| 000 | 03755nlm1a2200445 4500 | ||
|---|---|---|---|
| 001 | 664396 | ||
| 005 | 20231030041928.0 | ||
| 035 | _a(RuTPU)RU\TPU\network\35580 | ||
| 090 | _a664396 | ||
| 100 | _a20210412a2018 k y0engy50 ba | ||
| 101 | 0 | _aeng | |
| 102 | _aSK | ||
| 135 | _adrcn ---uucaa | ||
| 181 | 0 | _ai | |
| 182 | 0 | _ab | |
| 200 | 1 |
_aGeneral algorithm for efficiency evaluation of multi-column distillation flowsheets _fM. A. Samborskaya, I. A. Gryaznova, A. V. Volf, E. V. Popok |
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| 203 |
_aText _celectronic |
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| 300 | _aTitle screen | ||
| 320 | _a[References: p. 889 (10 tit.)] | ||
| 330 | _aThe paper shows the development and application of a general algorithm for efficiency evaluation (AEE) of distillation sequences. The algorithm provided consideration of energy efficiency, flowsheet structure, and product specifications. In Aspen HYSYSTM, we developed two “first principle” models of crude oil distillation units with and without heat integration. We have applied the AEE to compare the effectiveness of their performance for different types of oil. The effectiveness was higher for heat integrated unit, so its model was adopted as basic. Six alternative retrofit flowsheet models were developed for the purposes of preliminary optimization. Preliminary optimization was a combination of predesign optimization of unit flowsheet structure and apparatus design to create the optimal crude oil distillation unit and to provide the process flexibility in respect of feed flowrate and oil quality. Parametrical optimization was performed for all configurations of flowsheet structure. Maximum feed flowrates and the product yields were defined for all flowsheet structures. Relative total investments for retrofits of the basic flowsheet were estimated. They consider the cost of distillation columns, the internal device, pumps, heat exchangers, piping. AEE application to all retrofit flowsheets allows designing effective and relatively inexpensive refinery unit. | ||
| 333 | _aСвободный доступ из сети Интернет | ||
| 461 | _tPetroleum and Coal | ||
| 463 |
_tVol. 60, iss. 5 _v[P. 884-889] _d2018 |
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| 610 | 1 | _aэлектронный ресурс | |
| 610 | 1 | _aтруды учёных ТПУ | |
| 610 | 1 | _acrude oil distillation unit | |
| 610 | 1 | _amulti-column distillation sequences | |
| 610 | 1 | _ageneral algorithm for efficiency evaluation | |
| 610 | 1 | _apreliminary optimization | |
| 610 | 1 | _aоптимальные режимы | |
| 610 | 1 | _aparametrical optimization | |
| 610 | 1 | _athermodynamic efficiency | |
| 701 | 1 |
_aSamborskaya _bM. A. _cChemical Engineer _cAssociate Professor of Tomsk Polytechnic University, Candidate of chemical sciences _f1960- _gMarina Anatolievna _2stltpush _3(RuTPU)RU\TPU\pers\31290 |
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| 701 | 1 |
_aGryaznova _bI. A. _cchemist _cassistant of Tomsk Polytechnic University _f1989- _gInga Andreevna _2stltpush _3(RuTPU)RU\TPU\pers\35930 |
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| 701 | 1 |
_aVolf _bA. V. _cChemical Engineer _cAssistant of Tomsk Polytechnic University, master training _f1986- _gAndrey Viktorovich _2stltpush _3(RuTPU)RU\TPU\pers\33901 |
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| 701 | 1 |
_aPopok _bE. V. _cChemical Engineer _cAssociate Professor of Tomsk Polytechnic University, Candidate of technical sciences _f1987- _gEvgeniy Vladimirovich _2stltpush _3(RuTPU)RU\TPU\pers\33869 |
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| 712 | 0 | 2 |
_aНациональный исследовательский Томский политехнический университет _bИнженерная школа природных ресурсов _bОтделение химической инженерии _h8085 _2stltpush _3(RuTPU)RU\TPU\col\23513 |
| 801 | 2 |
_aRU _b63413507 _c20210412 _gRCR |
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| 856 | 4 | _uhttps://www.vurup.sk/wp-content/uploads/2018/09/PC_x_2018_Samborskaya_75.pdf | |
| 942 | _cCF | ||