| 000 | 04113nla2a2200541 4500 | ||
|---|---|---|---|
| 001 | 639500 | ||
| 005 | 20231030040321.0 | ||
| 035 | _a(RuTPU)RU\TPU\network\3986 | ||
| 035 | _aRU\TPU\network\3985 | ||
| 090 | _a639500 | ||
| 100 | _a20150313a2014 k y0engy50 ba | ||
| 101 | 0 | _aeng | |
| 105 | _ay z 100zy | ||
| 135 | _adrcn ---uucaa | ||
| 181 | 0 | _ai | |
| 182 | 0 | _ab | |
| 200 | 1 |
_aEffect of Feed Composition Changing at Naphtha Catalytic Reforming Unit Due to Involvement of Gasoline Fraction Obtained by Diesel Fuels Hydrodewaxing into the Processing _fN. S. Belinskaya [et al.] |
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| 203 |
_aText _celectronic |
||
| 300 | _aTitle screen | ||
| 320 | _a[References: р. 270 (11 tit.)] | ||
| 330 | _aOne of the primary products of hydrodewaxing process is stable gasoline, which is characterized by low octane number on the one hand. On the other hand, it contains a significant amount of iso-paraffins (on average 45% wt.) and naphthenes (on average 25% wt.), which are reagents in the naphtha catalytic reforming process primary reactions. Feasibility of stable gasoline obtained by means of diesel fuel catalytic hydrodewaxing process involving into the processing at the naphtha catalytic reforming unit has been estimated using naphtha catalytic reforming mathematical model. Technological scheme of stable gasoline from hydrodewaxing unit supply to the reforming unit is presented. Naphtha catalytic reforming and diesel fuels hydrodewaxing processes resource efficiency increases by 15–20% due to rise in catalytic reforming feed source. | ||
| 333 | _aРежим доступа: по договору с организацией-держателем ресурса | ||
| 461 | 0 |
_0(RuTPU)RU\TPU\network\3889 _tProcedia Chemistry |
|
| 463 | 0 |
_0(RuTPU)RU\TPU\network\3890 _tVol. 10 : Chemistry and Chemical Engineering in XXI century _oXV International Scientific Conference dedicated to Professor L.P. Kulyov, 26-29 May 2014, Tomsk, Russia _fNational Research Tomsk Polytechnic University (TPU) _v[P. 267-270] _d2014 |
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| 610 | 1 | _aэлектронный ресурс | |
| 610 | 1 | _aтруды учёных ТПУ | |
| 610 | 1 | _aкаталитическая гидродепарафинизация | |
| 610 | 1 | _aгидродепарафинизация | |
| 610 | 1 | _aнефти | |
| 610 | 1 | _aкаталитический риформинг | |
| 610 | 1 | _aматематические модели | |
| 610 | 1 | _aкомбикорма | |
| 610 | 1 | _aбензиновые фракции | |
| 610 | 1 | _acatalytic hydrodewaxing | |
| 610 | 1 | _anaphtha catalytic reforming | |
| 610 | 1 | _amathematical model | |
| 610 | 1 | _afeed composition | |
| 610 | 1 | _agasoline fraction | |
| 701 | 1 |
_aBelinskaya _bN. S. _cchemist _cEngineer of Tomsk Polytechnic University _gNatalia Sergeevna _2stltpush _3(RuTPU)RU\TPU\pers\31267 |
|
| 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 |
_aIvashkina _bE. N. _cchemist-technologist _cAssociate Professor of Tomsk Polytechnic University, Candidate of technical science _f1983- _gElena Nikolaevna _2stltpush _3(RuTPU)RU\TPU\pers\31275 |
|
| 701 | 1 |
_aFrantsina _bE. V. _cChemical-technologist _cAssociate Professor of Tomsk Polytechnic University, Candidate of technical sciences _f1985- _gEvgeniya Vladimirovna _2stltpush _3(RuTPU)RU\TPU\pers\32193 |
|
| 701 | 1 |
_aSilko _bG. Yu. _cchemist _cassistant of Tomsk Polytechnic University _f1990- _gGalina Yurievna _2stltpush _3(RuTPU)RU\TPU\pers\35979 |
|
| 712 | 0 | 2 |
_aНациональный исследовательский Томский политехнический университет (ТПУ) _bИнститут природных ресурсов (ИПР) _bКафедра химической технологии топлива и химической кибернетики (ХТТ) _h105 _2stltpush _3(RuTPU)RU\TPU\col\18665 |
| 801 | 2 |
_aRU _b63413507 _c20161228 _gRCR |
|
| 856 | 4 | _uhttp://dx.doi.org/10.1016/j.proche.2014.10.044 | |
| 856 | 4 | _uhttp://earchive.tpu.ru/handle/11683/35503 | |
| 942 | _cCF | ||