Effect of zeolite NTsVM in catalyst on hydroconversion parameters of vacuum distillate

M. V. Landau, V. A. Vyazkov, L. N. Alekseenko, O. V. Vinogradova, B. K. Nefedov, L. D. Konoval'chikov, A. B. Gorshtejn, G. N. Matveeva, V. M. Kurganov

Research output: Contribution to journalArticlepeer-review

Abstract

The influence of NTsVM high-silica zeolite addition on catalytic properties of traditional catalysts of hydrocracking on the basis of Y type zeolite was studied. The catalysts were tested in the process of vacuum distillates hydrocracking 350-500°C, which contained 1.8 % (mass) sulfur, 0.09 % (mass) nitrogen and 52 % (vol.) aromatic hydrocarbons under the pressure of 5 MPa and in the temperature range of 340-420°C. It is ascertained that, when monozeolite Al-Ni-Mo-catalysts are used, Y rare earth zeolite surpasses NTsVM considerably as to splitting activity in the process of hydrocracking of vacuum distillate. In the composition of bizeolite Al-Ni-Mo-catalyst the splitting activity of NTsVM zeolite at 400-420 °C, especially in petrol yield terms, is much higher than that of Y rare earth one, i.e. effect of superadditivity of splitting activity of Y rare earth and NTsVM zeolites in Al-Ni-Mo-matrix is observed.

Original languageEnglish
Pages (from-to)25-26
Number of pages2
JournalKhimiya i Tekhnologiya Topliv i Masel
Issue number3
StatePublished - 1 Mar 1991
Externally publishedYes

ASJC Scopus subject areas

  • Chemistry (all)
  • Chemical Engineering (all)
  • Fuel Technology
  • Energy Engineering and Power Technology

Fingerprint

Dive into the research topics of 'Effect of zeolite NTsVM in catalyst on hydroconversion parameters of vacuum distillate'. Together they form a unique fingerprint.

Cite this