Vapor–liquid equilibrium in the system of propylene oxide synthesis products
Abstract Vapor–liquid equilibrium data calculated for the systems formed by propylene oxide synthesis products have been compared to the same data available from the literature. Using the NRTL and UNIQUAC models, the vapor–liquid equilibrium data available from the literature for the systems have be...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Sulimov, A. V. [verfasserIn] |
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| Format: |
Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2015 |
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| Schlagwörter: |
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| Anmerkung: |
© Pleiades Publishing, Ltd. 2015 |
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| Übergeordnetes Werk: |
Enthalten in: Theoretical foundations of chemical engineering - Pleiades Publishing, 1967, 49(2015), 6 vom: Nov., Seite 854-863 |
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| Übergeordnetes Werk: |
volume:49 ; year:2015 ; number:6 ; month:11 ; pages:854-863 |
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| DOI / URN: |
10.1134/S0040579515060093 |
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OLC2054267058 |
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| 520 | |a Abstract Vapor–liquid equilibrium data calculated for the systems formed by propylene oxide synthesis products have been compared to the same data available from the literature. Using the NRTL and UNIQUAC models, the vapor–liquid equilibrium data available from the literature for the systems have been optimized, the model parameters and their errors have been estimated, and the corresponding diagrams have been calculated and mapped. A process flowsheet for propylene oxide isolation from the reaction mixture is suggested. | ||
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10.1134/S0040579515060093 doi (DE-627)OLC2054267058 (DE-He213)S0040579515060093-p DE-627 ger DE-627 rakwb eng 660 VZ Sulimov, A. V. verfasserin aut Vapor–liquid equilibrium in the system of propylene oxide synthesis products 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2015 Abstract Vapor–liquid equilibrium data calculated for the systems formed by propylene oxide synthesis products have been compared to the same data available from the literature. Using the NRTL and UNIQUAC models, the vapor–liquid equilibrium data available from the literature for the systems have been optimized, the model parameters and their errors have been estimated, and the corresponding diagrams have been calculated and mapped. A process flowsheet for propylene oxide isolation from the reaction mixture is suggested. mathematical modeling vapor–liquid equilibrium binary systems propylene oxide methanol Danov, S. M. aut Ovcharova, A. V. aut Ovcharov, A. A. aut Flid, V. R. aut Ugryumov, O. V. aut Enthalten in Theoretical foundations of chemical engineering Pleiades Publishing, 1967 49(2015), 6 vom: Nov., Seite 854-863 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:49 year:2015 number:6 month:11 pages:854-863 https://doi.org/10.1134/S0040579515060093 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 49 2015 6 11 854-863 |
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10.1134/S0040579515060093 doi (DE-627)OLC2054267058 (DE-He213)S0040579515060093-p DE-627 ger DE-627 rakwb eng 660 VZ Sulimov, A. V. verfasserin aut Vapor–liquid equilibrium in the system of propylene oxide synthesis products 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2015 Abstract Vapor–liquid equilibrium data calculated for the systems formed by propylene oxide synthesis products have been compared to the same data available from the literature. Using the NRTL and UNIQUAC models, the vapor–liquid equilibrium data available from the literature for the systems have been optimized, the model parameters and their errors have been estimated, and the corresponding diagrams have been calculated and mapped. A process flowsheet for propylene oxide isolation from the reaction mixture is suggested. mathematical modeling vapor–liquid equilibrium binary systems propylene oxide methanol Danov, S. M. aut Ovcharova, A. V. aut Ovcharov, A. A. aut Flid, V. R. aut Ugryumov, O. V. aut Enthalten in Theoretical foundations of chemical engineering Pleiades Publishing, 1967 49(2015), 6 vom: Nov., Seite 854-863 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:49 year:2015 number:6 month:11 pages:854-863 https://doi.org/10.1134/S0040579515060093 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 49 2015 6 11 854-863 |
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10.1134/S0040579515060093 doi (DE-627)OLC2054267058 (DE-He213)S0040579515060093-p DE-627 ger DE-627 rakwb eng 660 VZ Sulimov, A. V. verfasserin aut Vapor–liquid equilibrium in the system of propylene oxide synthesis products 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2015 Abstract Vapor–liquid equilibrium data calculated for the systems formed by propylene oxide synthesis products have been compared to the same data available from the literature. Using the NRTL and UNIQUAC models, the vapor–liquid equilibrium data available from the literature for the systems have been optimized, the model parameters and their errors have been estimated, and the corresponding diagrams have been calculated and mapped. A process flowsheet for propylene oxide isolation from the reaction mixture is suggested. mathematical modeling vapor–liquid equilibrium binary systems propylene oxide methanol Danov, S. M. aut Ovcharova, A. V. aut Ovcharov, A. A. aut Flid, V. R. aut Ugryumov, O. V. aut Enthalten in Theoretical foundations of chemical engineering Pleiades Publishing, 1967 49(2015), 6 vom: Nov., Seite 854-863 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:49 year:2015 number:6 month:11 pages:854-863 https://doi.org/10.1134/S0040579515060093 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 49 2015 6 11 854-863 |
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10.1134/S0040579515060093 doi (DE-627)OLC2054267058 (DE-He213)S0040579515060093-p DE-627 ger DE-627 rakwb eng 660 VZ Sulimov, A. V. verfasserin aut Vapor–liquid equilibrium in the system of propylene oxide synthesis products 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2015 Abstract Vapor–liquid equilibrium data calculated for the systems formed by propylene oxide synthesis products have been compared to the same data available from the literature. Using the NRTL and UNIQUAC models, the vapor–liquid equilibrium data available from the literature for the systems have been optimized, the model parameters and their errors have been estimated, and the corresponding diagrams have been calculated and mapped. A process flowsheet for propylene oxide isolation from the reaction mixture is suggested. mathematical modeling vapor–liquid equilibrium binary systems propylene oxide methanol Danov, S. M. aut Ovcharova, A. V. aut Ovcharov, A. A. aut Flid, V. R. aut Ugryumov, O. V. aut Enthalten in Theoretical foundations of chemical engineering Pleiades Publishing, 1967 49(2015), 6 vom: Nov., Seite 854-863 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:49 year:2015 number:6 month:11 pages:854-863 https://doi.org/10.1134/S0040579515060093 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 49 2015 6 11 854-863 |
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10.1134/S0040579515060093 doi (DE-627)OLC2054267058 (DE-He213)S0040579515060093-p DE-627 ger DE-627 rakwb eng 660 VZ Sulimov, A. V. verfasserin aut Vapor–liquid equilibrium in the system of propylene oxide synthesis products 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2015 Abstract Vapor–liquid equilibrium data calculated for the systems formed by propylene oxide synthesis products have been compared to the same data available from the literature. Using the NRTL and UNIQUAC models, the vapor–liquid equilibrium data available from the literature for the systems have been optimized, the model parameters and their errors have been estimated, and the corresponding diagrams have been calculated and mapped. A process flowsheet for propylene oxide isolation from the reaction mixture is suggested. mathematical modeling vapor–liquid equilibrium binary systems propylene oxide methanol Danov, S. M. aut Ovcharova, A. V. aut Ovcharov, A. A. aut Flid, V. R. aut Ugryumov, O. V. aut Enthalten in Theoretical foundations of chemical engineering Pleiades Publishing, 1967 49(2015), 6 vom: Nov., Seite 854-863 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:49 year:2015 number:6 month:11 pages:854-863 https://doi.org/10.1134/S0040579515060093 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 49 2015 6 11 854-863 |
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Abstract Vapor–liquid equilibrium data calculated for the systems formed by propylene oxide synthesis products have been compared to the same data available from the literature. Using the NRTL and UNIQUAC models, the vapor–liquid equilibrium data available from the literature for the systems have been optimized, the model parameters and their errors have been estimated, and the corresponding diagrams have been calculated and mapped. A process flowsheet for propylene oxide isolation from the reaction mixture is suggested. © Pleiades Publishing, Ltd. 2015 |
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Abstract Vapor–liquid equilibrium data calculated for the systems formed by propylene oxide synthesis products have been compared to the same data available from the literature. Using the NRTL and UNIQUAC models, the vapor–liquid equilibrium data available from the literature for the systems have been optimized, the model parameters and their errors have been estimated, and the corresponding diagrams have been calculated and mapped. A process flowsheet for propylene oxide isolation from the reaction mixture is suggested. © Pleiades Publishing, Ltd. 2015 |
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Abstract Vapor–liquid equilibrium data calculated for the systems formed by propylene oxide synthesis products have been compared to the same data available from the literature. Using the NRTL and UNIQUAC models, the vapor–liquid equilibrium data available from the literature for the systems have been optimized, the model parameters and their errors have been estimated, and the corresponding diagrams have been calculated and mapped. A process flowsheet for propylene oxide isolation from the reaction mixture is suggested. © Pleiades Publishing, Ltd. 2015 |
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<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a22002652 4500</leader><controlfield tag="001">OLC2054267058</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230507091020.0</controlfield><controlfield tag="007">tu</controlfield><controlfield tag="008">200819s2015 xx ||||| 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1134/S0040579515060093</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)OLC2054267058</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-He213)S0040579515060093-p</subfield></datafield><datafield tag="040" ind1=" " ind2=" "><subfield code="a">DE-627</subfield><subfield code="b">ger</subfield><subfield code="c">DE-627</subfield><subfield code="e">rakwb</subfield></datafield><datafield tag="041" ind1=" " ind2=" "><subfield code="a">eng</subfield></datafield><datafield tag="082" ind1="0" ind2="4"><subfield code="a">660</subfield><subfield code="q">VZ</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Sulimov, A. V.</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Vapor–liquid equilibrium in the system of propylene oxide synthesis products</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2015</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">ohne Hilfsmittel zu benutzen</subfield><subfield code="b">n</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Band</subfield><subfield code="b">nc</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="500" ind1=" " ind2=" "><subfield code="a">© Pleiades Publishing, Ltd. 2015</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract Vapor–liquid equilibrium data calculated for the systems formed by propylene oxide synthesis products have been compared to the same data available from the literature. Using the NRTL and UNIQUAC models, the vapor–liquid equilibrium data available from the literature for the systems have been optimized, the model parameters and their errors have been estimated, and the corresponding diagrams have been calculated and mapped. A process flowsheet for propylene oxide isolation from the reaction mixture is suggested.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">mathematical modeling</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">vapor–liquid equilibrium</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">binary systems</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">propylene oxide</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">methanol</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Danov, S. 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