Model of mass transfer processes in the cascade of centrifugal extractors; IOP Conference Series: Materials Science and Engineering; Vol. 135 : Issues of Physics and Technology in Science, Industry and Medicine

Detalhes bibliográficos
Parent link:IOP Conference Series: Materials Science and Engineering
Vol. 135 : Issues of Physics and Technology in Science, Industry and Medicine.— 2016.— [012053, 6 p.]
Autor principal: Zelenetskaya E. P. Ekaterina Petrovna
Autor Corporativo: Томский политехнический университет
Outros Autores: Goryunov A. G. Aleksey Germanovich, Daneykina (Daneikina) N. V. Natalia Viktorovna
Resumo:Title screen
The paper describes a mathematical model of mass transfer processes in a cascade of reverse-flow centrifugal extractors. Model of operation of each extractor is given as tightly coupled system of mixing and separating chambers. All model units are represented by systems of differential equations. The article presents the results of testing of the developed model, which confirmed the validity of the assumptions made in the model. The authors assessed the impact of the overflow of dense phase level on the hydrostatic position of phase interface level in the extractor. The research showed that a change in the volume of dense and light phases occurs in each apparatus of a cascade even in the steady mode. Operation of the cascade consisting of 12 series-connected centrifugal extractors was simulated in order to verify the model. Computer simulation results confirm the adequacy of the developed model.
Idioma:inglês
Publicado em: 2016
Assuntos:
Acesso em linha:http://dx.doi.org/10.1088/1757-899X/135/1/012053
http://earchive.tpu.ru/handle/11683/34844
Formato: Recurso Electrónico Capítulo de Livro
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=650341

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330 |a The paper describes a mathematical model of mass transfer processes in a cascade of reverse-flow centrifugal extractors. Model of operation of each extractor is given as tightly coupled system of mixing and separating chambers. All model units are represented by systems of differential equations. The article presents the results of testing of the developed model, which confirmed the validity of the assumptions made in the model. The authors assessed the impact of the overflow of dense phase level on the hydrostatic position of phase interface level in the extractor. The research showed that a change in the volume of dense and light phases occurs in each apparatus of a cascade even in the steady mode. Operation of the cascade consisting of 12 series-connected centrifugal extractors was simulated in order to verify the model. Computer simulation results confirm the adequacy of the developed model. 
461 0 |0 (RuTPU)RU\TPU\network\2008  |t IOP Conference Series: Materials Science and Engineering 
463 0 |0 (RuTPU)RU\TPU\network\15011  |t Vol. 135 : Issues of Physics and Technology in Science, Industry and Medicine  |o VIII International Scientific Conference, 1–3 June 2016, Tomsk, Russia  |o [proceedings]  |v [012053, 6 p.]  |d 2016 
610 1 |a электронный ресурс 
610 1 |a труды учёных ТПУ 
610 1 |a массоперенос 
610 1 |a центробежные экстракторы 
610 1 |a математические модели 
610 1 |a экстракторы 
610 1 |a границы раздела 
610 1 |a компьютерное моделирование 
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701 1 |a Goryunov  |b A. G.  |c Specialist in the field of automatic control  |c head of the Department Tomsk Polytechnic University, doctor of technical Sciences  |f 1979-  |g Aleksey Germanovich  |3 (RuTPU)RU\TPU\pers\32980  |9 16825 
701 1 |a Daneykina (Daneikina)  |b N. V.  |c linguist  |c Senior Lecturer of Tomsk Polytechnic University  |f 1977-  |g Natalia Viktorovna  |3 (RuTPU)RU\TPU\pers\32624 
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