Vapor-liquid equilibria in the system of glycidol synthesis products
Abstract Vapor-Liquid equilibrium (VLE) data have been calculated for systems made up by glycidol synthesis products and have been compared with data available from the literature. The VLE data reported for the systems have been optimized using the NRTL and UNIQUAC models, and the model parameters a...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Danov, S. M. [verfasserIn] |
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| Format: |
Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2013 |
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| Schlagwörter: |
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| Anmerkung: |
© Pleiades Publishing, Ltd. 2013 |
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| Übergeordnetes Werk: |
Enthalten in: Theoretical foundations of chemical engineering - Springer US, 1967, 47(2013), 5 vom: Sept., Seite 563-569 |
|---|---|
| Übergeordnetes Werk: |
volume:47 ; year:2013 ; number:5 ; month:09 ; pages:563-569 |
| Links: |
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| DOI / URN: |
10.1134/S0040579513040192 |
|---|
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OLC2054264563 |
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| 520 | |a Abstract Vapor-Liquid equilibrium (VLE) data have been calculated for systems made up by glycidol synthesis products and have been compared with data available from the literature. The VLE data reported for the systems have been optimized using the NRTL and UNIQUAC models, and the model parameters and their accuracy have been estimated. The VLE in binary and multicomponent systems has been simulated. | ||
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10.1134/S0040579513040192 doi (DE-627)OLC2054264563 (DE-He213)S0040579513040192-p DE-627 ger DE-627 rakwb eng 660 VZ Danov, S. M. verfasserin aut Vapor-liquid equilibria in the system of glycidol synthesis products 2013 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2013 Abstract Vapor-Liquid equilibrium (VLE) data have been calculated for systems made up by glycidol synthesis products and have been compared with data available from the literature. The VLE data reported for the systems have been optimized using the NRTL and UNIQUAC models, and the model parameters and their accuracy have been estimated. The VLE in binary and multicomponent systems has been simulated. Allyl Alcohol Glycidol Reflux Ratio Mesityl Oxide UNIQUAC Model Sulimov, A. V. aut Ovcharova, A. V. aut Enthalten in Theoretical foundations of chemical engineering Springer US, 1967 47(2013), 5 vom: Sept., Seite 563-569 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:47 year:2013 number:5 month:09 pages:563-569 https://doi.org/10.1134/S0040579513040192 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 47 2013 5 09 563-569 |
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10.1134/S0040579513040192 doi (DE-627)OLC2054264563 (DE-He213)S0040579513040192-p DE-627 ger DE-627 rakwb eng 660 VZ Danov, S. M. verfasserin aut Vapor-liquid equilibria in the system of glycidol synthesis products 2013 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2013 Abstract Vapor-Liquid equilibrium (VLE) data have been calculated for systems made up by glycidol synthesis products and have been compared with data available from the literature. The VLE data reported for the systems have been optimized using the NRTL and UNIQUAC models, and the model parameters and their accuracy have been estimated. The VLE in binary and multicomponent systems has been simulated. Allyl Alcohol Glycidol Reflux Ratio Mesityl Oxide UNIQUAC Model Sulimov, A. V. aut Ovcharova, A. V. aut Enthalten in Theoretical foundations of chemical engineering Springer US, 1967 47(2013), 5 vom: Sept., Seite 563-569 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:47 year:2013 number:5 month:09 pages:563-569 https://doi.org/10.1134/S0040579513040192 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 47 2013 5 09 563-569 |
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10.1134/S0040579513040192 doi (DE-627)OLC2054264563 (DE-He213)S0040579513040192-p DE-627 ger DE-627 rakwb eng 660 VZ Danov, S. M. verfasserin aut Vapor-liquid equilibria in the system of glycidol synthesis products 2013 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2013 Abstract Vapor-Liquid equilibrium (VLE) data have been calculated for systems made up by glycidol synthesis products and have been compared with data available from the literature. The VLE data reported for the systems have been optimized using the NRTL and UNIQUAC models, and the model parameters and their accuracy have been estimated. The VLE in binary and multicomponent systems has been simulated. Allyl Alcohol Glycidol Reflux Ratio Mesityl Oxide UNIQUAC Model Sulimov, A. V. aut Ovcharova, A. V. aut Enthalten in Theoretical foundations of chemical engineering Springer US, 1967 47(2013), 5 vom: Sept., Seite 563-569 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:47 year:2013 number:5 month:09 pages:563-569 https://doi.org/10.1134/S0040579513040192 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 47 2013 5 09 563-569 |
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10.1134/S0040579513040192 doi (DE-627)OLC2054264563 (DE-He213)S0040579513040192-p DE-627 ger DE-627 rakwb eng 660 VZ Danov, S. M. verfasserin aut Vapor-liquid equilibria in the system of glycidol synthesis products 2013 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2013 Abstract Vapor-Liquid equilibrium (VLE) data have been calculated for systems made up by glycidol synthesis products and have been compared with data available from the literature. The VLE data reported for the systems have been optimized using the NRTL and UNIQUAC models, and the model parameters and their accuracy have been estimated. The VLE in binary and multicomponent systems has been simulated. Allyl Alcohol Glycidol Reflux Ratio Mesityl Oxide UNIQUAC Model Sulimov, A. V. aut Ovcharova, A. V. aut Enthalten in Theoretical foundations of chemical engineering Springer US, 1967 47(2013), 5 vom: Sept., Seite 563-569 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:47 year:2013 number:5 month:09 pages:563-569 https://doi.org/10.1134/S0040579513040192 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 47 2013 5 09 563-569 |
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Abstract Vapor-Liquid equilibrium (VLE) data have been calculated for systems made up by glycidol synthesis products and have been compared with data available from the literature. The VLE data reported for the systems have been optimized using the NRTL and UNIQUAC models, and the model parameters and their accuracy have been estimated. The VLE in binary and multicomponent systems has been simulated. © Pleiades Publishing, Ltd. 2013 |
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Abstract Vapor-Liquid equilibrium (VLE) data have been calculated for systems made up by glycidol synthesis products and have been compared with data available from the literature. The VLE data reported for the systems have been optimized using the NRTL and UNIQUAC models, and the model parameters and their accuracy have been estimated. The VLE in binary and multicomponent systems has been simulated. © Pleiades Publishing, Ltd. 2013 |
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Abstract Vapor-Liquid equilibrium (VLE) data have been calculated for systems made up by glycidol synthesis products and have been compared with data available from the literature. The VLE data reported for the systems have been optimized using the NRTL and UNIQUAC models, and the model parameters and their accuracy have been estimated. The VLE in binary and multicomponent systems has been simulated. © Pleiades Publishing, Ltd. 2013 |
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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">OLC2054264563</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230507091014.0</controlfield><controlfield tag="007">tu</controlfield><controlfield tag="008">200819s2013 xx ||||| 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1134/S0040579513040192</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)OLC2054264563</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-He213)S0040579513040192-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">Danov, S. M.</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Vapor-liquid equilibria in the system of glycidol synthesis products</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2013</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. 2013</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract Vapor-Liquid equilibrium (VLE) data have been calculated for systems made up by glycidol synthesis products and have been compared with data available from the literature. The VLE data reported for the systems have been optimized using the NRTL and UNIQUAC models, and the model parameters and their accuracy have been estimated. The VLE in binary and multicomponent systems has been simulated.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Allyl Alcohol</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Glycidol</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Reflux Ratio</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Mesityl Oxide</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">UNIQUAC Model</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Sulimov, A. V.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Ovcharova, A. V.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Theoretical foundations of chemical engineering</subfield><subfield code="d">Springer US, 1967</subfield><subfield code="g">47(2013), 5 vom: Sept., Seite 563-569</subfield><subfield code="w">(DE-627)129601438</subfield><subfield code="w">(DE-600)241412-0</subfield><subfield code="w">(DE-576)015095061</subfield><subfield code="x">0040-5795</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:47</subfield><subfield code="g">year:2013</subfield><subfield code="g">number:5</subfield><subfield code="g">month:09</subfield><subfield code="g">pages:563-569</subfield></datafield><datafield tag="856" ind1="4" ind2="1"><subfield code="u">https://doi.org/10.1134/S0040579513040192</subfield><subfield code="z">lizenzpflichtig</subfield><subfield code="3">Volltext</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_USEFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SYSFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_OLC</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-TEC</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-CHE</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-PHA</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-DE-84</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_70</subfield></datafield><datafield tag="951" ind1=" " ind2=" "><subfield code="a">AR</subfield></datafield><datafield tag="952" ind1=" " ind2=" "><subfield code="d">47</subfield><subfield code="j">2013</subfield><subfield code="e">5</subfield><subfield code="c">09</subfield><subfield code="h">563-569</subfield></datafield></record></collection>
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