Way to increase the energy efficiency of the distillation unit at ethylbenzene manufacturing technology

Sonraí bibleagrafaíochta
Parent link:Petroleum and Coal
Vol. 61, iss. 2.— 2019.— [P. 402-406]
Údar corparáideach: Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии
Rannpháirtithe: Khlebnikova E. S. Elena Sergeevna, Ivashkina E. N. Elena Nikolaevna, Volf A. V. Andrey Viktorovich, Dolganova I. O. Irena Olegovna
Achoimre:Title screen
The object of research is the installation of rectification columns for benzene, ethylbenzene, and polyalkylbenzenes. The purpose of this work is an optimization of rectification technological modes and energy efficiency increasing of distillation in the technology of ethylbenzene production by replacing of the used in reboilers vapor at 4 MPa by vapor at 2 MPa. The proposed optimization option of therectification unit is efficient since the implementation of the proposed technical solution will be achieved using Vapor 2 with increased efficiency of the process, namely a reduction of vapor consumption. The total consumption of vapor after the upgrade will be 2.751 Gcal / hour, which is 2168 Gcal per year less than the current vapor load.
Teanga:Béarla
Foilsithe / Cruthaithe: 2019
Ábhair:
Rochtain ar líne:https://www.vurup.sk/wp-content/uploads/2019/03/PC-X-2019_Dolganova_8.pdf
Formáid: Leictreonach Caibidil leabhair
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=660547
Cur síos
Achoimre:Title screen
The object of research is the installation of rectification columns for benzene, ethylbenzene, and polyalkylbenzenes. The purpose of this work is an optimization of rectification technological modes and energy efficiency increasing of distillation in the technology of ethylbenzene production by replacing of the used in reboilers vapor at 4 MPa by vapor at 2 MPa. The proposed optimization option of therectification unit is efficient since the implementation of the proposed technical solution will be achieved using Vapor 2 with increased efficiency of the process, namely a reduction of vapor consumption. The total consumption of vapor after the upgrade will be 2.751 Gcal / hour, which is 2168 Gcal per year less than the current vapor load.