| 000 | 03032nlm1a2200433 4500 | ||
|---|---|---|---|
| 001 | 661904 | ||
| 005 | 20231030041803.0 | ||
| 035 | _a(RuTPU)RU\TPU\network\32975 | ||
| 090 | _a661904 | ||
| 100 | _a20200319a2020 k y0engy50 ba | ||
| 101 | 0 | _aeng | |
| 102 | _aSK | ||
| 135 | _adrcn ---uucaa | ||
| 181 | 0 | _ai | |
| 182 | 0 | _ab | |
| 200 | 1 |
_aMathematical Modeling of the Gasoline Manufacturing _fI. M. Dolganov, V. A. Chuzlov, A. Yu. Tyumentsev, I. O. Dolganova |
|
| 203 |
_aText _celectronic |
||
| 300 | _aTitle screen | ||
| 320 | _a[References: 9 tit.] | ||
| 330 | _aIn the process of gasoline preparation, various products of hydrocarbon processing processes are used, such as catalytic reforming, isomerization, hydrocracking, catalytic cracking, liquid-phase alkylation of isobutane with olefins, as well as additives such as MTBE. Optimization of the commercial types of gasoline preparing process is a complex multi-factor task, including the stages of the catalytic processing of hydrocarbon raw materials into high-octane components and the stage of commercial gasoline components, mixing. This requires taking into account the non-additivity of the properties of commercial products. Determining the ratios of the mixing components, considering changes in the composition and properties of hydrocarbon feeds for processing, as well as the optimal technological conditions at the stages of catalytic processing of feeds, will reduce the cost of commercial products by reducing their quality stock. | ||
| 333 | _aСвободный доступ из сети Интернет | ||
| 461 | _tPetroleum and Coal | ||
| 463 |
_tVol. 62, iss. 1 _v[P. 92-97] _d2020 |
||
| 610 | 1 | _aэлектронный ресурс | |
| 610 | 1 | _aтруды учёных ТПУ | |
| 610 | 1 | _amathematical modeling | |
| 610 | 1 | _amixing | |
| 610 | 1 | _acatalytic reforming | |
| 610 | 1 | _aматематическое моделирование | |
| 610 | 1 | _aсмешивание | |
| 610 | 1 | _aреформирование | |
| 701 | 1 |
_aDolganov _bI. M. _cChemical Engineer _cEngineer of Tomsk Polytechnic University _f1987- _gIgor Mikhailovich _2stltpush _3(RuTPU)RU\TPU\pers\32216 |
|
| 701 | 1 |
_aChuzlov _bV. A. _cchemist _cengineer of Tomsk Polytechnic University _f1991- _gVyacheslav Alekseevich _2stltpush _3(RuTPU)RU\TPU\pers\33898 |
|
| 701 | 1 |
_aTyumentsev _bA. Yu. _gAnton Yurjevich |
|
| 701 | 1 |
_aDolganova _bI. O. _cchemist _cAssociate Scientist of Tomsk Polytechnic University, postgraduate student, candidate of technical Sciences _f1988- _gIrena Olegovna _2stltpush _3(RuTPU)RU\TPU\pers\31271 |
|
| 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 _c20200319 _gRCR |
|
| 856 | 4 | _uhttps://www.vurup.sk/wp-content/uploads/2020/02/PC-X_-Dolganov-214.pdf | |
| 942 | _cCF | ||