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
相关论文
共 50 条
  • [1] COMPOSITION OF NAPHTHA FROM FLUID CATALYTIC CRACKING
    MELPOLDER, FW
    BROWN, RA
    YOUNG, WS
    HEADINGTON, CE
    INDUSTRIAL AND ENGINEERING CHEMISTRY, 1952, 44 (05): : 1142 - 1146
  • [2] Modeling, simulation, and optimization for producing ultra-low sulfur and high-octane number gasoline by separation and conversion of fluid catalytic cracking naphtha
    Zhang, Yuhao
    Liu, Mengmeng
    Zhao, Liang
    Liu, Suxin
    Gao, Jinsen
    Xu, Chunming
    Ma, Mingzhi
    Meng, Qingfei
    Zhao, Liang (liangzhao@cup.edu.cn), 1600, Elsevier Ltd (299):
  • [3] Modeling, simulation, and optimization for producing ultra-low sulfur and high-octane number gasoline by separation and conversion of fluid catalytic cracking naphtha
    Zhang, Yuhao
    Liu, Mengmeng
    Zhao, Liang
    Liu, Suxin
    Gao, Jinsen
    Xu, Chunming
    Ma, Mingzhi
    Meng, Qingfei
    FUEL, 2021, 299
  • [4] Research on a Dual Solvent To Separate Olefin/Aromatic-Sulfide from Heavy Fluid Catalytic Cracking Naphtha
    Zhang, Yuhao
    Wang, Yongtao
    Chen, Feng
    Liu, Suxin
    Zhao, Liang
    Gao, Jinsen
    Hao, Tianzhen
    Xu, Chunming
    ENERGY & FUELS, 2018, 32 (03) : 4057 - 4064
  • [6] Magnetic separation of fluid catalytic cracking equilibrium catalyst
    Chen, J
    Xiang, FZ
    He, PB
    Guo, JX
    TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA, 1998, 8 (02) : 319 - 323
  • [7] Surface modification of zeolite Y and mechanism for reducing naphtha olefin formation in catalytic cracking reaction
    Liu, CH
    Gao, XH
    Zhang, ZD
    Zhang, HT
    Sun, SH
    Deng, YQ
    APPLIED CATALYSIS A-GENERAL, 2004, 264 (02) : 225 - 228
  • [8] Reaction mechanism and kinetic modeling of hydroisomerization and hydroaromatization of fluid catalytic cracking naphtha
    Chen, Zhiping
    Xu, Jian
    Fan, Yu
    Shi, Gang
    Bao, Xiaojun
    FUEL PROCESSING TECHNOLOGY, 2015, 130 : 117 - 126
  • [9] Desulfurization of Fluid Catalytic Cracking Naphtha by Extractive Distillation: A Universal Simulation Method Established Using the Universal Quasi-Chemical Functional Group Activity Coefficient Model
    Zhang, Yuhao
    Chen, Feng
    Zhao, Liang
    Gao, Jinsen
    Xu, Chunming
    Meng, Qingfei
    Liu, Xiangqi
    ENERGY & FUELS, 2021, 35 (07) : 6322 - 6331
  • [10] Olefin separation from FCC naphtha by dimethyl sulfoxide: Effect of structure on the separation and correlation of thermodynamic models
    Zhang, Yuhao
    Wang, Hui
    Zhao, Liang
    Gao, Jinsen
    Xu, Chunming
    SEPARATION AND PURIFICATION TECHNOLOGY, 2019, 228