Complex modeling system for optimization of compounding process in gasoline pool to produce high-octane finished gasoline fuel

Research output: Contribution to journalArticle

17 Citations (Scopus)

Abstract

The process of gasoline compounding is a difficult multistage industrial technology. Octane number is a numerical equivalent of gasoline detonation resistance, the main operational characteristic of trade gasoline. Prediction of octane numbers of individual hydrocarbons was performed with calculations of dissociation energy of their molecules. In this paper, a new approach is proposed for optimization and prediction of the unit operation modes for processing of multicomponent hydrocarbon mixtures, based on a complex mathematical model that considers reactivities of hydrocarbons of wide gasoline fraction in the reforming, isomerization, and compounding processes. The accuracy of calculations is confirmed with huge massive of experimental data obtained from catalytic reforming, catalytic cracking (FCC), isomerization and alkylation units.

Original languageEnglish
Pages (from-to)194-205
Number of pages12
JournalChemical Engineering Journal
Volume282
DOIs
Publication statusPublished - 15 Dec 2015

Fingerprint

Gasoline
Hydrocarbons
hydrocarbon
Antiknock rating
Isomerization
industrial technology
modeling
prediction
Catalytic reforming
Catalytic cracking
Alkylation
Detonation
Reforming reactions
Mathematical models
Molecules
energy
octane
Processing
calculation

Keywords

  • Gasoline
  • Isomerization
  • Mathematical modeling
  • Octane number
  • Reforming

ASJC Scopus subject areas

  • Chemical Engineering(all)
  • Chemistry(all)
  • Industrial and Manufacturing Engineering
  • Environmental Chemistry

Cite this

@article{d53ccb240ce14ff5b4d0b1279657c391,
title = "Complex modeling system for optimization of compounding process in gasoline pool to produce high-octane finished gasoline fuel",
abstract = "The process of gasoline compounding is a difficult multistage industrial technology. Octane number is a numerical equivalent of gasoline detonation resistance, the main operational characteristic of trade gasoline. Prediction of octane numbers of individual hydrocarbons was performed with calculations of dissociation energy of their molecules. In this paper, a new approach is proposed for optimization and prediction of the unit operation modes for processing of multicomponent hydrocarbon mixtures, based on a complex mathematical model that considers reactivities of hydrocarbons of wide gasoline fraction in the reforming, isomerization, and compounding processes. The accuracy of calculations is confirmed with huge massive of experimental data obtained from catalytic reforming, catalytic cracking (FCC), isomerization and alkylation units.",
keywords = "Gasoline, Isomerization, Mathematical modeling, Octane number, Reforming",
author = "Ivanchina, {E. D.} and Maria Vladimirovna Kirgina and Nikita Vitalievich Chekantsev and Sakhnevich, {B. V.} and Sviridova, {E. V.} and Romanovskiy, {R. V.}",
year = "2015",
month = "12",
day = "15",
doi = "10.1016/j.cej.2015.03.014",
language = "English",
volume = "282",
pages = "194--205",
journal = "Chemical Engineering Journal",
issn = "1385-8947",
publisher = "Elsevier",

}

TY - JOUR

T1 - Complex modeling system for optimization of compounding process in gasoline pool to produce high-octane finished gasoline fuel

AU - Ivanchina, E. D.

AU - Kirgina, Maria Vladimirovna

AU - Chekantsev, Nikita Vitalievich

AU - Sakhnevich, B. V.

AU - Sviridova, E. V.

AU - Romanovskiy, R. V.

PY - 2015/12/15

Y1 - 2015/12/15

N2 - The process of gasoline compounding is a difficult multistage industrial technology. Octane number is a numerical equivalent of gasoline detonation resistance, the main operational characteristic of trade gasoline. Prediction of octane numbers of individual hydrocarbons was performed with calculations of dissociation energy of their molecules. In this paper, a new approach is proposed for optimization and prediction of the unit operation modes for processing of multicomponent hydrocarbon mixtures, based on a complex mathematical model that considers reactivities of hydrocarbons of wide gasoline fraction in the reforming, isomerization, and compounding processes. The accuracy of calculations is confirmed with huge massive of experimental data obtained from catalytic reforming, catalytic cracking (FCC), isomerization and alkylation units.

AB - The process of gasoline compounding is a difficult multistage industrial technology. Octane number is a numerical equivalent of gasoline detonation resistance, the main operational characteristic of trade gasoline. Prediction of octane numbers of individual hydrocarbons was performed with calculations of dissociation energy of their molecules. In this paper, a new approach is proposed for optimization and prediction of the unit operation modes for processing of multicomponent hydrocarbon mixtures, based on a complex mathematical model that considers reactivities of hydrocarbons of wide gasoline fraction in the reforming, isomerization, and compounding processes. The accuracy of calculations is confirmed with huge massive of experimental data obtained from catalytic reforming, catalytic cracking (FCC), isomerization and alkylation units.

KW - Gasoline

KW - Isomerization

KW - Mathematical modeling

KW - Octane number

KW - Reforming

UR - http://www.scopus.com/inward/record.url?scp=84947865924&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=84947865924&partnerID=8YFLogxK

U2 - 10.1016/j.cej.2015.03.014

DO - 10.1016/j.cej.2015.03.014

M3 - Article

VL - 282

SP - 194

EP - 205

JO - Chemical Engineering Journal

JF - Chemical Engineering Journal

SN - 1385-8947

ER -