Optimizing Process Parameters of Epoxidized Sucrose Soyate Synthesis for Industrial Scale Production
There is a growing need to produce epoxidized sucrose soyate (ESS) at an industrial scale for large-scale applications in coatings and material science. Industrial scale production of ESS requires optimization of the process conditions to minimize cost without compromising resin quality. Therefore,...
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Veröffentlicht in: | Organic process research & development 2015-11, Vol.19 (11), p.1683-1692 |
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description | There is a growing need to produce epoxidized sucrose soyate (ESS) at an industrial scale for large-scale applications in coatings and material science. Industrial scale production of ESS requires optimization of the process conditions to minimize cost without compromising resin quality. Therefore, a robust model was developed that predicts the conversion of double bonds to oxirane under different process scenarios. Data for the model were obtained by epoxidizing 30 g batches of sucrose soyate at three reactor temperatures (55, 60, and 65 °C), three molar ratios of acetic acid to oil unsaturation (0.25:1, 0.375:1, and 0.5:1), three molar ratios of H2O2 to oil unsaturation (1:1, 1.5:1, and 2:1), three catalyst amounts (1.5, 3.75, and 6 g), and three reaction times (3.5, 4.5, and 5.5 h). The model was highly significant with an adjusted R 2 of 97.6% and predicted R 2 of 96.8%. The root-mean-square errors (RMSE) of 0.54 showed that the model was a good fit in predicting optimal epoxidation conditions at different process levels. ESS samples epoxidized at 60–65 °C for 4.5–5 h had conversion greater than 98% even when reagent amounts were reduced by 18–20%. A similar resin quality was also attained when one of the optimal conditions was scaled-up 100 fold to a 3 kg batch. Therefore, this model can be used to determine appropriate processing conditions for epoxidizing vegetable oil-based compounds at any scale with sufficient mixing and temperature control. |
doi_str_mv | 10.1021/acs.oprd.5b00251 |
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Industrial scale production of ESS requires optimization of the process conditions to minimize cost without compromising resin quality. Therefore, a robust model was developed that predicts the conversion of double bonds to oxirane under different process scenarios. Data for the model were obtained by epoxidizing 30 g batches of sucrose soyate at three reactor temperatures (55, 60, and 65 °C), three molar ratios of acetic acid to oil unsaturation (0.25:1, 0.375:1, and 0.5:1), three molar ratios of H2O2 to oil unsaturation (1:1, 1.5:1, and 2:1), three catalyst amounts (1.5, 3.75, and 6 g), and three reaction times (3.5, 4.5, and 5.5 h). The model was highly significant with an adjusted R 2 of 97.6% and predicted R 2 of 96.8%. The root-mean-square errors (RMSE) of 0.54 showed that the model was a good fit in predicting optimal epoxidation conditions at different process levels. ESS samples epoxidized at 60–65 °C for 4.5–5 h had conversion greater than 98% even when reagent amounts were reduced by 18–20%. A similar resin quality was also attained when one of the optimal conditions was scaled-up 100 fold to a 3 kg batch. Therefore, this model can be used to determine appropriate processing conditions for epoxidizing vegetable oil-based compounds at any scale with sufficient mixing and temperature control.</description><identifier>ISSN: 1083-6160</identifier><identifier>EISSN: 1520-586X</identifier><identifier>DOI: 10.1021/acs.oprd.5b00251</identifier><language>eng</language><publisher>American Chemical Society</publisher><ispartof>Organic process research & development, 2015-11, Vol.19 (11), p.1683-1692</ispartof><rights>Copyright © 2015 American Chemical Society</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a280t-72d274c6ef15c9a4a21de38048d65825286d87cdccb02a9776d6e7ea2c03c9473</citedby><cites>FETCH-LOGICAL-a280t-72d274c6ef15c9a4a21de38048d65825286d87cdccb02a9776d6e7ea2c03c9473</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/acs.oprd.5b00251$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/acs.oprd.5b00251$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>314,780,784,2765,27076,27924,27925,56738,56788</link.rule.ids></links><search><creatorcontrib>Monono, Ewumbua M</creatorcontrib><creatorcontrib>Bahr, James A</creatorcontrib><creatorcontrib>Pryor, Scott W</creatorcontrib><creatorcontrib>Webster, Dean C</creatorcontrib><creatorcontrib>Wiesenborn, Dennis P</creatorcontrib><title>Optimizing Process Parameters of Epoxidized Sucrose Soyate Synthesis for Industrial Scale Production</title><title>Organic process research & development</title><addtitle>Org. Process Res. Dev</addtitle><description>There is a growing need to produce epoxidized sucrose soyate (ESS) at an industrial scale for large-scale applications in coatings and material science. Industrial scale production of ESS requires optimization of the process conditions to minimize cost without compromising resin quality. Therefore, a robust model was developed that predicts the conversion of double bonds to oxirane under different process scenarios. Data for the model were obtained by epoxidizing 30 g batches of sucrose soyate at three reactor temperatures (55, 60, and 65 °C), three molar ratios of acetic acid to oil unsaturation (0.25:1, 0.375:1, and 0.5:1), three molar ratios of H2O2 to oil unsaturation (1:1, 1.5:1, and 2:1), three catalyst amounts (1.5, 3.75, and 6 g), and three reaction times (3.5, 4.5, and 5.5 h). The model was highly significant with an adjusted R 2 of 97.6% and predicted R 2 of 96.8%. The root-mean-square errors (RMSE) of 0.54 showed that the model was a good fit in predicting optimal epoxidation conditions at different process levels. ESS samples epoxidized at 60–65 °C for 4.5–5 h had conversion greater than 98% even when reagent amounts were reduced by 18–20%. A similar resin quality was also attained when one of the optimal conditions was scaled-up 100 fold to a 3 kg batch. 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Process Res. Dev</addtitle><date>2015-11-20</date><risdate>2015</risdate><volume>19</volume><issue>11</issue><spage>1683</spage><epage>1692</epage><pages>1683-1692</pages><issn>1083-6160</issn><eissn>1520-586X</eissn><abstract>There is a growing need to produce epoxidized sucrose soyate (ESS) at an industrial scale for large-scale applications in coatings and material science. Industrial scale production of ESS requires optimization of the process conditions to minimize cost without compromising resin quality. Therefore, a robust model was developed that predicts the conversion of double bonds to oxirane under different process scenarios. Data for the model were obtained by epoxidizing 30 g batches of sucrose soyate at three reactor temperatures (55, 60, and 65 °C), three molar ratios of acetic acid to oil unsaturation (0.25:1, 0.375:1, and 0.5:1), three molar ratios of H2O2 to oil unsaturation (1:1, 1.5:1, and 2:1), three catalyst amounts (1.5, 3.75, and 6 g), and three reaction times (3.5, 4.5, and 5.5 h). The model was highly significant with an adjusted R 2 of 97.6% and predicted R 2 of 96.8%. The root-mean-square errors (RMSE) of 0.54 showed that the model was a good fit in predicting optimal epoxidation conditions at different process levels. ESS samples epoxidized at 60–65 °C for 4.5–5 h had conversion greater than 98% even when reagent amounts were reduced by 18–20%. A similar resin quality was also attained when one of the optimal conditions was scaled-up 100 fold to a 3 kg batch. Therefore, this model can be used to determine appropriate processing conditions for epoxidizing vegetable oil-based compounds at any scale with sufficient mixing and temperature control.</abstract><pub>American Chemical Society</pub><doi>10.1021/acs.oprd.5b00251</doi><tpages>10</tpages></addata></record> |
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title | Optimizing Process Parameters of Epoxidized Sucrose Soyate Synthesis for Industrial Scale Production |
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