Unsteady-State Mathematical Modeling of Hydrocarbon Feedstock Pyrolysis

Hydrocarbon feedstock pyrolysis is an important method for obtaining monomers that are then used to produce various polymer materials. During this process, a mixture of hydrocarbons is heated at a high temperature and in the absence of oxygen. Because of the side reactions of polymerization and poly...

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Main Authors: Igor Dolganov, Ajur Bunaev, Irena Dolganova
Format: Article
Language:English
Published: MDPI AG 2020-10-01
Series:Processes
Subjects:
Online Access:https://www.mdpi.com/2227-9717/8/11/1394
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spelling doaj-66609e37989f4fff9bbb20d1396515912020-11-25T04:02:09ZengMDPI AGProcesses2227-97172020-10-0181394139410.3390/pr8111394Unsteady-State Mathematical Modeling of Hydrocarbon Feedstock PyrolysisIgor Dolganov0Ajur Bunaev1Irena Dolganova2School of Earth Sciences & Engineering, National Research Tomsk Polytechnic University, 634050 Tomsk, RussiaSchool of Earth Sciences & Engineering, National Research Tomsk Polytechnic University, 634050 Tomsk, RussiaSchool of Earth Sciences & Engineering, National Research Tomsk Polytechnic University, 634050 Tomsk, RussiaHydrocarbon feedstock pyrolysis is an important method for obtaining monomers that are then used to produce various polymer materials. During this process, a mixture of hydrocarbons is heated at a high temperature and in the absence of oxygen. Because of the side reactions of polymerization and polycondensation, coke products are formed and settle on the inner walls of the coil. This decreases the technical efficiency of the hydrocarbon pyrolysis furnace during its operation, making the process unsteady. In the present research, we developed an unsteady-state mathematical model of hydrocarbon feedstock pyrolysis in order to improve the monitoring, forecasting, and optimization of this technological process. This model can calculate the rate of coke deposition along the length of the coil, considering the technological parameters and the composition of the supplied raw materials (the calculated value of coke deposition rate equals 0.01 mm/day). It was shown that with an increase in the propane/butane ratio from 4/1 to 1/4 mol/mol, the ethylene concentration decreases from 3.45 mol/L to 3.35 mol/L.https://www.mdpi.com/2227-9717/8/11/1394pyrolysishydrocarbon feedstockunsteady-statemathematical model
collection DOAJ
language English
format Article
sources DOAJ
author Igor Dolganov
Ajur Bunaev
Irena Dolganova
spellingShingle Igor Dolganov
Ajur Bunaev
Irena Dolganova
Unsteady-State Mathematical Modeling of Hydrocarbon Feedstock Pyrolysis
Processes
pyrolysis
hydrocarbon feedstock
unsteady-state
mathematical model
author_facet Igor Dolganov
Ajur Bunaev
Irena Dolganova
author_sort Igor Dolganov
title Unsteady-State Mathematical Modeling of Hydrocarbon Feedstock Pyrolysis
title_short Unsteady-State Mathematical Modeling of Hydrocarbon Feedstock Pyrolysis
title_full Unsteady-State Mathematical Modeling of Hydrocarbon Feedstock Pyrolysis
title_fullStr Unsteady-State Mathematical Modeling of Hydrocarbon Feedstock Pyrolysis
title_full_unstemmed Unsteady-State Mathematical Modeling of Hydrocarbon Feedstock Pyrolysis
title_sort unsteady-state mathematical modeling of hydrocarbon feedstock pyrolysis
publisher MDPI AG
series Processes
issn 2227-9717
publishDate 2020-10-01
description Hydrocarbon feedstock pyrolysis is an important method for obtaining monomers that are then used to produce various polymer materials. During this process, a mixture of hydrocarbons is heated at a high temperature and in the absence of oxygen. Because of the side reactions of polymerization and polycondensation, coke products are formed and settle on the inner walls of the coil. This decreases the technical efficiency of the hydrocarbon pyrolysis furnace during its operation, making the process unsteady. In the present research, we developed an unsteady-state mathematical model of hydrocarbon feedstock pyrolysis in order to improve the monitoring, forecasting, and optimization of this technological process. This model can calculate the rate of coke deposition along the length of the coil, considering the technological parameters and the composition of the supplied raw materials (the calculated value of coke deposition rate equals 0.01 mm/day). It was shown that with an increase in the propane/butane ratio from 4/1 to 1/4 mol/mol, the ethylene concentration decreases from 3.45 mol/L to 3.35 mol/L.
topic pyrolysis
hydrocarbon feedstock
unsteady-state
mathematical model
url https://www.mdpi.com/2227-9717/8/11/1394
work_keys_str_mv AT igordolganov unsteadystatemathematicalmodelingofhydrocarbonfeedstockpyrolysis
AT ajurbunaev unsteadystatemathematicalmodelingofhydrocarbonfeedstockpyrolysis
AT irenadolganova unsteadystatemathematicalmodelingofhydrocarbonfeedstockpyrolysis
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