Alkylation desulfurization of FCC gasoline over organic-inorganic heteropoly acid catalyst

被引:22
作者
Yu, Feng-Li [1 ]
Wang, Qing-Yu [1 ]
Yuan, Bing [1 ]
Xie, Cong-Xia [1 ]
Yu, Shi-Tao [2 ]
机构
[1] Qingdao Univ Sci & Technol, Coll Chem & Mol Engn, State Key Lab Base Ecochem Engn, Qingdao 266042, Peoples R China
[2] Qingdao Univ Sci & Technol, Coll Chem Engn, Qingdao 266042, Peoples R China
基金
中国国家自然科学基金;
关键词
Alkylation; Desulfurization; Thiophenic sulfides; Organic-inorganic heteropoly acids; FCC gasoline; SUPPORTED PHOSPHORIC-ACID; THIOPHENIC COMPOUNDS ALKYLATION; DEEP DESULFURIZATION; IONIC LIQUIDS; OXIDATIVE DESULFURIZATION; CRACKING GASOLINE; HYBRID CATALYSTS; MODEL; FUELS; DIBENZOTHIOPHENE;
D O I
10.1016/j.cej.2016.10.003
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The alkylation reaction of thiophenic sulfides with olefin in model fluid catalytic cracking (FCC) gasoline has been carried out over many kinds of organic-inorganic heteropoly acids, H3PW12O40, and AlPW12O40. The results have showed that organic-inorganic heteropoly acid [Bmim]H2PW12O40 exhibits the best catalytic activity for the alkylation of thiophene (T), 2-methyl thiophene (2-MT) and 3-methyl thiophene (3-MT). Many effect factors for the alkylation of thiophenic sulfides catalyzed by [Bmim]H2PW12O40 have been fully investigated. Under the optimal reaction conditions (the catalyst dosage 1 wt%, reaction temperature 120 degrees C, reaction time 40 min and the stirring rate 500 rpm), the conversions of T, 2-MT and 3-MT all can nearly reach up to 100%. [Bmim]H2PW12O40 has also exhibited good stability and recyclability. The conversions of thiophenic sulfides nearly remain unchanged during 11 recycles of [Bmim]H2PW12O40. Apparent reaction kinetics for the alkylation of thiophenic sulfides is studied. The alkylations of T, 2-MT and 3-MT all show the pseudo-first-order kinetic characteristics. The order of the reaction rate constants of three thiophenic sulfides is 2-MT > 3-MT > T. However, the calculated apparent activation energies of T, 2-MT and 3-MT are 62, 45.54 and 71.33 kJ/mol, respectively. So, the order of apparent activation energies is 3-MT > T > 2-MT. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:298 / 304
页数:7
相关论文
共 50 条
  • [31] FCC gasoline desulfurization using a ZSM-5 catalyst Interactive effects of sulfur containing species and gasoline components
    Jaimes, Lisette
    Badillo, Miguel
    de Lasa, Hugo
    FUEL, 2011, 90 (05) : 2016 - 2025
  • [32] Aromatization of FCC gasoline over modified HZSM-5 catalyst
    Zhao, L.
    Zhu, J.
    Wang, H. Y.
    Wei, M.
    Ma, J.
    Bai, Y. Z.
    PETROLEUM SCIENCE AND TECHNOLOGY, 2007, 25 (5-6) : 577 - 584
  • [33] Reactivity of olefins in the hydrodesulfurization of FCC gasoline over CoMo sulfide catalyst
    Toba, Makoto
    Miki, Yasuo
    Matsui, Takashi
    Harada, Masaru
    Yoshimura, Yuji
    APPLIED CATALYSIS B-ENVIRONMENTAL, 2007, 70 (1-4) : 542 - 547
  • [34] Effect of acid strength distribution on conversion of FCC gasoline over a ZSM-5 zeolite catalyst
    Zhihua Wu
    Shenglin Liu
    Sujuan Xie
    Qingxia Wang
    Xinhua Qian
    Longya Xu
    Reaction Kinetics and Catalysis Letters, 2005, 84 : 45 - 51
  • [35] Effect of acid strength distribution on conversion of FCC gasoline over a ZSM-5 zeolite catalyst
    Wu, ZH
    Liu, SL
    Xie, SJ
    Wang, QX
    Qian, XH
    Xu, LY
    REACTION KINETICS AND CATALYSIS LETTERS, 2005, 84 (01): : 45 - 51
  • [36] Hydrodesulfurization of FCC Gasoline over Ni-Mo Catalyst supported on MCM-41
    Jang, Chol Ryong
    Matei, Vasile
    Voicu, Viorel
    Borcea, Anca
    Ciuparu, Dragos
    REVISTA DE CHIMIE, 2014, 65 (12): : 1525 - 1529
  • [37] One-Step Oxidation-Desulfurization of FCC Gasoline Catalyzed by Tungstophosphoric Acid
    Li, J.
    Yang, L. N.
    Shen, J.
    PETROLEUM SCIENCE AND TECHNOLOGY, 2011, 29 (03) : 247 - 253
  • [38] Deep desulfurization of FCC gasoline by selective adsorption over nanosized zeolite-based adsorbents
    Zhilin Cheng
    Xuesong Liu
    Jiqing Lu
    Mengfei Luo
    Reaction Kinetics and Catalysis Letters, 2009, 97 : 1 - 6
  • [39] Preliminary study on reducing olefin content of FCC gasoline over cracking catalyst
    Liang, YM
    Yang, HF
    Liu, YF
    Xu, CM
    CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2003, 11 (06) : 740 - 742
  • [40] Preliminary Study on Reducing Olefin Content of FCC Gasoline over Cracking Catalyst
    梁咏梅
    杨海峰
    刘耀芳
    徐春明
    Chinese Journal of Chemical Engineering, 2003, (06) : 128 - 130