Reaction mechanism study of catalytic conversion of light straight-run naphtha to light olefins over micro-spherical HZSM-5 zeolite catalyst

被引:2
|
作者
Asfha, Hagos Birhane [1 ]
Berta, Ashenafi Hailu [1 ,3 ]
Kang, Nayoung [1 ]
Yun, Danim [1 ]
Park, Jaedeuk [1 ]
Park, Yong-Ki [1 ,2 ]
Kim, Kiwoong [1 ,2 ]
机构
[1] Korea Res Inst Chem Technol KRICT, Ctr Low Carbon Chem Proc, Gajeong Ro 141, Daejeon 34114, South Korea
[2] Univ Sci & Technol UST, Adv Mat & Chem Engn, Gajeong Ro 217, Daejeon 34113, South Korea
[3] Adama Sci & Technol Univ, Sch Mech Chem & Mat Engn, POB 1888, Adama, Ethiopia
关键词
Catalytic cracking; Naphtha cracking; Hydrocarbons; ZSM-5; catalyst; Reaction mechanism; N-BUTANE CRACKING; THERMAL-DECOMPOSITION; ORGANIC-COMPOUNDS; REACTION PATHWAYS; KINETIC-MODEL; FREE-RADICALS; ZSM-5; TRANSFORMATION; HYDROCARBONS; INTERCONVERSION;
D O I
10.1016/j.cattod.2023.114376
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Catalytic conversion of naphtha has attracted attention as an alternative method to the conventional thermal cracking to produce light olefins in an environment-friendly and energy-efficient way. In this work, a reaction mechanism study of light straight run naphtha cracking over micro-spherical catalyst containing HZSM-5 was systematically investigated using single hydrocarbon feeds, and the straight run naphtha itself. The identified reaction pathways from the single feeds along with the naphtha experimental data have been utilized to investigate reaction pathways of the naphtha conversion reactions. The experimental tests were carried out in the temperature ranges of 450-650 degrees C and space-times of 0.3-1.5 min using a fixed bed micro-reactor in isothermal and isobaric conditions. The product distribution for the naphtha feed shows that light paraffins and light olefins are the primary products, which are products of monomolecular protolytic cracking of the paraffin components of the naphtha feed. The olefin interconversion reactions illustrated that oligomerization and cracking by beta-scission dominate the secondary reactions of naphtha catalytic cracking conversions. The experiments con-ducted on cyclohexane, cyclohexene and n-hexane single feeds revealed that BTX formation proceeds through the formation of C6-C8 naphthenes, and C6-C8 cyclo-olefinic intermediates. Low temperatures and space times pro-mote the selectivity to propylene while the selectivity of ethylene increases with temperature. The degree of thermal cracking (DTC) illustrated that thermal cracking is considerable only for temperatures of higher than 550 degrees C.
引用
收藏
页数:10
相关论文
共 50 条
  • [1] Reaction network of the chloromethane conversion into light olefins using a HZSM-5 zeolite catalyst
    Gamero, Monica
    Valle, Beatriz
    Castano, Pedro
    Aguayo, Andres T.
    Bilbao, Javier
    JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2018, 61 : 427 - 436
  • [2] Catalytic pyrolysis of straight-run naphtha to light olefins: Experiment and molecular-level kinetic modeling study
    Dang, Falu
    Chen, Zhengyu
    Sun, Zhiguo
    Wang, Gang
    Zhang, Linzhou
    Gao, Zhao
    Lian, Jingcun
    Liu, Yupei
    Liu, Meijia
    Zhang, Zhongdong
    Liu, Chaowei
    CHEMICAL ENGINEERING JOURNAL, 2024, 497
  • [3] Reaction Kinetic Model of Naphtha-Methanol Catalytic Conversion for Light Olefins over HZSM-5 Based on Structure-Oriented Lumping
    Cheng, Qitong
    Shen, Benxian
    Liu, Jichang
    Qin, Xinglong
    Ye, Lei
    Xing, Biao
    ENERGY & FUELS, 2021, 35 (13) : 10786 - 10795
  • [4] A new approach for gasoline upgrading: Coupling octane enhancement and desulfurization of heavy straight-run naphtha over Ni/HZSM-5 catalyst
    Sharifi, Khashayar
    Halladj, Rouein
    Royaee, Sayed Javid
    Nasr, Mohammad Reza Jafari
    CATALYSIS COMMUNICATIONS, 2018, 115 : 31 - 35
  • [5] Effect of zeolite crystal size on the catalytic performance of HZSM-5 in the reaction of methanol to light olefins
    Zhang, Su-Hong
    Zhang, Bian-Ling
    Gao, Zhi-Xian
    Han, Yi-Zhuo
    Ranliao Huaxue Xuebao/Journal of Fuel Chemistry and Technology, 2010, 38 (04): : 483 - 489
  • [6] Kinetic model for the reaction of DME to olefins over a HZSM-5 zeolite catalyst
    Perez-Uriarte, Paula
    Ateka, Ainara
    Aguayo, Andres T.
    Gayubo, Ana G.
    Bilbao, Javier
    CHEMICAL ENGINEERING JOURNAL, 2016, 302 : 801 - 810
  • [7] Deactivation kinetics for the conversion of dimethyl ether to olefins over a HZSM-5 zeolite catalyst
    Perez-Uriarte, Paula
    Ateka, Ainara
    Gayubo, Ana G.
    Cordero-Lanzac, Tomas
    Aguayo, Andres T.
    Bilbao, Javier
    CHEMICAL ENGINEERING JOURNAL, 2017, 311 : 367 - 377
  • [8] Pt-Zn/HZSM-5 as a highly selective catalyst for the Co-aromatization of methane and light straight run naphtha
    Jarvis, Jack
    He, Peng
    Wang, Aiguo
    Song, Hua
    FUEL, 2019, 236 : 1301 - 1310
  • [9] Steam catalytic cracking of naphtha over Ce/SBA-15 and Ce/HZSM-5 for production of light olefins
    Keyvanloo, Kamyar
    Mohamadalizadeh, Ali
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2013, 246
  • [10] Synthesis of zirconium and cerium over HZSM-5 catalysts for light olefins production from naphtha
    Momayez, Forough
    Darian, Jafar Towfighi
    Sendesi, Seyedeh Mahboobeh Teimouri
    JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2015, 112 : 135 - 140