Increase of efficiency isopropylbenzene manufacturing with use of integrated mathematical models

書誌詳細
Parent link:Petroleum and Coal
Vol. 58, iss. 2.— 2016.— [P. 155-160]
団体著者: Национальный исследовательский Томский политехнический университет Институт природных ресурсов Кафедра химической технологии топлива и химической кибернетики
その他の著者: Chudinova A. A. Alyona Anatoljevna, Buchatskaya N. I. Nadezhda, Podgorniy V. V. Vladimir, Gavrikov А. А. Aleksey Alekseevich, Ivashkina E. N. Elena Nikolaevna, Dolganova I. O. Irena Olegovna
要約:Title screen
A mathematical model of isopropyl benzene obtaining reactor process on chloroaluminum catalyst was developed. With use of HYSYS software a computer model of benzene with propylene alkylation technological scheme was created. Integration of computer models allowed carrying out calculations to determine technological modes of production, allowing to obtain a marketable product of higher quality. It was shown that increasing of isopropylbenzene concentration in commercial product to 99.9% by weight can be achieved by implementing of sequence separation in distillation columns due to redistribution of ethylbenzene and n-butyl benzene loads.
Свободный доступ из сети Интернет
言語:英語
出版事項: 2016
主題:
オンライン・アクセス:http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_2_2016_chudinova_415.pdf
フォーマット: 電子媒体 図書の章
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=652329

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300 |a Title screen 
320 |a [References: p. 159-160 (16 tit.)] 
330 |a A mathematical model of isopropyl benzene obtaining reactor process on chloroaluminum catalyst was developed. With use of HYSYS software a computer model of benzene with propylene alkylation technological scheme was created. Integration of computer models allowed carrying out calculations to determine technological modes of production, allowing to obtain a marketable product of higher quality. It was shown that increasing of isopropylbenzene concentration in commercial product to 99.9% by weight can be achieved by implementing of sequence separation in distillation columns due to redistribution of ethylbenzene and n-butyl benzene loads. 
333 |a Свободный доступ из сети Интернет 
461 |t Petroleum and Coal 
463 |t Vol. 58, iss. 2  |v [P. 155-160]  |d 2016 
610 1 |a электронный ресурс 
610 1 |a труды учёных ТПУ 
610 1 |a эффективность 
610 1 |a изопропилбензол 
610 1 |a математические модели 
701 1 |a Chudinova  |b A. A.  |g Alyona Anatoljevna 
701 1 |a Buchatskaya  |b N. I.  |g Nadezhda 
701 1 |a Podgorniy  |b V. V.  |g Vladimir 
701 1 |a Gavrikov  |b А. А.  |c Chemical engineer  |c Senior Lecturer of Tomsk Polytechnic University  |f 1977-  |g Aleksey Alekseevich  |3 (RuTPU)RU\TPU\pers\35243  |9 18508 
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 
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 
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