Mathematical Modeling Sulfuric Acid Catalyzed Alkylation of Isobutane with Olefins

E. N. Ivashkina, E. D. Ivanchina, A. E. Nurmakanova, S. S. Boychenko, A. S. Ushakov, I. O. Dolganova

Research output: Contribution to journalArticle

5 Citations (Scopus)

Abstract

The article provides the results of applied mathematical model of sulfuric acid catalyzed alkylation of isobutane with olefins. It was shown that increasing the content of propylene in the feedstock to 2% leads to decrease in octane number of alkylate to 0.5-1.0 points. Alkylates produced from feedstock with less isobutane mass fraction have a smaller value of octane number. Using mathematic model it was determined that the main parameter influencing the acid activity in the alkylation process is the fresh acid concentration.

Original languageEnglish
Pages (from-to)81-86
Number of pages6
JournalProcedia Engineering
Volume152
DOIs
Publication statusPublished - 2016

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Antiknock rating
Alkylation
Sulfuric acid
Feedstocks
Olefins
Acids
Propylene
Mathematical models

Keywords

  • alkylate
  • mathematical modeling
  • octane number
  • optimization
  • sulfuric acid alkylation

ASJC Scopus subject areas

  • Engineering(all)

Cite this

Mathematical Modeling Sulfuric Acid Catalyzed Alkylation of Isobutane with Olefins. / Ivashkina, E. N.; Ivanchina, E. D.; Nurmakanova, A. E.; Boychenko, S. S.; Ushakov, A. S.; Dolganova, I. O.

In: Procedia Engineering, Vol. 152, 2016, p. 81-86.

Research output: Contribution to journalArticle

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AU - Boychenko, S. S.

AU - Ushakov, A. S.

AU - Dolganova, I. O.

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