Unsteady-State Mathematical Modeling of Hydrocarbon Feedstock Pyrolysis

被引:3
作者
Dolganov, Igor [1 ]
Bunaev, Ajur [1 ]
Dolganova, Irena [1 ]
机构
[1] Natl Res Tomsk Polytech Univ, Sch Earth Sci & Engn, Tomsk 634050, Russia
关键词
pyrolysis; hydrocarbon feedstock; unsteady-state; mathematical model; CATALYTIC PYROLYSIS; TEMPERATURE; KINETICS;
D O I
10.3390/pr8111394
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
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.
引用
收藏
页码:1 / 13
页数:13
相关论文
共 22 条
[1]   Recent advances on catalysts for improving hydrocarbon compounds in bio-oil of biomass catalytic pyrolysis [J].
Bhoi, P. R. ;
Ouedraogo, A. S. ;
Soloiu, V. ;
Quirino, R. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2020, 121
[2]   Influence of feedstock, catalyst, pyrolysis and hydrotreatment temperature on the composition of upgraded oils from intermediate pyrolysis [J].
Boscagli, Chiara ;
Morgano, Marco Tomasi ;
Raffelt, Klaus ;
Leibold, Hans ;
Grunwaldt, Jan-Dierk .
BIOMASS & BIOENERGY, 2018, 116 :236-248
[3]   Increasing the economic efficiency of gasoline production: Reducing the quality giveaway and simulation of catalytic cracking and compounding [J].
Chuzlov, Vyacheslav ;
Nazarova, Galina ;
Ivanchina, Emiliya ;
Ivashkina, Elena ;
Dolganova, Irena ;
Solopova, Anastasia .
FUEL PROCESSING TECHNOLOGY, 2019, 196
[4]   Modeling the multistage process of the linear alkylbenzene sulfonic acid manufacturing [J].
Dolganova, Irena ;
Ivanchina, Emilia ;
Dolganov, Igor ;
Ivashkina, Elena ;
Solopova, Anastasia .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2019, 147 :510-519
[5]   Alkylaromatics in Detergents Manufacture: Modeling and Optimizing Linear Alkylbenzene Sulfonation [J].
Dolganova, Irena ;
Dolganov, Igor ;
Ivanchina, Emiliya ;
Ivashkina, Elena .
JOURNAL OF SURFACTANTS AND DETERGENTS, 2018, 21 (01) :175-184
[6]   Hydrocarbon pyrolysis with a methane focus: A review on the catalytic effect and the coke production [J].
Fau, Guillaume ;
Gascoin, Nicolas ;
Steelant, Johan .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2014, 108 :1-11
[7]   Numerical study on the influences of heat and mass transfers on the pyrolysis of hydrocarbon fuel in mini-channel [J].
Feng, Yu ;
Jiang, Yuguang ;
Li, Xin ;
Zhang, Silong ;
Qin, Jiang ;
Cao, Yong ;
Huang, Hongyan .
APPLIED THERMAL ENGINEERING, 2017, 119 :650-658
[8]   Life cycle optimization for sustainable design and operations of hydrocarbon biorefinery via fast pyrolysis, hydrotreating and hydrocracking [J].
Gebreslassie, Berhane H. ;
Slivinsky, Maxim ;
Wang, Belinda ;
You, Fengqi .
COMPUTERS & CHEMICAL ENGINEERING, 2013, 50 :71-91
[9]   Influence of secondary reactions on heat transfer process during pyrolysis of hydrocarbon fuel under supercritical conditions [J].
Gong, Keyu ;
Cao, Yong ;
Feng, Yu ;
Liu, Shuyuan ;
Qin, Jiang .
APPLIED THERMAL ENGINEERING, 2019, 159
[10]   Mathematical modeling of multicomponent catalytic processes of petroleum refining and petrochemistry [J].
Ivanchina, Emiliya D. ;
Ivashkina, Elena N. ;
Dolganova, Irena O. ;
Belinskaya, Nataliya S. .
REVIEWS IN CHEMICAL ENGINEERING, 2021, 37 (01) :163-191