The Effects of Residual Air and Viscosity on the Rate of Heat Penetration of Retort Food Simulant in Pouch When Using Static and Oscillating Motions

The objectives of this work were to determine the effect of 3 levels of residual air and 2 different retort motions on the value of the average heating slope of the rate of heat penetration of 3 different viscosities of a food simulant in flexible retort pouches. Pouches were thermally processed in...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:Journal of food science 2018-04, Vol.83 (4), p.922-928
Hauptverfasser: MacNaughton, Mollye S., Whiteside, William S., Rieck, James R., Thomas, Ronald L.
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 928
container_issue 4
container_start_page 922
container_title Journal of food science
container_volume 83
creator MacNaughton, Mollye S.
Whiteside, William S.
Rieck, James R.
Thomas, Ronald L.
description The objectives of this work were to determine the effect of 3 levels of residual air and 2 different retort motions on the value of the average heating slope of the rate of heat penetration of 3 different viscosities of a food simulant in flexible retort pouches. Pouches were thermally processed in a water spray automated batch retort system using 2 different methods of motion: static and oscillating continuously at a speed of 10.5 rotations per min (RPM) with an angle of 15°. Nine residual air and viscosity combinations were processed during each experimental run: low viscosity with no residual air (LV‐NRA), medium viscosity with no residual air (MV‐NRA), high viscosity with no residual air (HV‐NRA), low viscosity with medium residual air (LV‐MRA), medium viscosity with medium residual air (MV‐MRA), high viscosity with medium residual air (HV‐MRA), low viscosity with high residual air (LV‐HRA), medium viscosity with high residual air (MV‐HRA), and high viscosity with high residual air (HV‐HRA). As the amount of residual air in the pouches increased, the average heating slope value decreased in both static and oscillating motions. As the viscosity of the product increased the amount of residual air affected the average heating slope less in static and oscillating motions. Overall, the oscillating motion resulted in faster rates of heat penetration in all viscosities compared to static mode. The oscillating motion reduced processing times up to 27% compared to static mode. Practical Application This research can be applied to food manufacturers that are retorting foods in pouches. Residual air in pouches has been studied previously; however, with the development of new retort motions, more research needs to be conducted about the effect of residual air in a pouch using the different motions. Food manufacturers can use this information to optimize their amount of residual air based on their product viscosity and retort motion. This could dramatically lower processing time which would save money and increase output as well as potentially increases product quality. This research is aimed at influencing food manufacturers, process authorities, and product developers.
doi_str_mv 10.1111/1750-3841.13963
format Article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_2013515139</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>2013515139</sourcerecordid><originalsourceid>FETCH-LOGICAL-c3723-ab6f1c8b33db06fdfcd4534e4ca39ecbbda06cde52e6ed739277288c4b86cab3</originalsourceid><addsrcrecordid>eNqFkUtPGzEUhS1EBSllzQ5ZYsNmwI95LhGQ0ooKRAIsLY99hxhN7GB7VOV_9AfXk1AWbOqNda-_c3ztg9ARJWc0rXNaFSTjdU7PKG9KvoMmH51dNCGEsYzSvNpHX0N4JWPNyz20z5qCs4YXE_RnvgB83XWgYsCuww8QjB5kjy-Mx9Jq_GSCcsHENXYWxwQ_yAgjeQMy4nuwEL2MJh1u1NH5iKfOaTwzy6GXNmJj8b0b1AI_L8Dix2DsC57FpFGbC-6CMn2fytT-5Uan8A196WQf4PB9P0Dz6fX88ia7vfv-4_LiNlO8YjyTbdlRVbec65aUne6UzgueQ64kb0C1rZakVBoKBiXoijesqlhdq7ytSyVbfoBOt7Yr794GCFEs02MhDWPBDUEwQnlBi_SzCT35hL66wds0XKJYkTDSkESdbynlXQgeOrHyZin9WlAixrzEmI4Y0xGbvJLi-N13aJegP_h_ASWg3AK_TQ_r__mJn9Or2db5L8JAoI0</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2025351090</pqid></control><display><type>article</type><title>The Effects of Residual Air and Viscosity on the Rate of Heat Penetration of Retort Food Simulant in Pouch When Using Static and Oscillating Motions</title><source>Wiley Online Library - AutoHoldings Journals</source><source>MEDLINE</source><creator>MacNaughton, Mollye S. ; Whiteside, William S. ; Rieck, James R. ; Thomas, Ronald L.</creator><creatorcontrib>MacNaughton, Mollye S. ; Whiteside, William S. ; Rieck, James R. ; Thomas, Ronald L.</creatorcontrib><description>The objectives of this work were to determine the effect of 3 levels of residual air and 2 different retort motions on the value of the average heating slope of the rate of heat penetration of 3 different viscosities of a food simulant in flexible retort pouches. Pouches were thermally processed in a water spray automated batch retort system using 2 different methods of motion: static and oscillating continuously at a speed of 10.5 rotations per min (RPM) with an angle of 15°. Nine residual air and viscosity combinations were processed during each experimental run: low viscosity with no residual air (LV‐NRA), medium viscosity with no residual air (MV‐NRA), high viscosity with no residual air (HV‐NRA), low viscosity with medium residual air (LV‐MRA), medium viscosity with medium residual air (MV‐MRA), high viscosity with medium residual air (HV‐MRA), low viscosity with high residual air (LV‐HRA), medium viscosity with high residual air (MV‐HRA), and high viscosity with high residual air (HV‐HRA). As the amount of residual air in the pouches increased, the average heating slope value decreased in both static and oscillating motions. As the viscosity of the product increased the amount of residual air affected the average heating slope less in static and oscillating motions. Overall, the oscillating motion resulted in faster rates of heat penetration in all viscosities compared to static mode. The oscillating motion reduced processing times up to 27% compared to static mode. Practical Application This research can be applied to food manufacturers that are retorting foods in pouches. Residual air in pouches has been studied previously; however, with the development of new retort motions, more research needs to be conducted about the effect of residual air in a pouch using the different motions. Food manufacturers can use this information to optimize their amount of residual air based on their product viscosity and retort motion. This could dramatically lower processing time which would save money and increase output as well as potentially increases product quality. This research is aimed at influencing food manufacturers, process authorities, and product developers.</description><identifier>ISSN: 0022-1147</identifier><identifier>EISSN: 1750-3841</identifier><identifier>DOI: 10.1111/1750-3841.13963</identifier><identifier>PMID: 29532935</identifier><language>eng</language><publisher>United States: Wiley Subscription Services, Inc</publisher><subject>Air ; critical factors ; Food ; Food Analysis ; Food Handling - methods ; Food Packaging - methods ; Food Preservation - methods ; Food processing ; Food production ; Food-Processing Industry - methods ; Heating ; heating penetration ; Hot Temperature ; Humans ; Penetration ; pouches ; residual air ; retort ; Viscosity ; Water</subject><ispartof>Journal of food science, 2018-04, Vol.83 (4), p.922-928</ispartof><rights>2018 Institute of Food Technologists</rights><rights>2018 Institute of Food Technologists®.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c3723-ab6f1c8b33db06fdfcd4534e4ca39ecbbda06cde52e6ed739277288c4b86cab3</citedby><cites>FETCH-LOGICAL-c3723-ab6f1c8b33db06fdfcd4534e4ca39ecbbda06cde52e6ed739277288c4b86cab3</cites><orcidid>0000-0003-2511-0401</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1111%2F1750-3841.13963$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1111%2F1750-3841.13963$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,780,784,1417,27924,27925,45574,45575</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/29532935$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>MacNaughton, Mollye S.</creatorcontrib><creatorcontrib>Whiteside, William S.</creatorcontrib><creatorcontrib>Rieck, James R.</creatorcontrib><creatorcontrib>Thomas, Ronald L.</creatorcontrib><title>The Effects of Residual Air and Viscosity on the Rate of Heat Penetration of Retort Food Simulant in Pouch When Using Static and Oscillating Motions</title><title>Journal of food science</title><addtitle>J Food Sci</addtitle><description>The objectives of this work were to determine the effect of 3 levels of residual air and 2 different retort motions on the value of the average heating slope of the rate of heat penetration of 3 different viscosities of a food simulant in flexible retort pouches. Pouches were thermally processed in a water spray automated batch retort system using 2 different methods of motion: static and oscillating continuously at a speed of 10.5 rotations per min (RPM) with an angle of 15°. Nine residual air and viscosity combinations were processed during each experimental run: low viscosity with no residual air (LV‐NRA), medium viscosity with no residual air (MV‐NRA), high viscosity with no residual air (HV‐NRA), low viscosity with medium residual air (LV‐MRA), medium viscosity with medium residual air (MV‐MRA), high viscosity with medium residual air (HV‐MRA), low viscosity with high residual air (LV‐HRA), medium viscosity with high residual air (MV‐HRA), and high viscosity with high residual air (HV‐HRA). As the amount of residual air in the pouches increased, the average heating slope value decreased in both static and oscillating motions. As the viscosity of the product increased the amount of residual air affected the average heating slope less in static and oscillating motions. Overall, the oscillating motion resulted in faster rates of heat penetration in all viscosities compared to static mode. The oscillating motion reduced processing times up to 27% compared to static mode. Practical Application This research can be applied to food manufacturers that are retorting foods in pouches. Residual air in pouches has been studied previously; however, with the development of new retort motions, more research needs to be conducted about the effect of residual air in a pouch using the different motions. Food manufacturers can use this information to optimize their amount of residual air based on their product viscosity and retort motion. This could dramatically lower processing time which would save money and increase output as well as potentially increases product quality. This research is aimed at influencing food manufacturers, process authorities, and product developers.</description><subject>Air</subject><subject>critical factors</subject><subject>Food</subject><subject>Food Analysis</subject><subject>Food Handling - methods</subject><subject>Food Packaging - methods</subject><subject>Food Preservation - methods</subject><subject>Food processing</subject><subject>Food production</subject><subject>Food-Processing Industry - methods</subject><subject>Heating</subject><subject>heating penetration</subject><subject>Hot Temperature</subject><subject>Humans</subject><subject>Penetration</subject><subject>pouches</subject><subject>residual air</subject><subject>retort</subject><subject>Viscosity</subject><subject>Water</subject><issn>0022-1147</issn><issn>1750-3841</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqFkUtPGzEUhS1EBSllzQ5ZYsNmwI95LhGQ0ooKRAIsLY99hxhN7GB7VOV_9AfXk1AWbOqNda-_c3ztg9ARJWc0rXNaFSTjdU7PKG9KvoMmH51dNCGEsYzSvNpHX0N4JWPNyz20z5qCs4YXE_RnvgB83XWgYsCuww8QjB5kjy-Mx9Jq_GSCcsHENXYWxwQ_yAgjeQMy4nuwEL2MJh1u1NH5iKfOaTwzy6GXNmJj8b0b1AI_L8Dix2DsC57FpFGbC-6CMn2fytT-5Uan8A196WQf4PB9P0Dz6fX88ia7vfv-4_LiNlO8YjyTbdlRVbec65aUne6UzgueQ64kb0C1rZakVBoKBiXoijesqlhdq7ytSyVbfoBOt7Yr794GCFEs02MhDWPBDUEwQnlBi_SzCT35hL66wds0XKJYkTDSkESdbynlXQgeOrHyZin9WlAixrzEmI4Y0xGbvJLi-N13aJegP_h_ASWg3AK_TQ_r__mJn9Or2db5L8JAoI0</recordid><startdate>201804</startdate><enddate>201804</enddate><creator>MacNaughton, Mollye S.</creator><creator>Whiteside, William S.</creator><creator>Rieck, James R.</creator><creator>Thomas, Ronald L.</creator><general>Wiley Subscription Services, Inc</general><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>7QR</scope><scope>7ST</scope><scope>7T7</scope><scope>7U7</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>P64</scope><scope>RC3</scope><scope>SOI</scope><scope>7X8</scope><orcidid>https://orcid.org/0000-0003-2511-0401</orcidid></search><sort><creationdate>201804</creationdate><title>The Effects of Residual Air and Viscosity on the Rate of Heat Penetration of Retort Food Simulant in Pouch When Using Static and Oscillating Motions</title><author>MacNaughton, Mollye S. ; Whiteside, William S. ; Rieck, James R. ; Thomas, Ronald L.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3723-ab6f1c8b33db06fdfcd4534e4ca39ecbbda06cde52e6ed739277288c4b86cab3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2018</creationdate><topic>Air</topic><topic>critical factors</topic><topic>Food</topic><topic>Food Analysis</topic><topic>Food Handling - methods</topic><topic>Food Packaging - methods</topic><topic>Food Preservation - methods</topic><topic>Food processing</topic><topic>Food production</topic><topic>Food-Processing Industry - methods</topic><topic>Heating</topic><topic>heating penetration</topic><topic>Hot Temperature</topic><topic>Humans</topic><topic>Penetration</topic><topic>pouches</topic><topic>residual air</topic><topic>retort</topic><topic>Viscosity</topic><topic>Water</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>MacNaughton, Mollye S.</creatorcontrib><creatorcontrib>Whiteside, William S.</creatorcontrib><creatorcontrib>Rieck, James R.</creatorcontrib><creatorcontrib>Thomas, Ronald L.</creatorcontrib><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>Chemoreception Abstracts</collection><collection>Environment Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Toxicology Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ANTE: Abstracts in New Technology &amp; Engineering</collection><collection>Engineering Research Database</collection><collection>Biotechnology and BioEngineering Abstracts</collection><collection>Genetics Abstracts</collection><collection>Environment Abstracts</collection><collection>MEDLINE - Academic</collection><jtitle>Journal of food science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>MacNaughton, Mollye S.</au><au>Whiteside, William S.</au><au>Rieck, James R.</au><au>Thomas, Ronald L.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>The Effects of Residual Air and Viscosity on the Rate of Heat Penetration of Retort Food Simulant in Pouch When Using Static and Oscillating Motions</atitle><jtitle>Journal of food science</jtitle><addtitle>J Food Sci</addtitle><date>2018-04</date><risdate>2018</risdate><volume>83</volume><issue>4</issue><spage>922</spage><epage>928</epage><pages>922-928</pages><issn>0022-1147</issn><eissn>1750-3841</eissn><abstract>The objectives of this work were to determine the effect of 3 levels of residual air and 2 different retort motions on the value of the average heating slope of the rate of heat penetration of 3 different viscosities of a food simulant in flexible retort pouches. Pouches were thermally processed in a water spray automated batch retort system using 2 different methods of motion: static and oscillating continuously at a speed of 10.5 rotations per min (RPM) with an angle of 15°. Nine residual air and viscosity combinations were processed during each experimental run: low viscosity with no residual air (LV‐NRA), medium viscosity with no residual air (MV‐NRA), high viscosity with no residual air (HV‐NRA), low viscosity with medium residual air (LV‐MRA), medium viscosity with medium residual air (MV‐MRA), high viscosity with medium residual air (HV‐MRA), low viscosity with high residual air (LV‐HRA), medium viscosity with high residual air (MV‐HRA), and high viscosity with high residual air (HV‐HRA). As the amount of residual air in the pouches increased, the average heating slope value decreased in both static and oscillating motions. As the viscosity of the product increased the amount of residual air affected the average heating slope less in static and oscillating motions. Overall, the oscillating motion resulted in faster rates of heat penetration in all viscosities compared to static mode. The oscillating motion reduced processing times up to 27% compared to static mode. Practical Application This research can be applied to food manufacturers that are retorting foods in pouches. Residual air in pouches has been studied previously; however, with the development of new retort motions, more research needs to be conducted about the effect of residual air in a pouch using the different motions. Food manufacturers can use this information to optimize their amount of residual air based on their product viscosity and retort motion. This could dramatically lower processing time which would save money and increase output as well as potentially increases product quality. This research is aimed at influencing food manufacturers, process authorities, and product developers.</abstract><cop>United States</cop><pub>Wiley Subscription Services, Inc</pub><pmid>29532935</pmid><doi>10.1111/1750-3841.13963</doi><tpages>7</tpages><orcidid>https://orcid.org/0000-0003-2511-0401</orcidid></addata></record>
fulltext fulltext
identifier ISSN: 0022-1147
ispartof Journal of food science, 2018-04, Vol.83 (4), p.922-928
issn 0022-1147
1750-3841
language eng
recordid cdi_proquest_miscellaneous_2013515139
source Wiley Online Library - AutoHoldings Journals; MEDLINE
subjects Air
critical factors
Food
Food Analysis
Food Handling - methods
Food Packaging - methods
Food Preservation - methods
Food processing
Food production
Food-Processing Industry - methods
Heating
heating penetration
Hot Temperature
Humans
Penetration
pouches
residual air
retort
Viscosity
Water
title The Effects of Residual Air and Viscosity on the Rate of Heat Penetration of Retort Food Simulant in Pouch When Using Static and Oscillating Motions
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-02T12%3A44%3A30IST&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=The%20Effects%20of%20Residual%20Air%20and%20Viscosity%20on%20the%20Rate%20of%20Heat%20Penetration%20of%20Retort%20Food%20Simulant%20in%20Pouch%20When%20Using%20Static%20and%20Oscillating%20Motions&rft.jtitle=Journal%20of%20food%20science&rft.au=MacNaughton,%20Mollye%20S.&rft.date=2018-04&rft.volume=83&rft.issue=4&rft.spage=922&rft.epage=928&rft.pages=922-928&rft.issn=0022-1147&rft.eissn=1750-3841&rft_id=info:doi/10.1111/1750-3841.13963&rft_dat=%3Cproquest_cross%3E2013515139%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=2025351090&rft_id=info:pmid/29532935&rfr_iscdi=true