Kinetics of light alkane aromatization on high - siliceous zeolite catalysts

V. L. Vorob'ev, A. V. Kravtsov, Yu I. Koshelev, N. V. Usheva, E. I. Cmetanina, O. E. Mojzes

Research output: Contribution to journalArticle

Abstract

Kinetic regularities of light alkane aromatization on gallium - containing zeolite catalyst of ZSM-5 type have been investigated. The kinetic model of complex multicomponent process describing the regularities of hydrocarbons and hydrogen conversion in this process has been developed. The influence of different process parameters (temperature, pressure, volume rate) on its kinetic regularities has been established. The conditions providing conversion and process selectivity increase have been determined. .

Original languageEnglish
Pages (from-to)306-313
Number of pages8
JournalNeftekhimiya
Volume32
Issue number4
Publication statusPublished - Jul 1992

Fingerprint

Aromatization
Zeolites
Alkanes
Paraffins
Catalysts
Kinetics
Gallium
Hydrocarbons
Hydrogen
Temperature

ASJC Scopus subject areas

  • Fuel Technology

Cite this

Vorob'ev, V. L., Kravtsov, A. V., Koshelev, Y. I., Usheva, N. V., Cmetanina, E. I., & Mojzes, O. E. (1992). Kinetics of light alkane aromatization on high - siliceous zeolite catalysts. Neftekhimiya, 32(4), 306-313.

Kinetics of light alkane aromatization on high - siliceous zeolite catalysts. / Vorob'ev, V. L.; Kravtsov, A. V.; Koshelev, Yu I.; Usheva, N. V.; Cmetanina, E. I.; Mojzes, O. E.

In: Neftekhimiya, Vol. 32, No. 4, 07.1992, p. 306-313.

Research output: Contribution to journalArticle

Vorob'ev, VL, Kravtsov, AV, Koshelev, YI, Usheva, NV, Cmetanina, EI & Mojzes, OE 1992, 'Kinetics of light alkane aromatization on high - siliceous zeolite catalysts', Neftekhimiya, vol. 32, no. 4, pp. 306-313.
Vorob'ev VL, Kravtsov AV, Koshelev YI, Usheva NV, Cmetanina EI, Mojzes OE. Kinetics of light alkane aromatization on high - siliceous zeolite catalysts. Neftekhimiya. 1992 Jul;32(4):306-313.
Vorob'ev, V. L. ; Kravtsov, A. V. ; Koshelev, Yu I. ; Usheva, N. V. ; Cmetanina, E. I. ; Mojzes, O. E. / Kinetics of light alkane aromatization on high - siliceous zeolite catalysts. In: Neftekhimiya. 1992 ; Vol. 32, No. 4. pp. 306-313.
@article{b8d06fd829ea4bebbf14ea9fc3e1472a,
title = "Kinetics of light alkane aromatization on high - siliceous zeolite catalysts",
abstract = "Kinetic regularities of light alkane aromatization on gallium - containing zeolite catalyst of ZSM-5 type have been investigated. The kinetic model of complex multicomponent process describing the regularities of hydrocarbons and hydrogen conversion in this process has been developed. The influence of different process parameters (temperature, pressure, volume rate) on its kinetic regularities has been established. The conditions providing conversion and process selectivity increase have been determined. .",
author = "Vorob'ev, {V. L.} and Kravtsov, {A. V.} and Koshelev, {Yu I.} and Usheva, {N. V.} and Cmetanina, {E. I.} and Mojzes, {O. E.}",
year = "1992",
month = "7",
language = "English",
volume = "32",
pages = "306--313",
journal = "Neftekhimiya",
issn = "0028-2421",
publisher = "Izdatel'stvo Nauka",
number = "4",

}

TY - JOUR

T1 - Kinetics of light alkane aromatization on high - siliceous zeolite catalysts

AU - Vorob'ev, V. L.

AU - Kravtsov, A. V.

AU - Koshelev, Yu I.

AU - Usheva, N. V.

AU - Cmetanina, E. I.

AU - Mojzes, O. E.

PY - 1992/7

Y1 - 1992/7

N2 - Kinetic regularities of light alkane aromatization on gallium - containing zeolite catalyst of ZSM-5 type have been investigated. The kinetic model of complex multicomponent process describing the regularities of hydrocarbons and hydrogen conversion in this process has been developed. The influence of different process parameters (temperature, pressure, volume rate) on its kinetic regularities has been established. The conditions providing conversion and process selectivity increase have been determined. .

AB - Kinetic regularities of light alkane aromatization on gallium - containing zeolite catalyst of ZSM-5 type have been investigated. The kinetic model of complex multicomponent process describing the regularities of hydrocarbons and hydrogen conversion in this process has been developed. The influence of different process parameters (temperature, pressure, volume rate) on its kinetic regularities has been established. The conditions providing conversion and process selectivity increase have been determined. .

UR - http://www.scopus.com/inward/record.url?scp=0026890707&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=0026890707&partnerID=8YFLogxK

M3 - Article

AN - SCOPUS:0026890707

VL - 32

SP - 306

EP - 313

JO - Neftekhimiya

JF - Neftekhimiya

SN - 0028-2421

IS - 4

ER -