Pre-design Optimization of Crude Oil Distillation Flowsheet
| Parent link: | Procedia Chemistry Vol. 15 : Chemistry and Chemical Engineering in XXI century (CCE 2015).— 2015.— [P. 134-142] |
|---|---|
| Hovedforfatter: | |
| Institution som forfatter: | |
| Andre forfattere: | , |
| Summary: | Title screen Several first principle models of crude oil distillation units were developed in Aspen Plus{TM} for purposes of pre-design optimization of flowsheet structure and apparatus design and choice of the optimal variant of distillation to provide the process flexibility in respect to flowrate of crude oil and oil quality. The developed models consider air temperature and type of crude oil. The two-column flowsheet of crude oil distillation is adopted as basic. The sum of the capital investments and operation costs per year was estimated for the basic flowsheet. Stepwise increasing of crude oil flowrate is used to determine "weak points" of the flowsheet and estimate maximum oil flowrate. Parametrical optimization was performed for each step. The alternative upgrading flowsheets were developed to increase operation effectiveness in a wide range of crude oil flowrates. The optimization criterion was developed to evaluate the relative efficiency of the alternative distillation unit flowsheets. The optimization criterion was a ratio of average annual revenue from the sale of petroleum products to the total costs (capital investments and operational costs) with restrictions on the product quality. The way of re-equipment of the column internals was chosen as a preferable variant. Режим доступа: по договору с организацией-держателем ресурса |
| Sprog: | engelsk |
| Udgivet: |
2015
|
| Fag: | |
| Online adgang: | http://dx.doi.org/10.1016/j.proche.2015.10.022 http://earchive.tpu.ru/handle/11683/15044 |
| Format: | Electronisk Book Chapter |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=645335 |
MARC
| LEADER | 00000nla2a2200000 4500 | ||
|---|---|---|---|
| 001 | 645335 | ||
| 005 | 20231220104533.0 | ||
| 035 | |a (RuTPU)RU\TPU\network\10419 | ||
| 035 | |a RU\TPU\network\10418 | ||
| 090 | |a 645335 | ||
| 100 | |a 20151216a2015 k y0engy50 ba | ||
| 101 | 0 | |a eng | |
| 105 | |a y z 100zy | ||
| 135 | |a drcn ---uucaa | ||
| 181 | 0 | |a i | |
| 182 | 0 | |a b | |
| 200 | 1 | |a Pre-design Optimization of Crude Oil Distillation Flowsheet |f M. A. Samborskaya, I. A. Gryaznova, A. V. Volf | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: р. 142 (10 tit.)] | ||
| 330 | |a Several first principle models of crude oil distillation units were developed in Aspen Plus{TM} for purposes of pre-design optimization of flowsheet structure and apparatus design and choice of the optimal variant of distillation to provide the process flexibility in respect to flowrate of crude oil and oil quality. The developed models consider air temperature and type of crude oil. The two-column flowsheet of crude oil distillation is adopted as basic. The sum of the capital investments and operation costs per year was estimated for the basic flowsheet. Stepwise increasing of crude oil flowrate is used to determine "weak points" of the flowsheet and estimate maximum oil flowrate. Parametrical optimization was performed for each step. The alternative upgrading flowsheets were developed to increase operation effectiveness in a wide range of crude oil flowrates. The optimization criterion was developed to evaluate the relative efficiency of the alternative distillation unit flowsheets. The optimization criterion was a ratio of average annual revenue from the sale of petroleum products to the total costs (capital investments and operational costs) with restrictions on the product quality. The way of re-equipment of the column internals was chosen as a preferable variant. | ||
| 333 | |a Режим доступа: по договору с организацией-держателем ресурса | ||
| 461 | 0 | |0 (RuTPU)RU\TPU\network\3889 |t Procedia Chemistry | |
| 463 | 0 | |0 (RuTPU)RU\TPU\network\10324 |t Vol. 15 : Chemistry and Chemical Engineering in XXI century (CCE 2015) |o XVI International Scientific Conference dedicated to Professor L.P. Kulyov, 25-29 May 2015, Tomsk, Russia |f National Research Tomsk Polytechnic University (TPU) ; ed. E. I. Korotkova |v [P. 134-142] |d 2015 | |
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a сырые нефти | |
| 610 | 1 | |a дистилляция | |
| 610 | 1 | |a оптимизация | |
| 610 | 1 | |a технологические схемы | |
| 610 | 1 | |a параметрическая оптимизация | |
| 610 | 1 | |a перегонка | |
| 610 | 1 | |a схемы | |
| 700 | 1 | |a Samborskaya |b M. A. |c Chemical Engineer |c Associate Professor of Tomsk Polytechnic University, Candidate of chemical sciences |f 1960- |g Marina Anatolievna |3 (RuTPU)RU\TPU\pers\31290 |9 15468 | |
| 701 | 1 | |a Gryaznova |b I. A. |c chemist |c assistant of Tomsk Polytechnic University |f 1989- |g Inga Andreevna |3 (RuTPU)RU\TPU\pers\35930 | |
| 701 | 1 | |a Volf |b A. V. |c chemical-technologist |c Assistant of Tomsk Polytechnic University, master training |f 1986- |g Andrey Viktorovich |3 (RuTPU)RU\TPU\pers\33901 | |
| 712 | 0 | 2 | |a Национальный исследовательский Томский политехнический университет (ТПУ) |b Институт природных ресурсов (ИПР) |b Кафедра химической технологии топлива и химической кибернетики (ХТТ) |3 (RuTPU)RU\TPU\col\18665 |
| 801 | 2 | |a RU |b 63413507 |c 20161121 |g RCR | |
| 856 | 4 | |u http://dx.doi.org/10.1016/j.proche.2015.10.022 | |
| 856 | 4 | |u http://earchive.tpu.ru/handle/11683/15044 | |
| 942 | |c CF | ||