Low-temperature separation of gas: Simulation of dynamic conditions; Petroleum Science and Technology; Vol. 35, № 12

Dades bibliogràfiques
Parent link:Petroleum Science and Technology
Vol. 35, № 12.— 2017.— [P. 1263-1269]
Autor corporatiu: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Altres autors: Dolganova I. O. Irena Olegovna, Dolganov I. M. Igor Mikhailovich, Ivashkina E. N. Elena Nikolaevna, Vladesku A. Alina
Sumari:Title screen
The aim of the present paper is to increase the efficiency of low-temperature gas separation plant with use of simulation dynamic model. The paper analyzes the main processes occurring at the installation and performs the results of model verification. In addition, the technological scheme of natural low-temperature gas separation and operating parameters of one of the existing installations were considered. A non-stationary mathematical model of the chemical-technological system of low-temperature gas separation was developed. Due to the unsteady mathematical model, it became possible to estimate the time spent on the transient phenomena, as well as to choose the rate of low-temperature separation control parameters change, depending on the technological mode. Eventually, the calculations show how it is possible to avoid the instability of plant operation upset conditions at the workplace. The field of the developed model application is oil and gas industry and also higher education institutions. This software can be used to test the stability of both existing and projected low-temperature gas separation plants.
Idioma:anglès
Publicat: 2017
Matèries:
Accés en línia:http://dx.doi.org/10.1080/10916466.2017.1322979
Format: MixedMaterials Electrònic Capítol de llibre
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=656487

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200 1 |a Low-temperature separation of gas: Simulation of dynamic conditions  |f I. O. Dolganova, I. M. Dolganov, E. N. Ivashkina, A. Vladesku 
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330 |a The aim of the present paper is to increase the efficiency of low-temperature gas separation plant with use of simulation dynamic model. The paper analyzes the main processes occurring at the installation and performs the results of model verification. In addition, the technological scheme of natural low-temperature gas separation and operating parameters of one of the existing installations were considered. A non-stationary mathematical model of the chemical-technological system of low-temperature gas separation was developed. Due to the unsteady mathematical model, it became possible to estimate the time spent on the transient phenomena, as well as to choose the rate of low-temperature separation control parameters change, depending on the technological mode. Eventually, the calculations show how it is possible to avoid the instability of plant operation upset conditions at the workplace. The field of the developed model application is oil and gas industry and also higher education institutions. This software can be used to test the stability of both existing and projected low-temperature gas separation plants. 
461 |t Petroleum Science and Technology 
463 |t Vol. 35, № 12  |v [P. 1263-1269]  |d 2017 
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610 1 |a газы 
610 1 |a разделение газов 
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701 1 |a Dolganova  |b I. O.  |c chemist  |c Associate Scientist of Tomsk Polytechnic University, postgraduate student, candidate of technical Sciences  |f 1988-  |g Irena Olegovna  |3 (RuTPU)RU\TPU\pers\31271  |9 15449 
701 1 |a Dolganov  |b I. M.  |c Chemical Engineer  |c Associate Professor of Tomsk Polytechnic University, Candidate of Technical Sciences  |f 1987-  |g Igor Mikhailovich  |3 (RuTPU)RU\TPU\pers\32216  |9 16216 
701 1 |a Ivashkina  |b E. N.  |c Chemical Engineer  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1983-  |g Elena Nikolaevna  |3 (RuTPU)RU\TPU\pers\31275  |9 15453 
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