Increase of efficiency isopropylbenzene manufacturing with use of integrated mathematical models

Alyona A. Chudinova, Nadezhda I. Buchatskaya, Vladimir V. Podgorniy, Aleksey A. Gavrikov, Elena N. Ivashkina, Irena O. Dolganova

Research output: Contribution to journalArticle

1 Citation (Scopus)

Abstract

A mathematical model of isopropyl benzene obtaining reactor process on chloroaluminum catalyst was developed. With use of HYSYS software a computer model of benzene with propylene alkylation technological scheme was created. Integration of computer models allowed carrying out calculations to determine technological modes of production, allowing to obtain a marketable product of higher quality. It was shown that increasing of isopropylbenzene concentration in commercial product to 99.9% by weight can be achieved by implementing of sequence separation in distillation columns due to redistribution of ethylbenzene and n-butyl benzene loads.

Original languageEnglish
Pages (from-to)155-160
Number of pages6
JournalPetroleum and Coal
Volume58
Issue number2
Publication statusPublished - 1 Jan 2016

Fingerprint

Benzene
Mathematical models
Ethylbenzene
Distillation columns
Alkylation
Propylene
Catalysts

Keywords

  • Alkylation
  • Isopropylbenzene
  • Mathematical modeling
  • Rectification

ASJC Scopus subject areas

  • Energy(all)

Cite this

Increase of efficiency isopropylbenzene manufacturing with use of integrated mathematical models. / Chudinova, Alyona A.; Buchatskaya, Nadezhda I.; Podgorniy, Vladimir V.; Gavrikov, Aleksey A.; Ivashkina, Elena N.; Dolganova, Irena O.

In: Petroleum and Coal, Vol. 58, No. 2, 01.01.2016, p. 155-160.

Research output: Contribution to journalArticle

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