Thermal/catalytic cracking of hydrocarbons for the production of olefins; a state-of-the-art review III: Process modeling and simulation

被引:111
作者
Fakhroleslam, Mohammad [1 ]
Sadrameli, Seyed Mojtaba [1 ]
机构
[1] Tarbiat Modares Univ, Fac Chem Engn, Proc Engn Dept, Tehran, Iran
关键词
Olefins; Hydrocarbons; Thermal cracking; Production; Mathematical modeling; Simulation; NAPHTHA THERMAL-CRACKING; MULTIOBJECTIVE OPERATION OPTIMIZATION; CONVECTION HEAT-TRANSFER; TRANSFER LINE EXCHANGER; STEAM CRACKING; COKE FORMATION; COUPLED SIMULATION; DYNAMIC OPTIMIZATION; COMPUTER-GENERATION; PYROLYSIS REACTIONS;
D O I
10.1016/j.fuel.2019.04.127
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Ethylene and propylene are among the light olefins which are the main building blocks in the petrochemical and chemical industry. They are produced from thermal/catalytic cracking of gaseous and liquid hydrocarbons and recently from methanol. This paper continues the two review articles published before entitled thermal and catalytic cracking of hydrocarbons for the production of light olefins. In the last two review articles, the processes and the kinetics of thermal and catalytic cracking have been discussed in details. This paper reviews the mathematical modeling and simulation of the olefin plants including mechanisms and kinetic models, CFD simulations, rigorous models, and abstract models.
引用
收藏
页码:553 / 566
页数:14
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