| 000 | 03485nlm1a2200565 4500 | ||
|---|---|---|---|
| 001 | 666790 | ||
| 005 | 20231030042048.0 | ||
| 035 | _a(RuTPU)RU\TPU\network\37994 | ||
| 035 | _aRU\TPU\network\37101 | ||
| 090 | _a666790 | ||
| 100 | _a20220127a2021 k y0engy50 ba | ||
| 101 | 0 | _aeng | |
| 102 | _aCH | ||
| 135 | _adrcn ---uucaa | ||
| 181 | 0 | _ai | |
| 182 | 0 | _ab | |
| 200 | 1 |
_aA Model of Catalytic Cracking: Product Distribution and Catalyst Deactivation Depending on Saturates, Aromatics and Resins Content in Feed _fG. Yu. Nazarova, E. N. Ivashkina, E. D. Ivanchina [et al.] |
|
| 203 |
_aText _celectronic |
||
| 300 | _aTitle screen | ||
| 320 | _a[References: 40 tit.] | ||
| 330 | _aThe problems of catalyst deactivation and optimization of the mixed feedstock become more relevant when the residues are involved as a catalytic cracking feedstock. Through numerical and experimental studies of catalytic cracking, we optimized the composition of the mixed feedstock in order to minimize the catalyst deactivation by coke. A pure vacuum gasoil increases the yields of the wet gas and the gasoline (56.1 and 24.9 wt%). An increase in the ratio of residues up to 50% reduces the gasoline yield due to the catalyst deactivation by 19.9%. However, this provides a rise in the RON of gasoline and the light gasoil yield by 1.9 units and 1.7 wt% Moreover, the ratio of residue may be less than 50%, since the conversion is limited by the regenerator coke burning ability. | ||
| 338 |
_bРоссийский фонд фундаментальных исследований _d21-53-10004 |
||
| 338 |
_bРоссийский научный фонд _d19-71-10015 |
||
| 461 | _tCatalysts | ||
| 463 |
_tVol. 11, iss. 6 _v[701, 17 p.] _d2021 |
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| 610 | 1 | _aэлектронный ресурс | |
| 610 | 1 | _aтруды учёных ТПУ | |
| 610 | 1 | _avacuum gasoil | |
| 610 | 1 | _aresidues | |
| 610 | 1 | _acoke | |
| 610 | 1 | _acatalyst deactivation | |
| 610 | 1 | _akinetics | |
| 610 | 1 | _amathematical model | |
| 610 | 1 | _aвакуумные газойли | |
| 610 | 1 | _aкокс | |
| 610 | 1 | _aдезактивация | |
| 610 | 1 | _aкатализаторы | |
| 610 | 1 | _aкинетика | |
| 610 | 1 | _aматематические модели | |
| 701 | 1 |
_aNazarova _bG. Yu. _cchemist _cassistant of Tomsk Polytechnic University _f1990- _gGalina Yurievna _2stltpush _3(RuTPU)RU\TPU\pers\35588 |
|
| 701 | 1 |
_aIvashkina _bE. N. _cChemical Engineer _cProfessor of Tomsk Polytechnic University, Doctor of sciences _f1983- _gElena Nikolaevna _2stltpush _3(RuTPU)RU\TPU\pers\31275 |
|
| 701 | 1 |
_aIvanchina _bE. D. _cchemist _cProfessor of Tomsk Polytechnic University, Doctor of technical sciences _f1951- _gEmilia Dmitrievna _2stltpush _3(RuTPU)RU\TPU\pers\31274 |
|
| 701 | 1 |
_aVosmerikov _bA. V. _gAleksandr Vladimirovich |
|
| 701 | 1 |
_aVosmerikova _bL. N. _gLyudmila Nikolaevna |
|
| 701 | 1 |
_aAntonov _bA. V. _cchemist _cengineer of Tomsk Polytechnic University _f1996- _gArtem Viktorovich _2stltpush _3(RuTPU)RU\TPU\pers\47444 |
|
| 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 _c20230117 _gRCR |
|
| 856 | 4 | _uhttp://earchive.tpu.ru/handle/11683/70744 | |
| 856 | 4 | _uhttps://doi.org/10.3390/catal11060701 | |
| 942 | _cCF | ||