| 000 | 03703nla2a2200541 4500 | ||
|---|---|---|---|
| 001 | 639471 | ||
| 005 | 20231030040320.0 | ||
| 035 | _a(RuTPU)RU\TPU\network\3957 | ||
| 035 | _aRU\TPU\network\3955 | ||
| 090 | _a639471 | ||
| 100 | _a20150313a2014 k y0engy50 ba | ||
| 101 | 0 | _aeng | |
| 105 | _ay z 100zy | ||
| 135 | _adrcn ---uucaa | ||
| 181 | 0 | _ai | |
| 182 | 0 | _ab | |
| 200 | 1 |
_aImproving the Efficiency of Dehydrogenation Catalyst Resource while Reducing the H[2] Gas Circulation Rat _fE. N. Ivashkina [et al.] |
|
| 203 |
_aText _celectronic |
||
| 300 | _aTitle screen | ||
| 320 | _a[References: р. 136 (15 tit.)] | ||
| 330 | _aIn the research the various ways of increasing the selectivity of the dehydrogenation process and reducing the intensity of coke formation have been studied. All results were received by means of the mathematical model of the dehydrogenation process with the calculating technique of optimal water flow. The main conclusion consists in the fact that the decrease in molar ratio H[2]/feed leads to increasing the catalyst deactivation by coke. It can be partially compensated by increasing the supplied water flow to the reactor to 13-14 l/h instead of 9-10 l/h at the end of cycle. Reducing the life of the catalyst to 270-290 days even at an increased water flow is determined by the intensity of the coking reactions. However, the economic feasibility of operating in such condition causes a considerable increase in production of LAB to 181-186 t/day. | ||
| 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. 127-136] _d2014 |
|
| 610 | 1 | _aэлектронный ресурс | |
| 610 | 1 | _aтруды учёных ТПУ | |
| 610 | 1 | _aэффективность | |
| 610 | 1 | _aкатализаторы | |
| 610 | 1 | _aдегидрирование | |
| 610 | 1 | _aкокс | |
| 610 | 1 | _aматематические модели | |
| 610 | 1 | _aкоксование | |
| 610 | 1 | _adehydrogenation | |
| 610 | 1 | _aH2-containing gas | |
| 610 | 1 | _adeactivation | |
| 610 | 1 | _amodelling | |
| 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 |
_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 |
_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 |
_aPlatonov _bV. V. |
|
| 701 | 1 |
_aGlik _bP. A. |
|
| 701 | 1 |
_aVolkov _bM. A. |
|
| 701 | 1 |
_aKolmogorova _bV. А. |
|
| 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.2014.10.023 | |
| 856 | 4 | _uhttp://earchive.tpu.ru/handle/11683/35483 | |
| 942 | _cCF | ||