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100 _a20200625a2020 k y0engy50 ba
101 0 _aeng
102 _aCH
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181 0 _ai
182 0 _ab
200 1 _aConversion of the Propane–Butane Fraction into Arenes on MFI Zeolites Modified by Zinc Oxide and Activated by Low-Temperature Plasma
_fV. I. Erofeev, S. N. Dzhalilova, M. V. Erofeev [et al.]
203 _aText
_celectronic
300 _aTitle screen
320 _a[References: 23 tit.]
330 _aThe effect of modification of MFI zeolite 1–5 wt.% ZnO activated by plasma on acid and catalytic properties in the conversion of the propane–butane fraction into arenes was investigated. The high-silica zeolites with silicate module 45 were synthesized from alkaline alumina–silica gels in the presence of an ‘X-oil’ organic structure-forming additive. The modification of the zeolite with zinc was carried out by impregnating the zeolite granules in the H-form with an aqueous solution of Zn(NO3)2. The obtained zeolites were characterized by X-ray phase analysis and IR spectroscopy. It is shown that the synthesized zeolites belong to the high-silica MFI zeolites. The study of microporous zeolite-containing catalysts during the conversion of C3-C4 alkanes to aromatic hydrocarbons made it possible to establish that the highest yield of aromatic hydrocarbons is observed on zeolite catalysts modified with 1 and 3% ZnO and amount to 63.7 and 64.4% at 600 °C, respectively, which is 7.7–8.4% more than on the original zeolite. The preliminary activation of microporous zeolites modified with 1–5% ZnO and plasma leads to an increase in the yield of aromatic hydrocarbons from the propane–butane fraction; the maximum yield of arenes is observed in zeolite catalysts modified with 1 and 3% ZnO and activated by plasma, amounting to 64.9 and 65.5% at 600 °C, respectively, which is 8.9–9.5% more than on the initial zeolite. The activity of the zeolite catalysts modified by ZnO and activated by plasma show good agreement with their acid properties. Activation of the zeolites modified by 1 and 3% ZnO and plasma leads to an increase in the concentration of the weak acid sites of the catalyst to 707 and 764 mmol/g in comparison with plasma-inactivated 1 and 3% ZnO/ZKE-XM catalysts at 626 and 572 mmol/g, respectively.
461 _tMolecules
463 _tVol. 25, iss. 11
_v[2704, 16 p.]
_d2020
610 1 _aтруды учёных ТПУ
610 1 _aэлектронный ресурс
610 1 _aMFI zeolite
610 1 _amodification
610 1 _azinc oxide
610 1 _aplasma activation
610 1 _aacidity
610 1 _apropane–butane fraction
610 1 _aconversion
610 1 _aarenes
610 1 _aцеолиты
610 1 _aмодификация
610 1 _aоксид цинка
610 1 _aпреобразования
701 1 _aErofeev
_bV. I.
_cspecialist in the field of oil and gas business
_cProfessor of Tomsk Polytechnic University, Doctor of technical sciences
_f1946-
_gVladimir Ivanovich
_2stltpush
_3(RuTPU)RU\TPU\pers\32197
701 1 _aDzhalilova
_bS. N.
_cspecialist in the field of petroleum engineering
_cAssistant of the Department of Tomsk Polytechnic University
_f1990-
_gSofiya Nasibullaevna
_2stltpush
_3(RuTPU)RU\TPU\pers\45678
701 1 _aErofeev
_bM. V.
_gMikhail Vladimirovich
701 1 _aRipenko
_bV. S.
_gVasily Sergeevich
701 1 _aReschetilowski
_bW. P.
_gWladimir Petrovich
712 0 2 _aНациональный исследовательский Томский политехнический университет
_bИнженерная школа природных ресурсов
_bОтделение нефтегазового дела
_h8084
_2stltpush
_3(RuTPU)RU\TPU\col\23546
801 2 _aRU
_b63413507
_c20210318
_gRCR
856 4 0 _uhttp://earchive.tpu.ru/handle/11683/64812
856 4 0 _uhttps://doi.org/10.3390/molecules25112704
942 _cCF