000			02237naa2a2200433 4500
001			584046
005			20231030032954.0
035			_a(RuTPU)RU\TPU\prd\285297
035			_aRU\TPU\prd\285296
090			_a584046
100			_a20190821a2019 k y0engy50 ba
101	0		_aeng
102			_aRU
135			_adrcn ---uucaa
181		0	_ai
182		0	_ab
200	1		_aStudy of the influence of feedstock of the processed raw materials atnaphtha catalytic reforming and isomerization _fV. Chabanenkov
203			_aText _celectronic
215			_a1 файл (287 Кб)
225	1		_aСоциологические науки
230			_aЭлектронные текстовые данные (1 файл : 287 Кб)
300			_aTitle screen
320			_a[References: 2 tit.]
330			_aA mathematical method of optimization of naphtha catalytic reforming and isomerization of industrial unit A100 ofPavlodar oil refinery combined with separation unit B300S was proposed. In order to achieve the required quality of theproducts of the splitter column for the C6 hydrocarbon content in the heavy gasoline fraction and the C7+ hydrocarboncontent in the light gasoline fraction, the research was carried out to optimize the process parameters. The obtained datawere checked for adequacy and confirmed by the simulation results presented for different modes of operation ofisomerization reactors and columns. The data can be used to solve real technological problems arising in production.
461		1	_0(RuTPU)RU\TPU\prd\225573 _x2312-2978 _tJournal of Economics and Social Sciences _oelectronic scientific journal _d2012-
463		1	_0(RuTPU)RU\TPU\prd\285293 _t№ 14 _v[4 p.] _d2019
610	1		_aэлектронный ресурс
610	1		_aтруды ученых ТПУ
610	1		_aseparation of raw materials
610	1		_amathematical simulation
610	1		_aisomerization
610	1		_areforming
610	1		_asplitter
700		1	_aChabanenkov _bV. _gVladimir
712	0	2	_aEngineering school of natural resources, Tomsk Polytechnic University
801		1	_aRU _b63413507 _c20090623 _gPSBO
801		2	_aRU _b63413507 _c20190903 _gPSBO
856	4	0	_uhttp://earchive.tpu.ru/handle/11683/55736
942			_cBK