Mathematical modeling of the continuous process of butadiene polymerization over a neodymium-based catalyst with allowance for its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors
Abstract A mathematical model for continuous butadiene polymerization under the effect of a neodymium versatate-diisobutylaluminum hydride-hexachloro-p-xylene catalytic system is developed that takes into account its polycentric nature and chain transfer to the polymer in a cascade of stirred reacto...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Manuiko, G. V. [verfasserIn] |
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| Format: |
Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2010 |
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| Schlagwörter: |
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| Anmerkung: |
© Pleiades Publishing, Ltd. 2010 |
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| Übergeordnetes Werk: |
Enthalten in: Theoretical foundations of chemical engineering - SP MAIK Nauka/Interperiodica, 1967, 44(2010), 6 vom: Dez., Seite 920-926 |
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| Übergeordnetes Werk: |
volume:44 ; year:2010 ; number:6 ; month:12 ; pages:920-926 |
| Links: |
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| DOI / URN: |
10.1134/S0040579510060126 |
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OLC2054262048 |
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| 245 | 1 | 0 | |a Mathematical modeling of the continuous process of butadiene polymerization over a neodymium-based catalyst with allowance for its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors |
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| 520 | |a Abstract A mathematical model for continuous butadiene polymerization under the effect of a neodymium versatate-diisobutylaluminum hydride-hexachloro-p-xylene catalytic system is developed that takes into account its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors. The constructed mathematical model adequately describes industrial data and makes it possible to calculate not only the average molecular weights, but also the characteristics of polymer branching at the outlet of the kth reactor of the cascade. | ||
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| 700 | 1 | |a Dyakonov, G. S. |4 aut | |
| 700 | 1 | |a Farakshina, E. I. |4 aut | |
| 700 | 1 | |a Salakhov, I. I. |4 aut | |
| 700 | 1 | |a Bronskaya, V. V. |4 aut | |
| 700 | 1 | |a Bashkirov, D. V. |4 aut | |
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10.1134/S0040579510060126 doi (DE-627)OLC2054262048 (DE-He213)S0040579510060126-p DE-627 ger DE-627 rakwb eng 660 VZ Manuiko, G. V. verfasserin aut Mathematical modeling of the continuous process of butadiene polymerization over a neodymium-based catalyst with allowance for its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors 2010 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2010 Abstract A mathematical model for continuous butadiene polymerization under the effect of a neodymium versatate-diisobutylaluminum hydride-hexachloro-p-xylene catalytic system is developed that takes into account its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors. The constructed mathematical model adequately describes industrial data and makes it possible to calculate not only the average molecular weights, but also the characteristics of polymer branching at the outlet of the kth reactor of the cascade. Electron Spin Resonance Chain Transfer Polydispersity Index Lateral Branch Backbone Chain Aminova, G. A. aut Dyakonov, G. S. aut Farakshina, E. I. aut Salakhov, I. I. aut Bronskaya, V. V. aut Bashkirov, D. V. aut Enthalten in Theoretical foundations of chemical engineering SP MAIK Nauka/Interperiodica, 1967 44(2010), 6 vom: Dez., Seite 920-926 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:44 year:2010 number:6 month:12 pages:920-926 https://doi.org/10.1134/S0040579510060126 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 44 2010 6 12 920-926 |
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10.1134/S0040579510060126 doi (DE-627)OLC2054262048 (DE-He213)S0040579510060126-p DE-627 ger DE-627 rakwb eng 660 VZ Manuiko, G. V. verfasserin aut Mathematical modeling of the continuous process of butadiene polymerization over a neodymium-based catalyst with allowance for its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors 2010 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2010 Abstract A mathematical model for continuous butadiene polymerization under the effect of a neodymium versatate-diisobutylaluminum hydride-hexachloro-p-xylene catalytic system is developed that takes into account its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors. The constructed mathematical model adequately describes industrial data and makes it possible to calculate not only the average molecular weights, but also the characteristics of polymer branching at the outlet of the kth reactor of the cascade. Electron Spin Resonance Chain Transfer Polydispersity Index Lateral Branch Backbone Chain Aminova, G. A. aut Dyakonov, G. S. aut Farakshina, E. I. aut Salakhov, I. I. aut Bronskaya, V. V. aut Bashkirov, D. V. aut Enthalten in Theoretical foundations of chemical engineering SP MAIK Nauka/Interperiodica, 1967 44(2010), 6 vom: Dez., Seite 920-926 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:44 year:2010 number:6 month:12 pages:920-926 https://doi.org/10.1134/S0040579510060126 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 44 2010 6 12 920-926 |
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10.1134/S0040579510060126 doi (DE-627)OLC2054262048 (DE-He213)S0040579510060126-p DE-627 ger DE-627 rakwb eng 660 VZ Manuiko, G. V. verfasserin aut Mathematical modeling of the continuous process of butadiene polymerization over a neodymium-based catalyst with allowance for its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors 2010 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2010 Abstract A mathematical model for continuous butadiene polymerization under the effect of a neodymium versatate-diisobutylaluminum hydride-hexachloro-p-xylene catalytic system is developed that takes into account its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors. The constructed mathematical model adequately describes industrial data and makes it possible to calculate not only the average molecular weights, but also the characteristics of polymer branching at the outlet of the kth reactor of the cascade. Electron Spin Resonance Chain Transfer Polydispersity Index Lateral Branch Backbone Chain Aminova, G. A. aut Dyakonov, G. S. aut Farakshina, E. I. aut Salakhov, I. I. aut Bronskaya, V. V. aut Bashkirov, D. V. aut Enthalten in Theoretical foundations of chemical engineering SP MAIK Nauka/Interperiodica, 1967 44(2010), 6 vom: Dez., Seite 920-926 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:44 year:2010 number:6 month:12 pages:920-926 https://doi.org/10.1134/S0040579510060126 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 44 2010 6 12 920-926 |
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10.1134/S0040579510060126 doi (DE-627)OLC2054262048 (DE-He213)S0040579510060126-p DE-627 ger DE-627 rakwb eng 660 VZ Manuiko, G. V. verfasserin aut Mathematical modeling of the continuous process of butadiene polymerization over a neodymium-based catalyst with allowance for its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors 2010 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2010 Abstract A mathematical model for continuous butadiene polymerization under the effect of a neodymium versatate-diisobutylaluminum hydride-hexachloro-p-xylene catalytic system is developed that takes into account its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors. The constructed mathematical model adequately describes industrial data and makes it possible to calculate not only the average molecular weights, but also the characteristics of polymer branching at the outlet of the kth reactor of the cascade. Electron Spin Resonance Chain Transfer Polydispersity Index Lateral Branch Backbone Chain Aminova, G. A. aut Dyakonov, G. S. aut Farakshina, E. I. aut Salakhov, I. I. aut Bronskaya, V. V. aut Bashkirov, D. V. aut Enthalten in Theoretical foundations of chemical engineering SP MAIK Nauka/Interperiodica, 1967 44(2010), 6 vom: Dez., Seite 920-926 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:44 year:2010 number:6 month:12 pages:920-926 https://doi.org/10.1134/S0040579510060126 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 44 2010 6 12 920-926 |
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10.1134/S0040579510060126 doi (DE-627)OLC2054262048 (DE-He213)S0040579510060126-p DE-627 ger DE-627 rakwb eng 660 VZ Manuiko, G. V. verfasserin aut Mathematical modeling of the continuous process of butadiene polymerization over a neodymium-based catalyst with allowance for its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors 2010 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2010 Abstract A mathematical model for continuous butadiene polymerization under the effect of a neodymium versatate-diisobutylaluminum hydride-hexachloro-p-xylene catalytic system is developed that takes into account its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors. The constructed mathematical model adequately describes industrial data and makes it possible to calculate not only the average molecular weights, but also the characteristics of polymer branching at the outlet of the kth reactor of the cascade. Electron Spin Resonance Chain Transfer Polydispersity Index Lateral Branch Backbone Chain Aminova, G. A. aut Dyakonov, G. S. aut Farakshina, E. I. aut Salakhov, I. I. aut Bronskaya, V. V. aut Bashkirov, D. V. aut Enthalten in Theoretical foundations of chemical engineering SP MAIK Nauka/Interperiodica, 1967 44(2010), 6 vom: Dez., Seite 920-926 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:44 year:2010 number:6 month:12 pages:920-926 https://doi.org/10.1134/S0040579510060126 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 44 2010 6 12 920-926 |
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mathematical modeling of the continuous process of butadiene polymerization over a neodymium-based catalyst with allowance for its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors |
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Mathematical modeling of the continuous process of butadiene polymerization over a neodymium-based catalyst with allowance for its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors |
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Abstract A mathematical model for continuous butadiene polymerization under the effect of a neodymium versatate-diisobutylaluminum hydride-hexachloro-p-xylene catalytic system is developed that takes into account its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors. The constructed mathematical model adequately describes industrial data and makes it possible to calculate not only the average molecular weights, but also the characteristics of polymer branching at the outlet of the kth reactor of the cascade. © Pleiades Publishing, Ltd. 2010 |
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Abstract A mathematical model for continuous butadiene polymerization under the effect of a neodymium versatate-diisobutylaluminum hydride-hexachloro-p-xylene catalytic system is developed that takes into account its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors. The constructed mathematical model adequately describes industrial data and makes it possible to calculate not only the average molecular weights, but also the characteristics of polymer branching at the outlet of the kth reactor of the cascade. © Pleiades Publishing, Ltd. 2010 |
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Abstract A mathematical model for continuous butadiene polymerization under the effect of a neodymium versatate-diisobutylaluminum hydride-hexachloro-p-xylene catalytic system is developed that takes into account its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors. The constructed mathematical model adequately describes industrial data and makes it possible to calculate not only the average molecular weights, but also the characteristics of polymer branching at the outlet of the kth reactor of the cascade. © Pleiades Publishing, Ltd. 2010 |
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Mathematical modeling of the continuous process of butadiene polymerization over a neodymium-based catalyst with allowance for its polycentric nature and chain transfer to the polymer in a cascade of stirred reactors |
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https://doi.org/10.1134/S0040579510060126 |
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Aminova, G. A. Dyakonov, G. S. Farakshina, E. I. Salakhov, I. I. Bronskaya, V. V. Bashkirov, D. V. |
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Aminova, G. A. Dyakonov, G. S. Farakshina, E. I. Salakhov, I. I. Bronskaya, V. V. Bashkirov, D. V. |
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10.1134/S0040579510060126 |
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