High efficient separation of olefin from fluid catalytic cracking naphtha: Separation mechanism and universal simulation method

被引:13
|
作者
Zhang, Yuhao [1 ]
Zhao, Liang [1 ]
Chen, Feng [1 ]
Wang, Yongtao [1 ]
Gao, Jinsen [1 ]
Cao, Liyuan [1 ]
Wang, Hui [2 ]
Xu, Chunming [1 ]
机构
[1] China Univ Petr, State Key Lab Heavy Oil Proc, 18 Fuxue Rd, Beijing 102249, Peoples R China
[2] Univ Saskatchewan, Saskatoon, SK, Canada
基金
中国国家自然科学基金;
关键词
FCC naphtha; liquid-liquid equilibrium; molecular refining; olefin separation; simulation; AROMATIC EXTRACTION; HYDROGENATION; 1-HEXENE; BENZENE; SULFIDE; SOLVENT;
D O I
10.1002/aic.17153
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The fluid catalytic cracking (FCC) naphtha critical component-oriented separation process is an efficient method to produce ultra-low-sulfur (<10 mu g/g) gasoline with minimal loss of octane number (<1 RON). However, the product quality is highly dependent on the structure of the components of FCC naphtha. Aromatics and thiophene sulfides without a methyl side chain favor the separation of olefin. The major impulse of olefin separation is the solvent-induced dipole of aromatics or thiophene sulfides, leading to a "Plane-to-Plane" combination between the solvent and aromatics or thiophene sulfides, accompanied by a steric hindrance due to their side chains. This condition resulted in 2-3 times greater theta of benzene and thiophene compared with that of toluene and 3-methylthiophene. In addition, an improved non-random two-liquid model was proposed based on the above results, and a simulation method for FCC naphtha solvent extraction process was established. The calculation results accorded well with industry data.
引用
收藏
页数:12
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