbulent flow</subject><ispartof>Food and bioprocess technology, 2015-07, Vol.8 (7), p.1543-1551</ispartof><rights>Springer Science+Business Media New York 2015</rights><rights>Springer Science+Business Media New York 2015.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c386t-423937e5cbfd3c1cc1695c35ee5272c30a2b8c8de5d4dc00bd3925c1a98210683</citedby><cites>FETCH-LOGICAL-c386t-423937e5cbfd3c1cc1695c35ee5272c30a2b8c8de5d4dc00bd3925c1a98210683</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s11947-015-1525-9$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s11947-015-1525-9$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,776,780,27901,27902,41464,42533,51294</link.rule.ids></links><search><creatorcontrib>Huertas, Juan-Pablo</creatorcontrib><creatorcontrib>Ros-Chumillas, María</creatorcontrib><creatorcontrib>Esteban, María-Dolores</creatorcontrib><creatorcontrib>Esnoz, Arturo</creatorcontrib><creatorcontrib>Palop, Alfredo</creatorcontrib><title>Determination of Thermal Inactivation Kinetics by the Multipoint Method in a Pilot Plant Tubular Heat Exchanger</title><title>Food and bioprocess technology</title><addtitle>Food Bioprocess Technol</addtitle><description>Heat resistance determinations, necessary for the design of safe thermal treatments, are usually performed in batch systems, but those on continuous systems are more realistic. In continuous systems, samples and temperatures are only taken from the inlet and outlet. Therefore, microbial inactivation kinetics and heat-labile compound degradation on these systems remain a black box. A pilot-scale heat exchanger, with several temperature sensors and sampling tubes along the system, was built. The aims of this research were to determine the residence time distribution, the flow type, and the inactivation kinetics of
Salmonella
Senftenberg and
Staphylococcus aureus
on the heat exchanger. Microbial inactivation data were obtained both under isothermal and non-isothermal conditions and compared to those obtained in a batch system. Flow was estimated as turbulent. Under isothermal conditions, similar inactivation levels were reached for
S. aureus
in both equipments (batch or continuous). Under non-isothermal conditions, for both microorganisms, higher inactivation of the population was observed in the last step of the treatment in the heat exchanger than in the batch system. These differences could be attributed to faster heating rates in the heat exchanger. The heat exchanger used in this investigation is a suitable tool to understand microbial inactivation kinetics in continuous systems.</description><subject>Agriculture</subject><subject>Biodegradation</subject><subject>Biotechnology</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Chemistry/Food Science</subject><subject>Deactivation</subject><subject>Fluid dynamics</subject><subject>Food Science</subject><subject>Heat exchangers</subject><subject>Heat resistance</subject><subject>Heat treatment</subject><subject>Inactivation</subject><subject>Kinetics</subject><subject>Microorganisms</subject><subject>Original Paper</subject><subject>Reaction kinetics</subject><subject>Residence time distribution</subject><subject>Salmonella</subject><subject>Temperature sensors</subject><subject>Thermal resistance</subject><subject>Tubes</subject><subject>Turbulent flow</subject><issn>1935-5130</issn><issn>1935-5149</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2015</creationdate><recordtype>article</recordtype><sourceid>BENPR</sourceid><recordid>eNp1kDFPwzAQhS0EEqXwA9gsMQd8dpzEIyqFVlDRocyW4zjEVRoX20H035MqCCamu3t67073IXQN5BYIye8CgEjzhABPgFOeiBM0AcF4wiEVp789I-foIoQtIRlJgU2QezDR-J3tVLSuw67Gm2aYVYuXndLRfo76s-1MtDrg8oBjY_Cqb6PdO9tFvDKxcRW2HVZ4bVsX8bpVg77py75VHi-Minj-pRvVvRt_ic5q1QZz9VOn6O1xvpktkpfXp-Xs_iXRrMhiklImWG64LuuKadAaMsE148ZwmlPNiKJloYvK8CqtNCFlxQTlGpQoKJCsYFN0M-7de_fRmxDl1vW-G05KmgIp0lzwbHDB6NLeheBNLffe7pQ_SCDyyFWOXOXAVR65SjFk6JgJg_f40t_m_0PfXv57Xw</recordid><startdate>20150701</startdate><enddate>20150701</enddate><creator>Huertas, Juan-Pablo</creator><creator>Ros-Chumillas, María</creator><creator>Esteban, María-Dolores</creator><creator>Esnoz, Arturo</creator><creator>Palop, Alfredo</creator><general>Springer US</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope><scope>3V.</scope><scope>7X2</scope><scope>8FE</scope><scope>8FG</scope><scope>8FH</scope><scope>8FK</scope><scope>ABJCF</scope><scope>AEUYN</scope><scope>AFKRA</scope><scope>ATCPS</scope><scope>BENPR</scope><scope>BGLVJ</scope><scope>BHPHI</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>HCIFZ</scope><scope>L6V</scope><scope>M0K</scope><scope>M7S</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PTHSS</scope></search><sort><creationdate>20150701</creationdate><title>Determination of Thermal Inactivation Kinetics by the Multipoint Method in a Pilot Plant Tubular Heat Exchanger</title><author>Huertas, Juan-Pablo ; Ros-Chumillas, María ; Esteban, María-Dolores ; Esnoz, Arturo ; Palop, Alfredo</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c386t-423937e5cbfd3c1cc1695c35ee5272c30a2b8c8de5d4dc00bd3925c1a98210683</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2015</creationdate><topic>Agriculture</topic><topic>Biodegradation</topic><topic>Biotechnology</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Chemistry/Food Science</topic><topic>Deactivation</topic><topic>Fluid dynamics</topic><topic>Food Science</topic><topic>Heat exchangers</topic><topic>Heat resistance</topic><topic>Heat treatment</topic><topic>Inactivation</topic><topic>Kinetics</topic><topic>Microorganisms</topic><topic>Original Paper</topic><topic>Reaction kinetics</topic><topic>Residence time distribution</topic><topic>Salmonella</topic><topic>Temperature sensors</topic><topic>Thermal resistance</topic><topic>Tubes</topic><topic>Turbulent flow</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Huertas, Juan-Pablo</creatorcontrib><creatorcontrib>Ros-Chumillas, María</creatorcontrib><creatorcontrib>Esteban, María-Dolores</creatorcontrib><creatorcontrib>Esnoz, Arturo</creatorcontrib><creatorcontrib>Palop, Alfredo</creatorcontrib><collection>CrossRef</collection><collection>ProQuest Central (Corporate)</collection><collection>Agricultural Science Collection</collection><collection>ProQuest SciTech Collection</collection><collection>ProQuest Technology Collection</collection><collection>ProQuest Natural Science Collection</collection><collection>ProQuest Central (Alumni) (purchase pre-March 2016)</collection><collection>Materials Science & Engineering Collection</collection><collection>ProQuest One Sustainability</collection><collection>ProQuest Central UK/Ireland</collection><collection>Agricultural & Environmental Science Collection</collection><collection>ProQuest Central</collection><collection>Technology Collection</collection><collection>Natural Science Collection</collection><collection>ProQuest One Community College</collection><collection>ProQuest Central Korea</collection><collection>SciTech Premium Collection</collection><collection>ProQuest Engineering Collection</collection><collection>Agricultural Science Database</collection><collection>Engineering Database</collection><collection>ProQuest One Academic Eastern Edition (DO NOT USE)</collection><collection>ProQuest One Academic</collection><collection>ProQuest One Academic UKI Edition</collection><collection>Engineering Collection</collection><jtitle>Food and bioprocess technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Huertas, Juan-Pablo</au><au>Ros-Chumillas, María</au><au>Esteban, María-Dolores</au><au>Esnoz, Arturo</au><au>Palop, Alfredo</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Determination of Thermal Inactivation Kinetics by the Multipoint Method in a Pilot Plant Tubular Heat Exchanger</atitle><jtitle>Food and bioprocess technology</jtitle><stitle>Food Bioprocess Technol</stitle><date>2015-07-01</date><risdate>2015</risdate><volume>8</volume><issue>7</issue><spage>1543</spage><epage>1551</epage><pages>1543-1551</pages><issn>1935-5130</issn><eissn>1935-5149</eissn><abstract>Heat resistance determinations, necessary for the design of safe thermal treatments, are usually performed in batch systems, but those on continuous systems are more realistic. In continuous systems, samples and temperatures are only taken from the inlet and outlet. Therefore, microbial inactivation kinetics and heat-labile compound degradation on these systems remain a black box. A pilot-scale heat exchanger, with several temperature sensors and sampling tubes along the system, was built. The aims of this research were to determine the residence time distribution, the flow type, and the inactivation kinetics of
Salmonella
Senftenberg and
Staphylococcus aureus
on the heat exchanger. Microbial inactivation data were obtained both under isothermal and non-isothermal conditions and compared to those obtained in a batch system. Flow was estimated as turbulent. Under isothermal conditions, similar inactivation levels were reached for
S. aureus
in both equipments (batch or continuous). Under non-isothermal conditions, for both microorganisms, higher inactivation of the population was observed in the last step of the treatment in the heat exchanger than in the batch system. These differences could be attributed to faster heating rates in the heat exchanger. The heat exchanger used in this investigation is a suitable tool to understand microbial inactivation kinetics in continuous systems.</abstract><cop>New York</cop><pub>Springer US</pub><doi>10.1007/s11947-015-1525-9</doi><tpages>9</tpages></addata></record> |
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subjects | Agriculture Biodegradation Biotechnology Chemistry Chemistry and Materials Science Chemistry/Food Science Deactivation Fluid dynamics Food Science Heat exchangers Heat resistance Heat treatment Inactivation Kinetics Microorganisms Original Paper Reaction kinetics Residence time distribution Salmonella Temperature sensors Thermal resistance Tubes Turbulent flow |
title | Determination of Thermal Inactivation Kinetics by the Multipoint Method in a Pilot Plant Tubular Heat Exchanger |
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